Electrolytic method utilizing carbon dioxide and high-nickel-content anodes to produce desired nanocarbon allotropes

Abstract

Embodiments of the present disclosure relate to methods and apparatus for producing carbon nanomaterial (CNM) products, which may include carbon nanotubes and various other allotropes of nanocarbon. The methods and apparatus use consumable carbon dioxide (CO2) and renewable carbonate electrolyte as reactants in an electrolysis reaction to make CNTs. In some embodiments of the present disclosure, the operating conditions of the electrolysis reaction may be varied to produce CNM products with even greater generation of a desired allotrope of nanocarbon or a desired combination of two or more allotropes.

Description

[Technical Field]

[0001]

[0001] Cross-reference to related applications This application claims priority to U.S. Provisional Patent Application No. 63 / 282,985, filed on 24 November 2021, and U.S. Provisional Patent Application No. 63 / 300,499, filed on 18 January 2022, both of which are incorporated herein by reference in their entirety.

[0002]

[0002] This disclosure generally relates to the production of carbon nanomaterials. More specifically, this disclosure relates to methods and apparatus for producing carbon nanomaterials of various allotropes using electrolysis. [Background technology]

[0003]

[0003] Carbon nanotubes (CNTs) have the highest tensile strength (strength of 93,900 MPa) ever measured among any material. Multiwalled CNTs consist of concentric walls of cylindrical graphene sheets. Graphene has sp² layers with a thickness of approximately 0.335 nm, which corresponds to the thickness of a single carbon atom. 2 It is a two-dimensional honeycomb structured material formed by a monolayer of hybridized orbital carbon atoms. Graphite, nanotubes, and fullerenes can be formed by graphene, for example, by winding and lamination.

[0004]

[0004] Carbon nanomaterials (CNMs) containing graphene structures possess many useful properties, including high strength, high electrical conductivity, high thermal conductivity, durability, hardness, flexibility, and lubricity. They can also be used as catalysts and are chemically modified. These useful properties mean that the applications of CNTs are steadily expanding. For example, low (typically <<1%) concentrations of CNTs in structural materials can increase the strength of a range of structural materials, such as cement, steel, plastics, wood, and aluminum. Since each of these materials can have a high carbon footprint, carbon composites with increased strength, or other useful properties that require no, little, or little high-footprint materials, can dramatically reduce the carbon footprint. Other applications that utilize the useful properties of carbon nanomaterials include: cables or wires, electric vehicles, sports equipment, medical applications, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage, and water treatment.

[0005]

[0005] The known process by which CNTs are produced is chemical vapor deposition (CVD). However, CVD of CNTs is expensive—current estimates are between $100K and $600K per ton of CNTs produced, and CVD has a high carbon footprint. [Overview of the Initiative] [Problems that the invention aims to solve]

[0006]

[0006] In addition to chemical vapor deposition (CVD), electrolytic reactions using carbon dioxide (CO2) and lithium-carbonate electrolytes are also known processes for producing CNTs. These electrolytic reactions may use an electrolytic potential of less than 1 volt to decompose CO2 in a molten lithium-carbonate solution to produce uniform CNT and carbon nanofiber (CNF) products with high Coulomb efficiency. CO2 from the atmosphere is an isotope ( 13C) As confirmed by tracking, it can be directly converted to CNTs. Electrolytic separation of CO2 in molten lithium carbonate can be brought about as direct carbon recovery and as conversion from air, without CO2 pre-concentration or with exhaust gas CO2 or with concentrated CO2. However, the products of known electrolytic reactions may contain various components in various physical forms, also called nanostructures, morphs, or allotropes. Furthermore, products prepared with similar electrolyte operating parameters may result in various physical forms and various related properties of various physical forms. [Means for solving the problem]

[0007]

[0007] Embodiments of the present disclosure relate to methods and apparatus for producing carbon nanomaterial products (CNMs) containing various carbon allotropes, including carbon nanotubes (CNTs), graphite carbon, nanobamboo, conical carbon nanofibers, nanopearl carbon, coated CNTs, nanoonions, hollow nanoonions, nanoflowers, nanodragons, branch and trunk CNTs (nanotrees), nanobelts, nanorods, long and / or linear CNTs, high aspect ratio CNTs, thin CNTs, and densely packed macroscopic assemblies of CNTs, linear CNTs, nanosponges, and nanowebs. The methods and apparatus utilize carbon dioxide (CO2) as a reactant in an electrolytic reaction to produce these various carbon nanomaterials (CNMs). Embodiments of the present disclosure provide a wide range of controlled electrolytic methods and apparatus to selectively provide CNM products having high purity of one or more of the desired allotropes.

[0008]

[0008] Some embodiments of the present disclosure relate to a method for producing a CNM product. The method includes: heating a carbonate electrolyte to obtain a molten carbonate electrolyte; positioning the molten carbonate electrolyte between the anode and cathode in an electrolytic cell; applying an electric current to the cathode and anode in the electrolytic cell; and selecting one or more of the following operating parameters: the composition or configuration of the cathode, the composition or configuration of the anode, additives to be added to the electrolyte, aging the electrolyte, current density, increasing or decreasing the current density, and the time for which the current is applied so that the CNM product contains a higher relative amount of the desired allotrope. Examples of desired allotropes include, but are not limited to, carbon nanotubes (CNTs), graphite carbon, nanobamboo, conical carbon nanofibers, nanopearl carbon, coated CNTs, nanoonions, hollow nanoonions, nanoflowers, nanodragons, branched and trunk CNTs (nanotrees), nanobelts, nanorods, long and / or linear CNTs, high aspect ratio CNTs, thin CNTs, macroscopic assemblies of CNTs, or combinations thereof. The method further includes the step of collecting CNM products from the cathode.

[0009]

[0009] The methods and apparatus use carbon dioxide (CO2) as a reactant in an electrolytic reaction to produce various carbon allotropes. Embodiments of the present disclosure provide a wide range of controlled electrolytic methods and apparatus to selectively provide CNM products having one or more of these allotropes in high purity. In the absence of sufficient CO2, the carbonate electrolyte becomes the carbon source and is consumed. The CO2 may originate from an external gas, or if there is temporarily insufficient external CO2 to support the desired electrolytic reaction, the carbon source may originate from the decomposition of the carbonate. Without adhering to any theory, carbonate decomposition involves the decomposition of CO2 and O 2 CO3 with oxides such as 2- This follows an imbalance. In the latter case, the construction of this oxide acts as a reserve to remove excess CO2 when it becomes available.

[0010]

[0010] In some embodiments of the present disclosure, the method may be modified to dope a CNM product containing a desired allotrope internally. The doped allotrope has atoms of the doping component directly incorporated into the chemical structure of the doped allotrope, thereby giving the doped allotrope new or enhanced physical and / or chemical properties when compared to an undoped allotrope.

[0011]

[0011] In some embodiments of the present disclosure, the method may be modified to produce a CNM product that responds to an external magnetic field and contains a desired allotrope internally. The magnetic allotrope can incorporate atoms of a magnetic material internally using a mechanism facilitated by chemoaddition and / or carbide, so that the magnetic allotrope can move along the magnetic field when located in or near a source of the magnetic field.

[0012]

[0012] Without being bound by any particular theory, some embodiments of this disclosure provide a novel method for synthesizing new allotropes of carbon by molten carbonate electrolysis using the greenhouse gas CO2 as a reactant. Beyond the conventional world of diamond, graphite, and buckyballs, a vast array of unique nanocarbon structures exists and has been discovered. Until recently, CO2 was thought to be non-reactive. Herein, we show that CO2 can be converted, among other things, into distinct nanobamboo, nanopearl, nanodragon, solid and hollow nanoonion, nanotree, nanorod, nanobelt, and nanoflower allotropes of carbon. The ability to produce these allotropes in high purity by simple electrolysis—similar to the aluminum-producing decomposition of aluminum oxide but instead by the decomposition of carbon dioxide—opens up a number of inexpensive and unique materials that have the potential to offer new high-strength properties, new electrical properties, new thermal properties, new flexibility, new charge storage properties, new lubricity, and new robustness. Commercial production techniques for nanocarbons are chemical vapor deposition (CVD), which is 10 to 100 times more expensive and generally requires metal-organic reactants, resulting in a highly positive carbon footprint rather than a negative one. Various nanocarbon allotropes were electrochemically prepared by varying anode and cathode compositions and structures, electrolyte compositions, pre-electrolytic treatment (aging), and current increases and current densities.

[0013]

[0013] Some embodiments of the present disclosure relate to a first method for producing a CNM product. The method includes: heating an electrolyte medium to obtain a molten electrolyte medium; positioning the molten electrolyte medium between a high-nickel-content anode and cathode of an electrolytic cell; introducing a carbon source into the electrolytic cell; applying an electric current to the cathode and anode of the electrolytic cell; and collecting the CNM product from the cathode. In these embodiments of the first method, the CNM product includes a minimum relative amount of at least 70% by weight compared to the total weight of the CNM product, of a desired allotrope selected from the group consisting of carbon nanotubes (CNTs) of a desired length, curled CNTs, conical carbon nanofibers, nanobamboo, hollow nanoonions, and nanotrees.

[0014]

[0014] Some embodiments of the present disclosure relate to a first method in which the anode is made of substantially pure nickel, the cathode contains copper, the desired allotrope is a CNT of a desired length, and the desired length is between about 30 μm and about 60 μm.

[0015]

[0015] Some embodiments of the present disclosure relate to a first method, further comprising the step of adding an iron-containing salt to an electrolyte medium or a molten electrolyte medium.

[0016]

[0016] In some embodiments of the present disclosure, an iron-containing salt is added in an amount between about 0.01% by weight and about 5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome C, and the current is about 0.1 A / cm². 2 ~about 0.2A / cm 2 The present invention relates to a first method, wherein a current density between is applied, and the desired allotrope is a CNT of a desired length, the desired length being between approximately 50 μm and approximately 100 μm.

[0017]

[0017] Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01 wt% and about 5 wt% based on the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome A, the desired allotrope is CNTs of a desired length, and the desired length is between about 20 μm and about 80 μm.

[0018]

[0018] Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01 wt% and about 5 wt% based on the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome C, and the current is applied at a current density between about 0.1 A / cm 2 ~ about 0.2 A / cm 2 The desired allotrope is CNTs of a desired length, and the desired length is between about 10 μm and about 30 μm.

[0019]

[0019] Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01 wt% and about l5 wt% based on the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome C, and the current is applied at a current density between about 0.1 A / cm 2 ~ about 0.75 A / cm 2 The desired allotrope is CNTs of a desired length, and the desired length is between about 100 μm and about 20 μm.

[0020]

[002] ]Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01 wt% and about 5 wt% based on the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome C, and the current is applied at a current density between about 0.05 A / cm 2 ~ about 0.2 A / cm 2 The desired allotrope is CNTs of a desired length, and the desired length is between about 30 μm and about 60 μm.

[0021]

[0021] Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01% by weight and about 1% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the anode is made of nichrome C, the desired allotrope is a mixture of CNTs and curled CNTs, the relative amount of curled CNTs is at least 25% by weight of the total weight of the CNM product.

[0022]

[0022] Some embodiments of the present disclosure relate to a first method, wherein an iron-containing salt is added in an amount of about 0.01% to about 5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the anode is a composite anode comprising a first layer of Inconel 625 and at least a second layer of Inconel 600, and the desired allotrope is a CNT of a desired length, the desired length being between about 10 μm and about 100 μm.

[0023]

[0023] Some embodiments of the present disclosure relate to a first method in which an iron-containing salt is added in an amount between about 0.01% by weight and about 5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the anode being a composite anode comprising a first layer of a first Inconel alloy and at least a second layer of a second Inconel alloy, the desired allotrope being a CNT of a desired length, the desired length being between about 100 μm and about 500 μm.

[0024]

[0024] Some embodiments of the present disclosure relate to a first method, which further comprises adding an iron-containing salt in an amount of about 0.01% to about 5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, and adding a nickel-containing additive in an amount between about 0.01% to about 5% by weight to the electrolyte medium, wherein the desired allotrope is curled carbon nanotubes.

[0025]

[0025] Some embodiments of the present disclosure relate to a first method in which the anode is an Inconel alloy.

[0026]

[0026] Some embodiments of the present disclosure relate to a first method in which the anode is a composite anode comprising a first layer of a first Inconel alloy and at least a second layer of a second Inconel alloy.

[0027]

[0027] Some embodiments of the present disclosure relate to a first method in which the anode and cathode are fabricated together from substantially pure nickel, and the desired allotrope is a mixture of nanobamboo and carbon nanotubes.

[0028]

[0028] Some embodiments of the present disclosure further include the step of adding a nickel-containing additive to an electrolyte medium or molten electrolyte medium in proportion to the amount of the electrolyte medium or molten electrolyte medium, wherein the anode is a composite anode comprising a first layer of Inconel 718 and at least a second layer of Inconel 600, and the desired allotrope is nanobamboo.

[0029]

[0029] Some embodiments of the present disclosure relate to a first method wherein the molten electrolyte is newly melted and the CNM product further comprises conical nanotube allotropes.

[0030]

[0030] Some embodiments of the present disclosure further include the step of adding a nickel-containing additive to an electrolyte medium or a molten electrolyte medium, wherein the anode is a composite anode comprising a first layer of Inconel 718 and at least a second layer of Inconel 600, and the desired allotrope is nanobamboo.

[0031]

[0031] Some embodiments of the present disclosure further include the step of introducing a lithium-containing additive into an electrolyte medium or a molten electrolyte medium, wherein the anode is a composite anode comprising a first layer of Inconel 718 and at least a second layer of Inconel 600, and the desired allotrope is a nanotree, relating to a first method.

[0032]

[0032] Some embodiments of the present disclosure relate to a first method in which the lithium-containing additive is lithium oxide, and is added in an amount between about 0.05% by weight and 0.5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0033]

[0033] Some embodiments of the present disclosure further include the step of adding a nickel-containing additive to an electrolyte medium or molten electrolyte medium, wherein the anode is made of nichrome C and the current is about 0.05 A / cm². 2 ~0.12A / cm 2 The present invention relates to a first method in which a current density between is applied and the desired allotrope is the CNR of a hollow nanoonion.

[0034]

[0034] Some embodiments of the present disclosure further include the step of introducing a magnetic additive component into an electrolytic cell, the magnetic additive component comprising a magnetic material additive component, a carbide growth component, or any combination thereof, wherein the desired allotrope is magnetic and moves when in a magnetic field, according to the first method.

[0035]

[0035] Some embodiments of the present disclosure further include the step of introducing a doping additive component into an electrolytic cell, thereby doping a desired allotrope, and the atoms of the doping additive component being directly incorporated throughout the doped desired allotrope to impart a desired physical and / or chemical property to the doped desired allotrope that is different from that of an undoped desired allotrope.

[0036]

[0036] Some embodiments of the present disclosure relate to a first CNM including nanobamboo, the nanobamboo including multiple graphene layers located between pairs of bamboo knobs.

[0037]

[0037] In these embodiments of the first CNM, the nanobamboo is measured by Raman spectroscopy and has at least 1 I D / I G It has a ratio.

[0038]

[0038] Some embodiments of the present disclosure relate to a second CNM including a nanotree, wherein the nanotree includes a trunk CNT having a plurality of branch CNTs extending away from the trunk CNT.

[0039]

[0039] In these embodiments of the second CNM, the nanotree is measured by Raman spectroscopy to be between approximately 0.7 and approximately 0.9. D / I G It has a ratio.

[0040]

[0040] In these embodiments of the second CNM, the second CNM further includes a curved graphene layer located proximal to each of the intersections of the multiple branch CNTs and trunk CNTs.

[0041]

[0041] Some embodiments of the present disclosure relate to a third CNM comprising one or more high aspect ratio carbon nanotubes (CNTs), nanobamboos; conical CNTs; curled CNTs, curled carbon nanofibers, or nanotrees having an aspect ratio greater than 1000.

[0042]

[0042] Some embodiments of the present disclosure relate to a fourth CNM including hollow nanoonions defining an internal core.

[0043]

[0043] In these embodiments of the fourth CNM, the internal core can be substantially empty.

[0044]

[0044] In these embodiments of the fourth CNM, the internal core may contain a metal, which is iron, nickel, or a combination thereof.

[0045]

[0045] In these embodiments of the fourth CNM, the hollow nanoonions are measured by Raman spectroscopy to be between about 0.2 and about 0.4 I D / I G It has a ratio.

[0046]

[0046] Some embodiments of the present disclosure relate to the use of a desired nanocarbon allotrope in medical devices, structural strengthening additives, strength strengthening additives, conductivity strengthening additives, thermal conductivity strengthening additives, or flexibility strengthening additives, hardness strengthening additives, durability strengthening additives, lubrication strengthening additives, or as catalysts, electric vehicles, cables or wires, sports equipment, pharmaceutical delivery systems, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage systems, light absorption strengthening agents for surfaces, electromagnetic shielding strengthening agents for surfaces, surface treatments, surface coatings, paints or water treatment systems, wherein the desired allotrope is selected from the group consisting of carbon nanotubes (CNTs), curled CNTs, conical carbon nanofibers, nanobamboo, hollow nanoonions, and nanotrees of a desired length.

[0047]

[0047] Some embodiments of the present disclosure relate to a second method for producing a macroassembly product. The second method includes: heating an electrolyte medium to obtain a molten electrolyte medium; positioning the molten electrolyte medium between the anode and cathode of an electrolytic cell; introducing a carbon source into the electrolytic cell; applying an electric current to the cathode and anode of the electrolytic cell; and collecting a CNM product from the cathode. In embodiments of the second method, the CNM product includes a macroassembly product comprising a minimum relative amount of nanosponge, densely packed substantially parallel carbon nanotubes (CNTs), or a nanoweb of CNTs.

[0048]

[0100] Some embodiments of this disclosure relate to a second method in which the anode and cathode are fabricated from high nickel-content materials, respectively, and the CNM product contains nanosponges, with a minimum relative amount being at least 70% of the total weight of the CNM product.

[0049]

[0101] Some embodiments of this disclosure relate to a second method wherein current is applied in a first stage of increasing current density and a second stage of a higher and substantially constant current density.

[0050]

[0102] In some embodiments of this disclosure, during the second stage, the current density is increased to approximately 0.005 A / cm² for approximately 20 minutes. 2 ~about 0.07A / cm 2 Regarding the second method of increasing between...

[0051]

[0103] Some embodiments of this disclosure have a higher and substantially constant current density of about 0.1 A / cm². 2 ~0.3A / cm 2 Regarding the second method, which is between these two.

[0052]

[0104] Some embodiments of this disclosure relate to a second method, further comprising the step of adding a nickel-containing additive to an electrolyte medium or a molten electrolyte medium.

[0053]

[0105] Some embodiments of this disclosure relate to a second method in which a nickel-containing additive is added in an amount between about 0.5% by weight and about 0.2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0054]

[0106] Some embodiments of this disclosure relate to a second method in which the high-nickel-content material is a nichrome alloy.

[0055]

[0107] Some embodiments of this disclosure relate to a second method in which the anode is fabricated from a high nickel content material and the CNM product comprises a nanoweb of carbon nanotubes (CNTs).

[0056]

[0108] Some embodiments of this disclosure relate to a second method in which the cathode comprises copper.

[0057]

[0109] Some embodiments of this disclosure relate to a second method, further comprising the step of adding a nickel-containing additive to an electrolyte medium or a molten electrolyte medium.

[0058]

[0110] Some embodiments of this disclosure relate to a second method in which a nickel-containing additive is added in an amount between about 0.5% by weight and about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0059]

[0111] Some embodiments of this disclosure involve a current of approximately 0.1 to 0.5 A / cm². 2 The second method involves applying a current density between .

[0060]

[0112] Some embodiments of this disclosure have a current density of 0.2 A / cm². 2 This concerns the second method.

[0061]

[0113] Some embodiments of the present disclosure relate to a second method further comprising the step of adding an iron-containing additive to a molten electrolyte, wherein the anode is a composite anode.

[0062]

[0114] Some embodiments of this disclosure relate to a second method in which an iron-containing additive is added in an amount of about 0.5% to about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0063]

[0115] Some embodiments of the present disclosure relate to a second method, wherein the composite anode comprises a first layer of a first Inconel alloy and at least a second layer of a second Inconel alloy, and the CNM product comprises densely packed substantially parallel CNTs.

[0064]

[0116] Some embodiments of the present disclosure relate to a second method wherein the composite anode comprises a first layer of nichrome alloy and at least a second layer of Inconel alloy, the desired allotrope is a CNT of a desired length, and the CNM product comprises densely packed substantially parallel CNTs.

[0065]

[0117] Some embodiments of the present disclosure further include the step of introducing a magnetic additive component into an electrolytic cell, wherein the magnetic additive component includes a magnetic material additive component, a carbide growth component, or any combination thereof, and the macro-assembly product is magnetic and moves when in a magnetic field, according to a second method.

[0066]

[0118] Some embodiments of the present disclosure further include the step of introducing a doping additive component into an electrolytic cell, thereby doping the macroassembly product, and the atoms of the doping additive component are directly incorporated throughout the doped macroassembly product to impart a desired physical and / or chemical property to the doped macroassembly product that is different from that of an undoped macroassembly product.

[0067]

[0119] Some embodiments of this disclosure relate to a first macroassembly comprising a nanosponge defining pores having a size between approximately 50 nm and approximately 300 nm.

[0068]

[0120] Some embodiments of this disclosure relate to a second macroassembly, which includes a macroassembly comprising nanosponges defining pores between approximately 100 nm and approximately 500 nm in size.

[0069]

[0121] Some embodiments of this disclosure are measured by Raman spectroscopy and the nanosponge is between approximately 0.6 and approximately 0.8 I D / I G This relates to a first (or second) macro-assembly having a ratio.

[0070]

[0122] Some embodiments of this disclosure relate to a third macroassembly including a nanoweb that defines pores having a size between approximately 200 nm and approximately 1 μm.

[0071]

[0123] Some embodiments of this disclosure describe a nanoweb that, when measured by Raman spectroscopy, has an I value between approximately 0.2 and approximately 0.4. D / I G This relates to a third macro-assembly having a ratio.

[0072]

[0124] Some embodiments of this disclosure relate to a fourth macroassembly comprising a number of densely packed, substantially parallel carbon nanotubes (CNTs) defining an inter-CNT spacing between approximately 50 nm and approximately 300 nm.

[0073]

[0125] Some embodiments of this disclosure describe a number of densely packed, substantially parallel carbon nanotubes, which, when measured by Raman spectroscopy, have an I of approximately 0.4 to approximately 0.6 D / I G This relates to a fourth macro-assembly having a ratio.

[0074]

[0126] Some embodiments of this disclosure relate to the use of a first, second, or third macro-assembly for nanofiltration.

[0075]

[0048] Some embodiments of the present disclosure relate to the use of a fourth macroassembly as conductive wire for nanofiltration or in artificial neural networks.

[0076]

[0049] Some embodiments of the present disclosure relate to a third method for producing a CNM product. The method includes: heating an electrolyte medium to obtain a molten electrolyte medium; positioning the molten electrolyte medium between a high nickel-content anode and a copper-containing cathode of an electrolytic cell; introducing a carbon source into the electrolytic cell; introducing an iron-containing salt into the electrolyte medium or molten electrolyte medium; applying a low current density current to the cathode and anode of the electrolytic cell; and collecting the CNM product from the cathode. In these embodiments of the third method, the CNM product comprises a minimum relative amount of a desired allotrope, which is a carbon nanodragon or a carbon nanobelt.

[0077]

[0100] Some embodiments of the present disclosure relate to a third method in which an iron-containing salt is added in an amount between about 0.05% by weight and about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0078]

[0101] Some embodiments of the present disclosure relate to a third method in which the iron-containing salt is iron oxide.

[0079]

[0102] Some embodiments of the present disclosure relate to a third method in which the anode is an Inconel alloy.

[0080]

[0103] Some embodiments of the present disclosure have a low current density, where the current is approximately 0.3 A / cm². 2 ~about 0.75A / cm 2 The third method has a current density between and the desired allotrope is nanodragon, and the minimum relative amount is at least 70% by weight of the total weight of the CNM product.

[0081]

[0104] Some embodiments of the present disclosure relate to a third method in which the copper-containing cathode is a Monel alloy.

[0082]

[0105] Some embodiments of the present disclosure relate to a third method, in which a current of low current density is applied for about 4 hours.

[0083]

[0106] Some embodiments of the present disclosure further include a step of aging a molten electrolyte medium for at least 24 hours, wherein iron oxide is added prior to the aging step, and a current with a low current density of about 0.05 A / cm² is applied. 2 ~0.15A / cm 2 The third method has a current density between and , the desired allotrope is a nanobelt, and the minimum relative amount is at least 90% by weight of the total weight of the CNM product.

[0084]

[0107] Some embodiments of the present disclosure relate to a third method in which the copper-containing cathode comprises Muntz brass.

[0085]

[0108] Some embodiments of the present disclosure relate to a third method wherein a current of low current density is applied over a period of about 15 to 20 hours.

[0086]

[0109] Some embodiments of the present disclosure further include the step of introducing a magnetic additive component into an electrolytic cell, wherein the magnetic additive component comprises a magnetic material additive component, a carbide growth component, or any combination thereof, and a desired allotrope moves when it is magnetic and in a magnetic field.

[0087]

[0110] Some embodiments of the present disclosure further include the step of introducing a doping additive component into an electrolytic cell, thereby doping a desired allotrope, and the atoms of the doping additive component being directly incorporated throughout the doped desired allotrope to impart a desired physical and / or chemical property to the doped desired allotrope that is different from that of an undoped desired allotrope.

[0088]

[0111] Some embodiments of the present disclosure relate to a fifth CNM including a nanodragon, the nanodragon having an elongated body CNT having at least one projection extending away from the elongated body CNT.

[0089]

[0112] Some embodiments of the present disclosure relate to a fifth CNM in which at least one projection is a plurality of projections.

[0090]

[0113] Some embodiments of the present disclosure relate to a fifth CNM in which each of at least one projection includes a branched CNT, a metal-grown nodule, or any combination thereof.

[0091]

[0114] In some embodiments of the present disclosure, the nanodragon is measured by Raman spectroscopy to have an I between approximately 0.6 and approximately 0.8 D / I G Regarding the fifth CNM, which has a ratio.

[0092]

[0115] Some embodiments of the present disclosure are measured by Raman spectroscopy and have an I of approximately 0.67D / I G Regarding the sixth CNM, including nanobelts with a ratio.

[0093]

[0116] Some embodiments of the present disclosure relate to the use of a desired nanocarbon allotrope in one or more medical devices, structural strengthening additives, strength strengthening additives, conductivity strengthening additives, thermal conductivity strengthening additives, flexibility strengthening additives, hardness strengthening additives, durability strengthening additives, lubrication strengthening additives, or as catalysts, electric vehicles, cables or wires, sports equipment, medical delivery systems, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage systems, surface light absorption strengthening, surface electromagnetic shielding strengthening, surface treatments, surface coatings, paints or water treatment systems, wherein the desired allotrope is carbon nanodragon or carbon nanobelt.

[0094]

[0117] Some embodiments of this disclosure relate to a fourth method for producing CNM products. The fourth method includes: heating an electrolyte medium to obtain a molten electrolyte medium; positioning the molten electrolyte medium between the anode and cathode of an electrolytic cell; introducing a carbon source into the electrolytic cell; introducing an iron-free additive into the electrolyte medium or molten electrolyte medium; applying an electric current to the cathode and anode of the electrolytic cell; and collecting the CNM product from the cathode. In these embodiments of the fourth method, the CNM product comprises a minimum relative amount of a desired allotrope selected from the group consisting of thin carbon nanotubes (CNTs), nanobamboo, nanorods, nanoonions, and nanoflowers.

[0095]

[0118] Some embodiments of this disclosure relate to a fourth method in which the anode is a corrosion-resistant anode.

[0096]

[0119] Some embodiments of the present disclosure relate to a fourth method in which the corrosion-resistant anode contains a precious metal.

[0097]

[0120] Some embodiments of the present disclosure have a current of approximately 0.05 A / cm².2 ~0.15A / cm 2 The present invention relates to a fourth method having a current density between .

[0098]

[0121] Some embodiments of the present disclosure relate to a fourth method, wherein the iron-free additive is a chromium-containing additive, added in an amount between about 0.05% by weight and about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the desired allotrope being a thin CNT having a length between about 25 μm and about 125 μm, the minimum relative amount being greater than 70% of the total weight of the CNM product.

[0099]

[0122] Some embodiments of the present disclosure relate to a fourth method in which the cathode comprises a Monel alloy.

[0100]

[0123] Some embodiments of the present disclosure relate to a fourth method, wherein the iron-free additive is a nickel-containing additive added in an amount between about 0.05% by weight and about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, and the desired allotrope is a nanorod, with a minimum relative amount greater than 70% of the total weight of the CNM product.

[0101]

[0124] Some embodiments of the present disclosure relate to a fourth method in which the cathode comprises a Monel alloy.

[0102]

[0125] Some embodiments of the present disclosure relate to a fourth method by which a molten electrolyte medium is newly melted.

[0103]

[0126] Some embodiments of the present disclosure relate to a fourth method, wherein the step of applying an electric current is carried out over a period of 15 to 25 hours.

[0104]

[0127] Some embodiments of the present disclosure relate to a fourth method, wherein the iron-free additive is a nickel-containing additive and a chromium-containing additive, each added in an amount between about 0.05% by weight and about 2% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the desired allotrope is nanobamboo, and the minimum relative amount is between about 50% by weight and about 80% by weight relative to the total weight of the CNM product.

[0105]

[0128] Some embodiments of this disclosure relate to a fourth method in which the cathode comprises Muntz brass.

[0106]

[0129] Some embodiments of the present disclosure relate to a fourth method, wherein the iron-free additive is a lithium-containing additive, added in an amount between about 1% by weight and about 10% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the desired allotrope is a nanoonion, and the minimum relative amount is between about 70% by weight and about 99% by weight relative to the total weight of the CNM product.

[0107]

[0130] Some embodiments of this disclosure relate to a fourth method in which the lithium-containing additive is lithium phosphate.

[0108]

[0131] Some embodiments of this disclosure relate to a fourth method in which the anode comprises a nichrome alloy.

[0109]

[0132] Some embodiments of this disclosure relate to a fourth method in which the cathode comprises copper.

[0110]

[0133] Some embodiments of the present disclosure relate to a fourth method, wherein the iron-free additive is a cobalt-containing additive added in an amount of about 0.01% to about 5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium, the desired allotrope is a nanoflower, and the minimum relative amount is between about 70% to about 99% by weight relative to the total weight of the CNM product.

[0111]

[0134] Some embodiments of this disclosure relate to a fourth method in which the cobalt-containing additive is cobalt powder and the molten electrolyte is aged.

[0112]

[0135] Some embodiments of this disclosure relate to a fourth method in which the anode comprises a nichrome alloy.

[0113]

[0136] Some embodiments of this disclosure relate to a fourth method in which the cathode comprises copper.

[0114]

[0137] Some embodiments of the present disclosure further include the step of introducing a magnetic additive component into an electrolytic cell, wherein the magnetic additive component includes a magnetic material additive component, a carbide growth component, or any combination thereof, and the desired allotrope is magnetic and moves when in a magnetic field, according to a fourth method.

[0115]

[0138] Some embodiments of the present disclosure further include the step of introducing a doping additive component into an electrolytic cell, thereby doping a desired allotrope, and the atoms of the doping additive component being directly incorporated throughout the doped desired allotrope to impart a desired physical and / or chemical property to the doped desired allotrope that is different from that of an undoped desired allotrope, in a fourth method.

[0116]

[0139] Some embodiments of this disclosure relate to a seventh CNM including nanorods, wherein the nanorods have a squat, ring-like shape.

[0117]

[0140] Some embodiments of this disclosure relate to a seventh CNM in which the nanorods contain both carbon and oxygen.

[0118]

[0141] Some embodiments of this disclosure relate to a seventh CNM in which the amount of oxygen in the nanorods is between approximately 5% by weight and 12% by weight.

[0119]

[0142] Some embodiments of this disclosure describe nanorods that, when measured by Raman spectroscopy, have an I value between approximately 0.6 and approximately 0.9. D / I G Regarding the seventh CNM, which has a ratio.

[0120]

[0143] Some embodiments of this disclosure relate to an eighth CNM including a nanoflower, wherein the nanoflower comprises a number of frustoconical carbon nanotubes (CNTs) originating from a single origin, each frustoconical CNT having a diameter that decreases as the CNT extends away from the origin, and the nanoflower, as measured by Raman spectroscopy, has a diameter between approximately 0.6 and approximately 0.9 D / I G It has a ratio.

[0121]

[0144] Some embodiments of this disclosure relate to the use of desired nanocarbon allotropes in medical devices, structural strengthening additives, strength strengthening additives, conductivity strengthening additives, thermal conductivity strengthening additives, or flexibility strengthening additives, hardness strengthening additives, durability strengthening additives, lubrication strengthening additives, or as catalysts, electric vehicles, cables or wires, sports equipment, medical delivery systems, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage systems, light absorption strengthening agents for surfaces, electromagnetic shielding strengthening agents for surfaces, surface treatments, surface coatings, paints or water treatment systems, wherein the desired allotrope is selected from the group consisting of thin carbon nanotubes (CNTs), nanobamboos, nanorods, nanoonions, and nanoflowers.

[0122]

[0145] Some embodiments of this disclosure relate to a fifth method for producing CNM products. The fifth method includes: heating an electrolyte medium to obtain a molten electrolyte medium; positioning the molten electrolyte medium between the anode and a steel cathode of an electrolytic cell; introducing a carbon source into the electrolytic cell; applying an electric current to the cathode and anode of the electrolytic cell; and collecting the CNM product from the cathode. In these embodiments of the fifth method, the CNM product includes a minimum relative amount of metal-coated CNM product.

[0123]

[0146] Some embodiments of this disclosure relate to a fifth method, further comprising the step of introducing an excess amount of metal into a molten electrolyte medium.

[0124]

[0147] Some embodiments of this disclosure relate to a fifth method by which an excess amount of metal is introduced by introducing a metal-containing additive, introducing an excess amount of metal by decomposing the inner wall of an electrolytic cell, introducing an excess amount of metal by decomposing the anode, or any combination thereof.

[0125]

[0148] Some embodiments of this disclosure relate to a fifth method in which the metal is nickel, iron, titanium, tin, copper, vanadium, cobalt, zinc, magnesium, aluminum, ruthenium, silver, iridium, palladium, rhodium, or platinum.

[0126]

[0149] Some embodiments of this disclosure relate to a fifth method, in which the metal is introduced as a metal mixture, a metal oxide, a metal salt, or any combination thereof.

[0127]

[0150] Some embodiments of this disclosure have a current of approximately 0.1 A / cm². 2 ~about 0.3A / cm 2 The fifth method has a current density between .

[0128]

[0151] Some embodiments of this disclosure relate to a fifth method in which the steel cathode includes galvanized steel, stainless steel, or any combination thereof.

[0129]

[0152] Some embodiments of this disclosure relate to a fifth method, further comprising the step of introducing a metal additive into an electrolyte medium or a molten electrolyte medium.

[0130]

[0153] Some embodiments of this disclosure relate to a fifth method, wherein the metal additive is added in an amount between about 0.25% and 1.5% by weight relative to the amount of the electrolyte medium or molten electrolyte medium.

[0131]

[0154] Some embodiments of this disclosure relate to a fifth method in which the metal additive is a nickel-containing additive.

[0132]

[0155] Some embodiments of this disclosure relate to a fifth method in which the anode includes nickel.

[0133]

[0156] Some embodiments of this disclosure relate to a fifth method in which the anode has a high nickel content.

[0134]

[0157] Some embodiments of the present disclosure further include a step of adding a nickel-containing additive, wherein the anode comprises a nichrome alloy, and the minimum relative amount of metal-coated CNTs is between about 5% by weight and 99.5% by weight of the total weight of the CNM product, relating to a fifth method.

[0135]

[0158] Some embodiments of this disclosure relate to a fifth method, in which the anode is made of substantially pure nickel.

[0136]

[0159] Some embodiments of this disclosure relate to a fifth method for moving a metal-coated CNM when it is magnetic and in a magnetic field.

[0137]

[0160] Some embodiments of the present disclosure further include the step of introducing a doping additive component into an electrolytic cell, thereby doping the metal-coated CNM, and the atoms of the doping additive component are directly incorporated throughout the doped and coated CNM to give the doped, metal-coated CNM a desired physical and / or chemical property different from that of an undoped, coated CNT.

[0138]

[0161] Some embodiments of this disclosure relate to a ninth CNM, including a metal-coated carbon nanotube (CNT).

[0139]

[0162] Some embodiments of this disclosure relate to a 10th CNM, including metal-coated graphite carbon, metal-coated nanobamboo, metal-coated conical carbon nanofibers, metal-coated nanopearls, metal-coated nanoonions, metal-coated hollow nanoonions, metal-coated nanoflowers, metal-coated nanodragons, metal-coated branches, and trunk CNTs (metal-coated nanotrees), metal-coated nanobelts, metal-coated nanorods, metal-coated long and / or linear CNTs, metal-coated high aspect ratio CNTs, metal-coated thin CNTs, and macroscopic assemblies of CNTs, including densely packed linear metal-coated CNTs, metal-coated nanosponges, metal-coated nanowebs, or any combination thereof.

[0140]

[0163] Some embodiments of this disclosure relate to ninth and tenth CNMs in which the metal-coated CNM includes an external coating of nickel.

[0141]

[0164] Some embodiments of this disclosure relate to the use of a desired metal-coated allotrope in medical devices, structural strengthening additives, strength strengthening additives, conductivity strengthening additives, thermal conductivity strengthening additives, or one or more flexibility strengthening additives, hardness strengthening additives, durability strengthening additives, lubrication strengthening additives, or as catalysts, electric vehicles, cables or wires, sports equipment, medical delivery systems, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage systems, light absorption strengthening agents for surfaces, electromagnetic shielding strengthening agents for surfaces, surface treatments, surface coatings, paints or water treatment systems, wherein the desired allotrope is Metal-coated CNTs, metal-coated graphite-like carbon, metal-coated nanobamboo, metal-coated conical carbon nanofibers, metal-coated nanopearls, metal-coated nanoonions, metal-coated hollow nanoonions, metal-coated nanoflowers, metal-coated nanodragons, metal-coated branch and trunk CNTs (metal-coated nanotrees), metal-coated nanobelts, metal-coated nanorods, metal-coated long and / or linear CNTs, metal-coated high aspect ratio CNTs, metal-coated thin CNTs, and macroscopic assemblies of CNTs including densely packed linear metal-coated CNTs, metal-coated nanosponges, metal-coated nanowebs, or any combination thereof.

[0142]

[0050] Without being bound by any particular theory, embodiments of the present disclosure provide methods for producing CNM products having a minimum relative amount, and in some cases high purity, of a desired nanocarbon allotrope in the CNM product. In some embodiments of the present disclosure, the methods can be scaled up to produce previously unseen amounts of CNM products having a minimum relative amount or high purity of the desired nanocarbon allotrope. According to such available methods, it is now possible to produce large quantities of the desired allotrope, and therefore it is now possible to consider a variety of practical uses and applications of such allotropes. In some embodiments of the present disclosure, the desired allotrope can be used in a variety of applications including, but not limited to, medical devices, structural strengthening additives, strength strengthening additives, conductivity strengthening additives, thermal conductivity strengthening additives, or flexibility strengthening additives, hardness strengthening additives, durability strengthening additives, lubrication strengthening additives, or as catalysts, electric vehicles, cables or wires, sports equipment, medical delivery systems, electronics, batteries, supercapacitors, sensors, plastics, polymers, textiles, hydrogen storage systems, or water treatment systems.

[0143]

[0051] Typically, those skilled in the art would not consider modifications of established processes, such as the applicant's known electrolytic processes for creating carbon nanomaterials using CO2, because the complexity of such processes can be extreme without any prospect of results. Surprisingly, embodiments of the present disclosure provide a wide range of controlled modifications of electrolytic operating parameters, including modifications of methods and apparatus, which successfully provide unexpectedly high purity of the constituent structures in the CNM products and unusual forms of the constituent structures. Such controlled modifications include, but are not limited to, various cathode components and compositions, composite anode components and compositions, numerous electrolyte additives, various electrolytic conditions, or combinations thereof.

[0144]

[0052] These and other features of the present disclosure will be made more apparent in the following detailed description with reference to the accompanying drawings. [Brief explanation of the drawing]

[0145] [Figure 1]

[0053] This is a schematic diagram showing various input and product output amounts for high-yield electrolytic synthesis of carbon nanomaterials from carbon dioxide. [Figure 2]

[0054] Scanning electron microscope (SEM) images of nanocarbon products of nanobamboo and nanopearl allotropes of carbon synthesized by electrolytic separation of CO2 in Li2CO3 at 770°C according to embodiments of the present disclosure are shown. [Figure 3]

[0055] Transmission electron microscope (TEM) images of novel nanobamboo, nanopearl, and conical CNF nanocarbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure are shown. [Figure 4]

[0056] Images of elemental composition analysis performed by HAADF (high-angle annular dark-field TEM) are shown, and the TEM of novel nanobamboo and nanopearl nanocarbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is compared. [Figure 5]

[0057] A schematic diagram summarizing the growth model of carbon nanomaterials fabricated according to the embodiments of this disclosure is shown. [Figure 6]

[0058] TEM and HAADF elemental analysis of hollow nanoonion carbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 7]

[0059] The SEM of the CNM products of carbon nanoflowers, nanoonions, and nickel-coated CNT allotropes prepared according to embodiments of the present disclosure is shown. [Figure 8]

[0060] The following are SEM images of the CNM products of carbon nanodragons, nanotrees, nanobelts, and nanorod allotropes prepared according to embodiments of the present disclosure. [Figure 9A]

[0061] TEM and HAADF elemental analysis of nanoflower carbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 9B]

[0062] TEM and HAADF elemental analysis of nanodragon carbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 10]

[0063] The HAADF elemental analysis of nanotree carbon allotropes synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure is shown. [Figure 11]

[0064] A schematic diagram illustrating the observed CVD-synthesized amorphous branched carbon nanotree growth catalyzed by nucleating a metal catalyst is shown. [Figure 12]

[0065] TEM and HAADF elemental analysis of nanobelt carbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 13]

[0066] TEM and HAADF elemental analysis of nanorod carbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 14]

[0067] SEM images of various allotropes of carbon synthesized by molten carbonate electrolysis according to embodiments of the present disclosure are shown. [Figure 15]

[0068] The Raman spectroscopic analysis of CNM products consisting of various nanocarbon allotropes and packed carbon nanotube assemblies synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 16A]

[0069] XRD analysis of CNM products consisting of various nanocarbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 16B]

[0070] The XRD analysis of CNM products consisting of various nanocarbon allotropes synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 17]

[0071] The image shows an SEM image of the CNM product of high-purity, high-yield carbon nanotubes synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. [Figure 18]

[0072] The TEM and HAADF of high-purity, high-yield CNTs synthesized by molten carbonate electrolysis according to embodiments of the present disclosure are shown. [Figure 19]

[0073] The image shows an SEM image of a CNM product of high aspect ratio (and high purity and yield) CNTs synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. [Figure 20]

[0074] TEM and HAADF analysis of the CNM product of high-purity, high-yield CNTs synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 21]

[0075] The image shows an SEM image of the CNM product of high-purity, high-yield CNTs synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. [Figure 22]

[0076] The TEM and HAADF of the CNM product of carbon nanotubes exhibiting nodules or buds, synthesized by molten carbonate electrolysis according to embodiments of the present disclosure. [Figure 23]

[0077] The image shows an SEM image of a CNM product consisting of carbon nanotubes arranged in a macroscopic assembly synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. [Figure 24]

[0078] Raman spectroscopic analysis of CNM products consisting of various macroscopic assemblies of CNTs synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 25]

[0079] XRD analysis of CNM products consisting of various CNT macroscopic assemblies synthesized by molten carbonate electrolysis according to embodiments of the present disclosure is shown. [Figure 26]

[0080] This is a line graph of mass (%) and temperature (°C) of high-purity carbon nanotube allotropes prepared according to embodiments of the present disclosure. [Figure 27]

[0081] A series of various magnified SEM images of high-purity carbon nanotube allotropes prepared according to embodiments of this disclosure are shown. [Figure 28]

[0082] This is a line graph of mass (%) and temperature (°C) of a high-purity carbon nanoonion allotrope prepared according to an embodiment of the present disclosure. [Figure 29]

[0083] A series of various magnified SEM images of high-purity carbon nanoonion allotropes prepared according to embodiments of this disclosure are shown. [Figure 30]

[0084] This is a line graph of mass (%) and temperature (°C) of high-purity carbon nanopearl allotropes prepared according to the embodiments of the present disclosure. [Figure 31]

[0085] A series of various magnified SEM images of high-purity carbon nanopearl allotropes prepared according to embodiments of this disclosure are shown. [Modes for carrying out the invention]

[0146]

[0086] Embodiments of the present disclosure relate to methods and apparatus for producing carbon nanomaterial (CNM) products containing various desired carbon allotropes, such as carbon nanotubes (CNTs), graphite carbon, nanobamboo, conical carbon nanofibers, nanopearl carbon, coated CNTs, nanoonions, hollow nanoonions, nanoflowers, nanodragons, branch and trunk CNTs (nanotrees), nanobelts, nanorods, long and / or linear CNTs, high aspect ratio CNTs, thin CNTs, and macroscopic assemblies of CNTs. The methods and apparatus utilize carbon dioxide (CO2) as a reactant in an electrolytic reaction to produce these various components of the CNM product. Embodiments of the present disclosure provide a range of controlled modifications of the electrolytic method and apparatus of the present disclosure to selectively provide CNM products having one or more of these allotropes in high purity. Figure 1 provides a chart showing various CNM products that can be produced by electrosynthesis using carbon dioxide. In summary, Figure 1 illustrates how CO2 can act as a source of captured carbon 102, where CO2 is captured from the atmosphere 108 or from a more concentrated source such as exhaust gas or other industrial waste streams 110, which are concentrated sources of CO2. As will be understood by those skilled in the art, any source of carbon contained in solid, gaseous, or liquid phases is contemplated herein. The carbon, such as CO2, is then introduced into an electrolytic cell, and an electrolytic reaction 104 occurs in a molten carbonate electrolyte medium. The products of the electrolytic reaction 104 may include oxygen and CNM products 106. Depending on the specific operating parameters of the electrolytic reaction 104, the CNM products 106 may include desired relative amounts of desired allotropes.

[0147]

[0087] Some embodiments of the present disclosure relate to methods and apparatus for producing a CNM product containing a desired carbon allotrope in a higher relative amount of a particular desired carbon allotrope. For example, the higher relative amount of the first desired carbon allotrope may be at least 20% by weight (relative to the weight of the first desired carbon allotrope compared to the total weight of the CNM product). In some embodiments of the present disclosure, the higher relative amount of the first desired carbon allotrope may be at least 25% by weight, at least 30% by weight, at least 35% by weight, at least 40% by weight, at least 50% by weight, at least 60% by weight, at least 70% by weight, at least 80% by weight, at least 90% by weight, at least 91% by weight, at least 92% by weight, at least 93% by weight, at least 94% by weight, at least 95% by weight, at least 96% by weight, at least 97% by weight, at least 98% by weight, at least 99% by weight, or at least 99.5% by weight of the total weight of the CNM product produced by the embodiments described herein. Some embodiments of this disclosure produce a CNM product in which the desired allotrope is of high purity.

[0148]

[0088] Definition

[0149]

[0089] Unless otherwise defined, all technical and scientific terms used herein have the same meanings as those commonly understood by those skilled in the art to which this disclosure belongs.

[0150]

[0090] The term “approximately” as used herein refers to a variation of approximately ±10% from a given value. It should be understood that such variation is always present in any given value provided herein, whether specifically mentioned or not.

[0151]

[0091] As used herein, the term “allotrope” may be used synonymously with “physical form,” “structure,” “morphology,” “nanocarbon allotrope,” “nanocarbon physical form,” “nanocarbon structure,” or “nanocarbon form,” and all of these terms—and similar terms—refer to the three-dimensional shape—and associated physicochemical properties—of nanoscale structures found as components in CNM products, prepared by embodiments described herein.

[0152]

[0092] As used herein, the terms “desired relative amount,” “relative amount,” or “minimum relative amount” all refer to the relative amount of the desired allotrope that contributes to the total amount of the CNM product, and this relative amount is greater than at least 70% by weight of the total amount of the CNM product produced in some embodiments, and the term “high purity” may be used herein. In some embodiments of the present disclosure, the relative amount of the desired allotrope is greater than 75% by weight of the total amount of the CNM product produced, greater than 80% by weight of the total amount of the CNM product produced, greater than 85% by weight of the total amount of the CNM product produced, greater than 90% by weight of the CNM product produced, greater than 95% by weight of the total amount of the CNM product produced, greater than 97.5% by weight of the total amount of the CNM product produced, or greater than 99% by weight of the total amount of the CNM product produced.

[0153]

[0093] Embodiments of the present disclosure will now be described, which will include references to examples and figures.

[0154]

[0094] Some embodiments of the present disclosure relate to a method for producing a CNM product containing a larger amount of a desired allotrope than other allotropes present in the CNM product. The method includes heating a carbonate electrolyte to obtain a molten carbonate electrolyte; positioning the molten carbonate electrolyte between the anode and cathode in an electrolytic cell; applying an electric current to the cathode and anode in the electrolytic cell; and collecting the CNM product from the cathode.

[0155]

[0095] In some embodiments of the present disclosure, the method further includes the step of selecting an anode or cathode material to synthesize a larger amount of a desired allotrope than other allotropes present in the CNM product. In some embodiments of the present disclosure, the method further includes the step of selecting an additive and adding a selected amount of the selected additive to the electrolyte to synthesize a desired nanocarbon allotrope. In some embodiments of the present disclosure, the method further includes the step of applying a current of a selected current density to synthesize a desired nanocarbon allotrope. In some embodiments of the present disclosure, the method further includes the step of applying a current for a selected period of time to synthesize a desired nanocarbon allotrope.

[0156]

[0096] The step of heating the carbonate electrolyte can be carried out by a variety of means, as will be understandable to readers skilled in the art. For example, heating devices such as ovens or furnaces can be used to heat the electrolyte to a sufficient temperature so that it transitions to a molten liquid state. Thus, any heating device capable of achieving the temperature required to heat the electrolyte to its melting point is intended herein. In some embodiments of the present disclosure, the method further includes a step of aging the molten electrolyte so that the molten electrolyte is held in a molten state at a substantially constant temperature so that a steady state can be achieved. For example, the molten electrolyte may be aged for a period of 1 to 48 hours.

[0157]

[0097] The molten electrolyte is then positioned between the anode and cathode of the electrolytic cell, which may also be called the case. The electrolytic cell may be any type of vessel that can maintain its structural integrity in the face of the electrochemical environment that arises during the electrolytic reaction of the present disclosure. The electrolytic cell may have one or more walls which may be made of a material of choice or which are covered with a material of choice that will not decompose in the environment of the electrolytic reaction. Table 1 below provides a detailed list of various electrode materials suitable for use in embodiments of the present disclosure. In some embodiments of the present disclosure, the electrolytic cell is made of substantially pure alumina. In other embodiments of the present disclosure, the electrolytic cell is made of stainless steel with or without such lining which is made of another metal which is made of Inconel, nichrome, or Monel, or a combination thereof. In some embodiments of the present disclosure, the electrolytic cell is a tubular vessel with closed ends. In other embodiments of the present disclosure, the electrolytic cell is a rectangular vessel with one or more compartments.

[0158]

[0098] In some embodiments of the present disclosure, the electrolyte may be melted within the electrolytic cell or melted outside the cell and transferred thereto. Since the electrolytic reaction typically occurs over a period of time, thereby potentially cooling the molten electrolyte, the electrolytic cell may be configured with an integrated heating device of its own, or may be self-heated by the CO2 dissolution reaction and the electrolytic reaction, or may be configured to be heated by an external heating device located outside the electrolytic cell, so that the electrolyte remains in a molten state for a desired period of time.

[0159]

[0099] In some embodiments of the present disclosure, the electrolytic cell may be configured to maintain an electrolytic temperature at least about 400°C, at least about 500°C, at least about 550°C, at least about 600°C, at least about 650°C, at least about 675°C, at least about 700°C, at least about 725°C, at least about 750°C, at least about 775°C, at least about 800°C, at least about 825°C, at least about 850°C, at least about 875°C, at least about 900°C, at least about 1000°C, or higher than 1000°C.

[0160]

[0100] Anodes can be made from a variety of metals or alloys. Some anodes can be made from materials containing metals that are resistant to corrosion by oxidation (or, if not, noble metals such as iridium, platinum, gold, ruthenium, rhodium, osmium, palladium, or any combination thereof). Anodes may also be made from non-noble metals or mixtures of metals that are substantially pure metals such as nickel. Some non-limiting examples of metals suitable for anodes in this disclosure include: substantially pure nickel, alloys composed substantially mostly of nickel, alloys with a high nickel content, or alloys composed of some nickel. As used herein, alloys with more than 50% by weight of nickel are referred to as high nickel content alloys. Suitable examples of alloys used as anodes include, but are not limited to, Inconel 718 (with at least about 72 wt% nickel content), Inconel 600 (with about 52.5 wt% nickel content), or other Inconel alloys, such as, but are not limited to, Inconel 625 (with about 58 wt% nickel content), Nichrome A (composed of about 80 wt% nickel and about 20 wt% chromium), and Nichrome C (composed of about 60 wt% nickel, about 24 wt% iron, and about 16 wt% chromium). Anodes made from alloys with lower nickel content may be suitable for use in some embodiments of this disclosure, including Incoloy alloys such as Incoloy 800 (composed of about 40 wt% iron, about 30-35 wt% nickel, and about 19-23 wt% chromium). In some embodiments of this disclosure, the anode may be monolithic or a composite composed of various materials.

[0161]

[0101] In some embodiments, the anode may be planar in shape and can be manufactured in various dimensions. In some embodiments of the present disclosure, the anode may be made of wire wound on a substantially flat coil having an upper and lower surface. In some embodiments of the present disclosure, the anode may be perforated. In other embodiments, the anode may be made of various shapes and surface modifications to maximize the active area of ​​the electrolysis. The upper and lower surfaces of the anode may have substantially equal areas suitable for fitting into an electrolytic cell. In some embodiments, the anode surface is about 1 cm 2 ~Approx. 100,000cm 2 Between; approximately 10cm 2 ~50,000cm 2 Between; or approximately 100 cm 2 ~Approx. 10,000cm 2 It has a surface area between these two ranges. In some embodiments of the present disclosure, the anode may have two or more anode faces, each of which is within these ranges. In some embodiments, the anode may be even larger with a wider surface area. Those skilled in the art will understand that the size of the electrolytic cell may determine the size of the anode, and vice versa. The anode may be configured to be substantially aligned to a horizontal or vertical plane, or to a plane that is not parallel to either the horizontal or vertical plane.

[0162]

[0102] The cathode can be made of a variety of metals or alloys. Some cathodes can be made of materials including steel, galvanized steel, stainless steel, copper, or any combination thereof. Some further non-limiting examples of materials suitable for the anode of this disclosure include: nickel, nichrome C, Monel (about 67 wt% nickel and about 31-33 wt% copper), and Muntz brass (about 60 wt% copper and about 40 wt% zinc).

[0163]

[0103] In one embodiment, the cathode may be planar in shape and can be manufactured in various dimensions. In some embodiments of the present disclosure, the cathode may be made of wire wound on a flat coil having an upper and lower surface. In other embodiments, the cathode may be made of various shapes and surface modifications to maximize the active area of ​​the electrolysis. The upper and lower surfaces of the coiled cathode may have substantially equal areas suitable for fitting into an electrolytic cell. In some embodiments, the coiled cathode surface is about 1 cm 2 ~about 5000cm 2 Between; approximately 2cm 2 ~3000cm 2 Between; or about 3cm 2 ~About 1000cm 2 It has a surface area between the two. In some embodiments, the cathode may be even larger with a larger surface area. Those skilled in the art will understand that the size of the electrolytic cell and / or the size of the anode may determine, for example, the size of the cathode, and the electrodes may be substantially similar in size. The cathode may be configured to be substantially aligned with a horizontal or vertical plane, or with a plane that is not parallel to either the horizontal or vertical plane.

[0164]

[0104] In some embodiments of the present disclosure, the size and orientation of the cathode can be selected to substantially reflect the size and orientation of the anode. In some embodiments of the present disclosure, the anode and cathode may be arranged substantially in a horizontal plane and spaced perpendicular to each other. In other embodiments of the present disclosure, the anode and cathode may be arranged substantially in a vertical plane and spaced horizontally to each other. As will be understood by those skilled in the art, the distance between electrodes must allow sufficient current to pass between them, but the amperage of the current and the size of the electrolytic cell may affect how far apart the electrodes are. In some embodiments of this disclosure, the electrodes may be spaced apart from each other at intervals of approximately 0.25 cm, 0.5 cm, 0.75 cm, 1 cm, 1.25 cm, 1.5 cm, 1.75 cm, 2 cm, 3 cm, 4 cm, 5 cm, 7.5 cm, 10 cm, 15 cm, 20 cm, 30 cm, or greater.

[0165]

[0105] Some embodiments of the present disclosure relate to larger, scaled-up electrolytic cell and electrode sets. For example, in some embodiments of the present disclosure, each electrode is approximately 1 m 2 ~about 10m 2 Between, approximately 2m 2 ~approximately 9m 2 Between approximately 3 meters 2 ~approximately 8m 2 Between them, approximately 4m 2 ~about 7m 2 Between them, approximately 5m 2 ~about 6m 2 They may have surfaces having a surface area between them. As will be understood by those skilled in the art, the dimensions of the electrodes may or may not coincide with each other, or they may be configured in a sandwich configuration, with one electrode positioned between two of the other electrodes or in other configurations, and the dimensions of the electrodes may determine the dimensions of the electrolytic cell in which the electrodes are used internally.

[0166]

[0106] To initiate and maintain the electrolytic reaction in the electrolytic cell, an electric current is applied and flows between the anode and the cathode, through the molten electrolyte between them. In some embodiments of the present disclosure, the current may be alternating current or direct current. In some embodiments of the present disclosure, the current may be between about 0.01 amperes (A) and about 5 A. In some embodiments of the present disclosure, the current may be between about 0.025 A and about 4 A; between about 0.05 A and about 3 A; between about 0.075 A and about 2 A; and between about 0.1 A and about 1 A. In some embodiments of the present disclosure, the current is about 0.5 A. In some embodiments of the present disclosure, the current may be between about 5 A and about 500,000 A; or between about 500 A and about 50,000 A. In other embodiments of the present disclosure, the current may be between about 5,000 A and about 50,000 A.

[0167]

[0107] In some embodiments of the present disclosure, the current is applied at a substantially constant current density. For example, the current density of the applied current is about 0.001 A / cm². 2 ~About 1A / cm 2 It may be between these values. In some embodiments, the current density of the applied current is about 0.0025 A / cm². 2 ~about 0.75A / cm 2 Between approximately 0.005 A / cm² 2 ~about 0.5A / cm 2 Between approximately 0.0075 A / cm² 2 ~about 0.25A / cm 2 Between; or approximately 0.01 A / cm² 2 ~about 0.1A / cm 2 It may be between. In other embodiments of this disclosure, the current density of the applied current is about 1 A / cm². 2 ~about 10A / cm 2 It may be between these ranges. In some embodiments, a low current density is used to control conductivity during the formation of the CNM product.

[0168]

[0108] In some embodiments of the present disclosure, the method further includes the step of increasing the current in a stepwise manner over a predetermined elapsed time. For example, after a first period of a first constant current density, there is a second period of a second constant current density, then a third period of a third constant current density, then a fourth period of a fourth constant current density, and so on until a final current density is applied for the duration of the electrolysis process. In these examples, the periods may be the same or different, and may range from one minute to one hour, or any time in between. In these examples, the constant current density may be the same or different, and may be 0.005 A / cm². 2 ~0.75A / cm 2 The range may be limited to a certain extent. In other embodiments, the rising current may be increased and / or decreased in a stepwise manner, such as by oscillation, linear rising change, or other fluctuations.

[0169]

[0109] In some embodiments of the present disclosure, the method further includes the step of introducing one or more additives, which may also be referred to herein as additives, into a carbonate electrolyte medium. This introduction step can be carried out by a variety of methods, depending on the properties of the additives. The introduction of the additives into the carbonate electrolyte can be carried out before, during, or after the carbonate electrolyte is heated to a molten state. Non-limiting examples of such additives include: lithium-containing additives (lithium phosphate; lithium oxide, and other lithium-containing salts, etc.); iron-containing additives (iron-containing salts including iron oxide, etc.); magnesium-containing additives (magnesium salts including magnesium oxide, etc.); transition metal nucleating agents (Fe2O3, nickel powder, chromium powder, etc.); and one or more transition metal salts of iron, nickel, chromium, nickel, copper, manganese, titanium, zirconium, molybdenum, tantalum, or cobalt. For clarity, additives that do not contain any iron (including iron-containing salts) are collectively referred to herein as “iron-free” additives. In non-limiting embodiments of this disclosure, iron-free additives include: additives that are substantially free of any iron, additives that contain trace amounts of iron, and / or additives that contain amounts of iron that do not participate in the electrolytic reaction in any substantial or meaningful way. Examples of iron-free additives include, but are not limited to, lithium-containing additives, cobalt-containing additives, nickel-containing additives, and chromium-containing additives. According to embodiments of this disclosure, additives may be introduced in amounts between about 0.01% by weight and 10% by weight relative to the amount of electrolyte medium or molten electrolyte medium. In some embodiments of this disclosure, additives may be introduced in amounts between about 0.05% by weight and 7.5% by weight relative to the amount of electrolyte medium or molten electrolyte medium. In some embodiments of this disclosure, additives may be introduced in amounts between about 0.075% by weight and 5% by weight relative to the amount of electrolyte medium or molten electrolyte medium.

[0170]

[0110] As further examples, in some embodiments of the present disclosure, the lithium-containing additive may be added in an amount between 0.01% by weight and about 10% by weight, or between about 0.05% by weight and about 9% by weight, or between about 0.075% by weight and about 8% by weight.

[0171]

[0111] As further examples, in some embodiments of the present disclosure, the iron-containing additive may be added in an amount between 0.01% by weight and about 5% by weight, or between about 0.05% by weight and about 2.5% by weight, or between about 0.075% by weight and about 1.25% by weight, and in further embodiments, the iron-containing additive is added in an amount between about 0.05% by weight and 0.15% by weight.

[0172]

[0112] As further examples, in some embodiments of the present disclosure, the nickel-containing additive (as either nickel powder or nickel salt) may be added in an amount between 0.01% by weight and about 5% by weight, or between about 0.05% by weight and about 2.5% by weight, or between about 0.075% by weight and about 1.25% by weight, and in further embodiments, the nickel-containing additive is added in an amount between about 0.05% by weight and 0.15% by weight.

[0173]

[0113] As further examples, in some embodiments of the present disclosure, the cobalt-containing additive (as either cobalt powder or cobalt salt) may be added in an amount between 0.01% by weight and about 5% by weight, or between about 0.05% by weight and about 2.5% by weight, or between about 0.075% by weight and about 1.25% by weight, and in further embodiments, the cobalt-containing additive may be added in an amount between about 0.05% by weight and about 0.15% by weight.

[0174]

[0114] As further examples, in some embodiments of the present disclosure, the chromium-containing additive (as either chromium powder or chromium salt) may be added in an amount between 0.01% by weight and about 5% by weight, or between about 0.05% by weight and about 2.5% by weight, or between about 0.075% by weight and about 1.25% by weight, and in further embodiments, the chromium-containing additive is added in an amount between about 0.05% by weight and about 0.15% by weight.

[0175]

[0115] In some embodiments, the transition metal nucleating agent may be a transition metal oxide. In some embodiments of the present disclosure, the nucleating agent may be incorporated into the CNM product so that atoms of the nucleating agent form a portion of one or more allotropes of the CNM product. In some embodiments of the present disclosure, the incorporated nucleating agent may be magnetic. In some embodiments of the present disclosure, a portion of the nanomaterial product may be responsive to a magnetic field (by moving when near or inside a magnetic field), and a portion may be non-responsive to a magnetic field (by not moving), and these two types of nanomaterial products may be separated by applying an external magnetic field.

[0176]

[0116] The total duration of the electrolytic synthesis process may be between approximately 10 minutes and approximately 156 hours.

[0177]

[0117] In some embodiments of the present disclosure, the selection step may be configured such that the CNM product contains a desired combination of two or more desired allotropes. For example, the selection step can be varied in a controlled manner so that the CNM product contains a first allotrope and a second allotrope or further allotropes. Furthermore, the selection step can be configured so that a desired relative amounts of the first allotrope and the second allotrope with respect to each other can be achieved in the CNM product. For example, it is considered desirable that the amount of the first allotrope be greater than, less than, or substantially equal to the amount of the second allotrope present in the CNM product.

[0178]

[0118] As will be understood by those skilled in the art, the specific variability of the electrolytic process conditions, also referred herein as operating parameters, described herein may vary further as the physical scale of the electrolytic process increases. [Examples]

[0179]

[0119] Example

[0180]

[0120] The components of the molten electrolyte mixture described herein are commercially available: lithium carbonate (Li2CO3; Alfa Aesar, about 99% pure), lithium oxide (Li2O, 99.5%, Alfa Aesar), lithium phosphate (Li3PO4, 99.5%), iron oxide (Fe2O3, 99.9%, Alfa Aesar), and boric acid (H3BO3, Alfa Aesar 99+%).

[0181]

[0121] The electrodes described herein, including nichrome A (0.04 inch thick), nichrome C (0.04 inch thick), Inconel 718, Inconel 600 (0.25 inch thick), Inconel 625 (0.25 inch thick), Monel 400, stainless steel 304 (0.25 inch thick), Muntz brass (0.25 inch thick), nickel, and iridium, were all purchased from common commercial metal suppliers. Composite electrodes were fabricated from these purchased materials or purchased as-is.

[0182]

[0122] In the additives described herein: Ni powder is 3-7 μm (99.9%, Alfa Aesar), Cr powder is <10 μm (99.2%, Alfa Aesar), Co powder is 1.6 μm (99.8%, Alfa Aesar), and iron oxide is 99.9% Fe2O3 (Alfa Aesar). Inconel 600 (100 mesh) was purchased from Cleveland Cloth. Electrolysis was performed in a high-foam crucible >99.6% alumina (Advalue).

[0183]

[0123] The specific electrolyte composition of each electrolyte is described herein. The electrolytes were premixed by weight in the proportions described, and then metal or metal oxide additives, if used, were added. The cathode was mounted perpendicularly opposite the anode and immersed in the electrolyte. Generally, the electrode was immersed immediately after the dissolution of the electrolyte. For example, with some electrolytes, after dissolution, the electrolyte was maintained at 770°C (to "age" the electrolyte), then the electrolyte was immersed, and then electrolysis was started immediately. Generally, electrolysis was driven at a constant current density as described. With some electrolytes, as described, the current density was increased in several steps to reach the applied electrolytic current and then maintained at a constant current density. Otherwise, electrolysis was started and held at a single constant current. The electrolysis temperature was about 770°C unless otherwise specified herein.

[0184]

[0124] The sources of carbon included CO2 directly captured from the air and CO2 from the exhaust gas of a natural gas power plant. In embodiments of the present disclosure, electrolytic separation can be brought about as direct air carbon capture with or without CO2 pre-concentration, with concentrated CO2, or with a CO2-containing gas, for example, exhaust gas.

[0185]

[0125] The CNM products prepared according to the following examples were washed (with deionized water, 6M HCl, and concentrated HCl) to remove excess electrolytes, separated from the washing solution, and analyzed by PHENOM Pro Pro-X scanning electron microscopy (SEM, EDX), FEI Teneo LV SEM, and FEI Teneo Talos F200X TEM (EDX). XRD powder diffraction analysis was performed using a Rigaku D=Max 2200 XRD diffractometer and analyzed with the Jade software package. Raman spectroscopy was performed with a 532.14 wavelength incident laser light and a high resolution of 0.6 cm. -1 Then, measurements were taken using a LabRAM HR800 Raman microscope (HORIBA).

[0186]

[0126] In some embodiments of the present disclosure, CNM products prepared by the methods, apparatus, and systems described herein may yield a high-purity desired allotrope that is doped with such desired allotrope. Without being bound by any particular theory, when a doping component, also called a dopant, is introduced into the method, apparatus, or system, the atoms of the dopant may be directly incorporated into the various graphite structures of the CNM product and into the desired allotrope therein. When the atoms of the doping component are directly incorporated into the CNM product so as to be built on the cathode in situ, the resulting doped CNM product has different desired chemophysical properties than a CNM product that does not contain atoms of the doping component (undoped CNM product). Without being bound by any particular theory, the doping component may include at least one material comprising Group IIIA elements, non-carbon Group IVA elements, Group VA elements, Group VIA chalcogenide elements, or at least one material comprising gold, platinum, iridium, iron, or other Period 4, 5, or 6 metals. In some embodiments of this disclosure, the doping components include one or more of the following: oxygen atoms, halide atoms, nitrates, phosphates, thiophosphates, silicates, thionyl chloride, sulfur chloride, silicon chloride, thiophosphates, thionyl nitrate, silicon nitrate, silicon nitrite, sulfur oxide, and nitrous oxide gas. Without being bound by any particular theory, desired chemical properties of doped CNM products may include: greater conductivity (compared to undoped CNM products), enhanced charge storage (compared to undoped CNM products), heterogeneous catalytic properties, homogeneous catalytic properties, fuel cell catalytic properties, aerobic oxidation catalytic properties, enhanced reaction activity properties, and any combination thereof. Desired physicochemical properties of doped CNM products prepared according to embodiments of this disclosure may have a wide variety of applications, including catalysts, heavy metal removal, energy storage, sorption applications, batteries, supersensitive sensors, and combinations thereof.

[0187]

[0127] In some embodiments of the present disclosure, CNM products prepared by the methods, apparatus, and systems described herein may yield a desired allotrope that is magnetic. For clarity, the magnetic CNM product and the magnetic allotrope within it are physically movable by a magnetic field. Without adhering to any particular theory, when a magnetic additive component is introduced into a method, apparatus, or system, carbide-driven growth of various graphite structures in the magnetic CNM product may occur. In some embodiments of the present disclosure, the magnetic additive component includes at least one of a magnetic material additive component, a carbide growth component, and any combination thereof. In some embodiments of the present disclosure, the magnetic material additive component includes one or more magnetic materials, such as iron, nickel, cobalt, gadolinium, samarium, neodymium, steel, and alloys, which are ferromagnetic, paramagnetic, diamagnetic, and any combination thereof. In some embodiments of this disclosure, the iron-based additive is one or more of cast iron powder, ferrous metal, steel, stainless steel, iron-containing metal alloy, iron oxide, FeO, Fe2O3, Fe3O4, or iron-containing salts. In the magnetic CNM product, the magnetic additive components are incorporated or formed as one or more nodules, which may be covered with one or more layers of graphite-like carbon on the magnetic CNM product. In some embodiments of this disclosure, the carbide growth component may be a metallic carbide: e.g., iron carbide, nickel carbide, cobalt carbide; zirconium carbide, chromium carbide, tantalum carbide, hafnium carbide, and any combination thereof. In some embodiments of this disclosure, the carbide growth component may be a non-metallic carbide, e.g., silicon carbide, germanium carbide, and any combination thereof. The magnetic additive components may be added as chemical additives to the methods, apparatus, and systems of this disclosure, or originate from one or more walls, anodes, cathodes, electrolyte media, and any combination thereof of an electrolytic cell.

[0188]

[0128] Example 1 Electrolytic process conditions for producing nanocarbon products with high-purity desired allotropes

[0189]

[0129] To produce the CNM product, the electrolytic reaction was carried out in an electrolyte cell comprising a vessel, anode, and cathode. The vessel was made of pure alumina (99.6% purity alumina, commercially available from AdValue) and had closed ends. The vessel contained molten Li2CO3 electrolyte at 770°C.

[0190]

[0130] The anode was made from various materials and configured to generate oxygen during the electrolytic reaction.

[0191]

[0131] The cathode was made of brass and also consisted of a substantially flat coil.

[0192]

[0132] Carbon dioxide from the air was directly captured by the molten electrolyte during the electrolytic reaction.

[0193]

[0133] Various electrochemical operating parameters included the composition and / or composition of the cathode and anode, the additives used in the Li2CO3 electrolyte and their concentrations, the current density, and the electrolysis time. Various electrolyte additives included Fe2O3, nickel, chromium powder, or combinations thereof. The electrolytic reaction varied over a range of electrolytic current densities. Electrode variations included the use of cathode metal electrodes such as Muntz brass Monel or nichrome alloy. Anode types included noble metal anodes, e.g., iridium, various nickel-containing anodes containing nickel, nichrome A or C, Inconel 600, 625, or 718, or specific layered combinations of these metals. The alloy compositions of metals used as electrodes are shown in Table 1. The metal variability was further refined by combining the metals in Table 1 as anodes, using solid sheets of one type of Inconel alloy layered with one or more screens of another Inconel alloy, such as an anode of Inconel 625 with three layers of (spot-welded) 100-mesh Inconel 600 screens.

[0194]

[0134] [Table 1]

[0195]

[0135] Thousands of runs of various combinations of electrolytic operating conditions were performed to realize embodiments of the present disclosure. In fewer than 30 of these electrolysis, attractive but rarely observed products were produced, which had nanomorphological analogues to the macrostructure of bamboo, but were observed in only a small proportion of the total products. Table 2 summarizes the systematic optimization of electrolytic conditions in Li2CO3 at 770°C to optimize and maximize the formation of nanobamboo electrolytes. Several conventional electrolysis processes for generating nanobamboo were associated with nickel electrodes or initiated by increasing the current to stimulate nucleation. Experimental electrolysis #I in the top row of Table 2 includes both of these features, with nickel as both the cathode and anode. Increasing the electrolytic current was also applied as follows: constant 0.01, then 0.02 A / cm 2 Then, electrolysis for another 10 minutes, followed by 0.04 A / cm², and then 0.08 A / cm². 2 Then, electrolysis for another 5 minutes, followed by electrolysis with a constant current of 0.2 A / cm². 2 The process was carried out as shown in Table 2. Nanobamboo was evident in the product SEM, but constituted only a small amount (30 wt%) of the total product. As seen in electrolysis #II in Table 2, the increase in nanobamboo product was achieved by the direct addition of Ni and Cr additive powders to the electrolyte, and the anode was replaced with a noble metal (iridium), accompanied by a 1 / 5 decrease in current density. As shown in Table 2, this electrolysis #II has the first majority of nanobamboo product, 60 wt%. Coulomb efficiency quantifies the available charge measured for the number of electrons measured per equivalent of C in the product (current multiplied by electrolysis time). Coulomb efficiency tends to decrease with lower current densities, and in this case, the Coulomb efficiency of the synthesis was 79%. Coulomb efficiency can approach higher values ​​at lower current densities by reducing impurities in the system.

[0196]

[0136] [Table 2]

[0197]

[0137] While not adhering to any particular theory, low current rise and pre-electrolysis conditions may have advantages and disadvantages. For example, as an advantage, current rise conditions may support the reduction and deposition of the initial graphene layer to facilitate ongoing reduction and growth. Furthermore, lower currents may favor transition metal deposition at the cathode and formation at nucleation sites. Analysis of bound pair-free metal cations in the molten electrolyte for reduction potential calculations has been extremely challenging, while the concentration is low compared to carbonates (from CO2) in the electrolyte. However, without Nernst activity and temperature correction, the reduction residual potentials of Ni, Fe, Cr, Cu, and CO2 at room temperature are CO2(IV / 0)=-1.02, Cr(III / 0)=-0.74, Fe(II / 0)=-0.44, Co(II / 0)=-0.28, Ni(II / 0)=-0.25, Fe(III / 0)=-0.04, Cu(II / 0)=0.34, and Co(III / 0)=1.82. However, the carbonate C(IV)O3 formed by the reaction of C(IV)O2 with electrolyte oxides in a pure molten carbonate solution... 2- It should be noted that the free activity of tetravalent carbon was orders of magnitude greater than the activity of transition metal ions dissolved in the electrolytic electrolyte. This helps to promote the thermodynamic and kinetic reduction of tetravalent carbon on the metal deposition at the cathode. However, actual observations have shown that, for most of the molten carbonate CO2 electrolysis studied, the initial low current rise does not appear to promote the deposition of carbon of the highest purity.

[0198]

[0138] Figure 2 shows SEM analysis images of nanocarbon products of carbon nanofibers and nanopearl allotropes synthesized by electrolytic separation of CO2 in Li2CO3 at 770 °C. Moving from left to right within the panel, the product was analyzed by SEM while increasing the magnification. The scale bars (starting from the left) within the panel are: for panel III: 100, 10, 3 μm (various electrolyses), and 2 μm; for panels IV and V: 5, 2, 1, and 1 μm; for panel VII: 50, 30, 20, and 15 μm; for panel VIII: 50 μm 10, 1, and 2 μm.

[0199]

[0139] The first row (panel #III) of Figure 2 presents the SEM of the product of electrolysis #III, continuing to use a low current density and showing a similar Coulomb efficiency of 78%, focusing on the addition of Ni powder to the electrolyte, purifying the anode to Inconel 718 with two layers of Inconel 600, at which point it rises to 89 wt% of the nanofiber product. Further, this electrolysis used an "aged" electrolyte (not depicted in the table). The newly melted electrolyte takes time (up to 24 hours) to reach a steady-state equilibrium (pre-equilibration process). In electrolysis #III, after aging the electrolyte for 24 hours, it was melted and then the electrodes were immersed. However, it was observed that aging is disadvantageous for maximizing the nanofiber yield. Final purification of the newly dissolved electrolyte and immediate use (elimination of the aging process) increases the nanofiber product to constitute 90 wt% of the product (second row of Figure 2, and electrolysis #IV in Table 2, and repeated #V). Interestingly, the 6% non-nanofiber product in electrolyses #IV and V appears to be in the form of conical carbon nanofibers, CNFs, and as seen in the second row of Figure 2, its form is its distinct triangular voids. The simplified electrolyte removes the observed CNF impurities, resulting in 95% of the nanofiber allotrope being obtained. This electrolysis #VI has a high 0.4 A / cm 2The electrolysis was performed at a current density without current-increasing activation and exhibited a Coulomb efficiency of 99.7%. This electrolysis was adjusted to have the intended excess nucleating metal, achieved through both the use of nichrome C electrodes containing Ni, Fe, and Cr (Table 1), and the direct addition of Ni and Cr powders to the electrolyte.

[0200]

[0140] Continued use of high-concentration added transition metal powders to the electrolyte, and use with low current densities but with changes in electrodes, results in another entirely different distinct nanocarbon allotrope, referred herein as "hollow nanoonions." In particular, in electrolysis #VII in Table 2 and Figure 2, the same concentration of Ni powder and electrolyte used as in electrolysis #VI and V, as well as the initial current applied, did not age and the initial current applied did not increase. However, Monel cathodes and nichrome C anodes were used, resulting in 95 wt% of products having a distinct hollow nanoonion morphology. The hollowness of the nanoonions will be revealed by TEM, while their spheroidal properties were observed by SEM in the third row of Figure 2. When the pure nickel electrolyte additive was changed to semi-nickel and semi-chromium powders, the products have a distinct "nanopearl" morphology with similarity to bead-shaped necklaces, as summarized in Table 2 for electrolysis #VIII and IX. In this case, the proportion of the product increased to 97% of this nanopearl carbon, as observed by SEM in the bottom row of Figure 2. Electrolysis #VII-IX was performed at a low current density, J=0.0A / cm². 2 It was run using and showed a 79-80% decrease in Coulomb efficiency.

[0201]

[0141] Figure 3 compares TEM images of novel nanobamboo, nanopearl, and conical carbon nanofiber (CNF) nanocarbon allotropes synthesized by molten carbonate electrolysis. As seen in the upper left panel of the figure, the CNF exhibits conical voids typical of this CNF structure. The growth of the nanobamboo is driven by nucleation, as seen in the middle left of the figure, and its nucleation region appeared to change shape as it moved from the tip of the structure inward. Without adhering to any particular theory, we hypothesized that the lateral walls forming the bamboo "knob" may be related to the periodic depletion of carbon that constructs the preceding wall. The walls of the nanobamboo and nanopearl allotropes exhibit graphene walls characterized by typical intergraphene wall separation of 0.33–0.34 nm, as described and measured by separation observed in the dense carbon plane by TEM. The lower left of the figure shows the lateral multiplicity graphene layers separating the "knob" of the nanobamboo structure. The lower left of the figure shows that an example of a nanopearl allotrope defines numerous bead-like sections extending along the longitudinal axis of the nanopearl, each of which is analogous to an individual pearl in a series of pearls. Each bead-like section contains numerous layers of curved graphene that form the respective walls of the individual bead-like sections of the nanopearl allotrope.

[0202]

[0142] Figure 4 shows an image of the elemental composition prepared by HAADF (High-Angle Annular Dark-Field TEM) and compares the TEM of nanobamboo and nanopearl nanocarbon allotropes synthesized with molten carbonate electrolyte. As can be seen from the HAADF, the nanobamboo product was pure carbon. It was with the exception of the presence of copper, which is widely distributed at low concentrations throughout, as shown in the lower left corner of the upper left panel, and may originate from the grid mount of the product sample or from the copper component when a Monel cathode is used. The HAADF probes two nanopearl samples. The first shows high or 100% concentrations of carbon (high noise level) and little or no Ni, Cr, or Fe. The second probes carbon at a higher resolution, and the increase and decrease in carbon levels were evident as the probe moved from left to right over two separate nanopearl structures. The upper right panel 402 shows the elemental profile obtained along the white arrows, from left to right within the panel. Panels 402 and 403 show HAADF data, 404 shows carbon content, 405 shows chromium content, 406 shows iron content, and 407 shows nickel content. Panel 410 on the lower right shows the elemental profiles obtained by moving left within the panel, along the white arrows. Panels 410 and 403 show HAADF data, and 404 shows carbon content.

[0203]

[0143] The top row of Figure 5 shows conical variations of bamboo carbon nanofibers and their proposed growth mechanisms, such as those formed by nickel nucleation CVD using methane and hydrogen (modified from Jia, K.; Kou, K.; Qin, M.; Wu, H.; Puleo, F.; Liotta, LF Controllable and Large-Scale Synthesis of Carbon Nanostructures: A review of Bamboo-Like Nanotubes. catalysts 2017, 7, 256, open access). The lower left panel of Figure 5 shows modified entangled bamboo nanocarbons by CVD, and the upper right panel of the schematic diagram shows the proposed growth mechanism (modified from Zhang, M. He, C.; Liu, E.,; Zhiu, S., Shi, C.; Li, J.; Li, Q.; Zhao, N. Activated Carbon Nano-Chains with Tailored Micro-Meso Pore Structures and Their Application for Supercapacitors. J. Phys. Chem. C, 2015, DOI: 10.1021 / acs.jpcc.5b05480). The lower right panel of Figure 5 shows the typical graphene layer structure produced by carbon nanofibers (modified from Yadav, D.; Amini, F.; Ehrmann, A. Recent advances in carbon nanofibers and their applications - A review. European Polym. J. 2020, 138, 109963). In Figure 5, 502 shows the chemical vapor deposition reaction of CH3 and H2 on nickel particles. Strong strain is indicated by 504, and graphite shell stress 506 is shown. Particle jumps 508 are also shown, resulting in conical holes 510.

[0204]

[0144] Conical CNF, nanobamboo, and nanopearl are novel and unusual high-yield carbon allotropes synthesized by molten electrolytes. Similar CVD synthesis forms have been synthesized by CVD. In particular, CVD conical CNF structures have been widely characterized, as shown in the upper row of Figure 5. It has been shown that the conical CNF morphology in CVD is due to the shape deformation of the nucleating (Ni) metal induced by repeated stress, which causes the metal particles to jump and bridge the allotrope walls, forming the observed lateral graphene separation. Spherical, spaced nanobamboo and nanopearl allotropes have been observed, though less common in CVD. An example is shown in the lower left row of Figure 5, whose structure was attributed to the periodic formation of pores within the structure due to defects in the outer layer. One specific application example of bamboo CVD CNTs is their use as a platform for constructing layer-based biosensors. Generally, carbon fibers are classified as amorphous, or as being constructed from graphene plates, carbon nanotubes, or conical structures, as shown in the lower right of Figure 5.

[0205]

[0145] Figure 6 shows the TEM and HAADF elemental analysis of hollow nanoonion allotropes synthesized by molten carbonate electrolysis. Panel A shows hollow nanoonions, panel B shows hollow nanoonions with and without trapped metals; panel C shows hollow nanoonions with trapped metals; and panel D shows hollow nanoonions with and without trapped metals. Panel 602 shows the elemental profiles obtained along the white arrows to the left of the panel. In panel 602, 604 shows the carbon content, 605 shows the iron content, and 606 shows the nickel content. Panel 610 shows the integral atomic fraction on region D #1, where carbon is approximately 98.1% and nickel is approximately 1.9%. Panel 620 shows the integral atomic fraction on region D #2, where carbon is substantially 100% (therefore, not considered, any copper content that may be present due to the method used to prepare the sample for analysis).

[0206]

[0146] Figure 6 shows the TEM and elemental composition by HAADF of a new hollow nano-onion nanocarbon allotropes synthesized by molten carbonate electrolysis. The hollow nano-onions define an internal core. As shown, part of the nano-onion internal core contains metal, while the other is substantially empty (void / hollow). The walls of the hollow nano-onions are composed of graphene layers, as characterized by a typical graphene inter-wall separation of 0.33 - 0.34 nm, measured as shown in the figure and by the separation observed between dense TEM carbon planes. As seen in the HAADF of Figure 6, the nano-onions are pure carbon when the core is hollow, and the metal is nickel, or a combination of nickel and iron when the core contains metal.

[0207]

[0147] Example 2 Electrochemical conditions for synthesizing CNT products with nickel-coated CNTs, nano-onion allotropes, or nanoflower allotropes

[0208] 【0*148】 Figure 7 shows SEM of CNT products of carbon nanoflowers, nano-onions, and nickel-coated CNT allotropes by electrolytic separation of CO2 in Li2CO3 at 770 °C. Moving from left to right in the panels, the products were analyzed by SEM with increasing magnification. The scale bars (starting from the left) in Panel XI are: 150, 20, 15, and 2 μm; in Panel XII: 50 μm; in Panel XIII: 50 and 15 μm; in Panel XIV: 100, 30, 15, and 10 μm; in Panel XV: 100 μm, 30, and 5 μm.

[0209]

[0149] Nickel anodes or excess nickel doping result in nickel-coated CNTs. Rather than forming alternative allotropes such as nanobamboo or nanopearl, the use of excess nickel tends to coat carbon nanotubes with nickel, especially when used with: (i) stainless steel cathodes; (ii) even higher electrolytic current densities when utilized; and (iii) activation by initial current increase. This is summarized in the top row of Table 3 as electrolysis #X, where 0.81 wt% Ni powder was added to the Li2CO3 electrolyte and nichrome C was used as the anode. The electrolysis was 0.20 A / cm². 2 The experiment was run at 0.15 A / cm² and showed a Coulomb efficiency of 98.9%. The Ni coating was further improved in electrolysis XI, as shown in Table 3 and the top row of Figure 7, when a pure nickel anode was used instead of nichrome C, but when Ni powder was not added to the electrolyte and when current increase was not used (it appears even more uniform in SEM). The electrolysis was performed at 0.15 A / cm². 2 It was executed and showed a Coulomb efficiency of 93.4%.

[0210]

[0150] While not adhering to any particular theory, the presence of an excess amount of nickel, in relation to other distinct operating parameters of the electrolytic reaction, is involved in the external coating of nickel formed on the outer surface of the CNTs. Excess nickel can be established in the electrolytic reaction as a result of the melting point of Li2CO3 of the additive (containing metal oxides or metal salts as metals) being 723°C. Another inner wall of the electrolytic cell decomposes during the electrolytic reaction, the cathode decomposes during the electrolytic reaction, the anode decomposes during the electrolytic reaction, or any combination of these. Thus, when the method uses other distinct operating parameters—including steel cathodes—that result in nickel-coated CNTs, an excess amount of other metals or metal-containing compounds can also result in CNTs coated with other metals. For example, an excess amount of metal—other than nickel—but not limited to, for example: iron, titanium, tin, copper, vanadium, cobalt, zinc, magnesium, aluminum, ruthenium, silver, iridium, palladium, rhodium, and platinum is thought to result in metal-coated CNM products and metal-coated CNT allotropes in CNM products. Furthermore, excess amounts of metal mixtures, metal oxides, or any combination thereof are also contemplated herein. In summary, a coating on an allotrope containing one metal, a metal mixture, or a metal oxide is collectively referred to as a metal-coated allotrope.

[0211]

[0151] In some embodiments of the present disclosure, the entire CNM product may be coated. In some embodiments of the present disclosure, a desired allotrope in the CNM product may be coated with a metal. For example, using embodiments described herein, the method may be used to coat one or more desired allotropes with a metal, such desired allotropes include, but are not limited to: metal-coated carbon nanotubes (CNTs), metal-coated graphite carbon, metal-coated nanobamboo, metal-coated conical carbon nanofibers, metal-coated nanopearls, metal-coated nanoonions, metal-coated hollow nanoonions, metal-coated nanoflowers, metal-coated nanodragons, metal-coated branch and trunk CNTs (metal-coated nanotrees), metal-coated nanobelts, metal-coated nanorods, metal-coated long and / or linear CNTs, metal-coated high aspect ratio CNTs, metal-coated thin CNTs, and macroscopic assemblies of CNTs, including densely packed linear metal-coated CNTs, metal-coated nanosponges, and metal-coated nanowebs. In some embodiments of the present disclosure, the relative amount of metal-coated allotropes—of the total amount of allotropes present in the CNM product—is between about 5% by weight and about 99.5% by weight. In other embodiments of the present disclosure, the relative amount of metal-coated allotropes is between about 7.5% by weight and about 97.5% by weight, between about 10% by weight and about 15% by weight, between about 20% by weight and about 92.5% by weight, or between about 30% by weight and about 90% by weight.

[0212]

[0152] While not adhering to any particular theory, the exclusion of transition metals from the molten electrolytic environment may hinder their activity as nucleation sites for carbon growth and potentially inhibit the growth of carbon nanotubes. Suppression of metallic nucleation growth of CNTs, such as through the use of noble metal anodes, has been an effective means of promoting the growth of another nanocarbon: carbon nanoonions. Here, another molten electrolytic pathway was found to ensure a high nanoonion product yield through the addition of lithium phosphate to the electrolyte. As summarized in Electrolytics XII and XIII in Table 3, the addition of 8 wt% Li3PO4 to the Li2CO3 electrolyte resulted in a product that was nearly pure (97-98%) carbon nanoonions, as summarized in Table 3. This nanoonion product was suitable for a wide range of electrolytic synthesis current densities (0.08-0.20 A / cm²). 2 In the case of ), it was observed that either Muntz brass or Monel was used as the cathode, and that the electrolysis included an initial current rise step (electrolysis #XII) or not (electrolysis #XIII).

[0213]

[0153] Various low current densities, Muntz brass cathodes, nichrome C anodes, and aged electrolytes yield attractive new high-purity fused electrolytic nanocarbon allotropes: nanoflowers. In particular, after 24 aging of the electrolyte, an excess (0.081 wt%) of chromium metal powder was added to the electrolyte. The electrolysis was 0.08 A / cm². 2The process is performed and shows a Coulomb efficiency of 78%. Repeated electrolysis (as electrolysis #14 and #15) yields the same results as summarized in Table 3, shown by SEM in Figure 7. As seen in the lower right panel of Figure 7, the product appears as hollow tubes within a flower morphology. Magnification of these hollow tubes by TEM HAADF (not shown) ensures that they arise individually and together as interconnected aggregates. However, the morphology of the product is quite unusual in some aspects. Numerous CNTs arise from an origin that gives rise to a flower-like arrangement. Without adhering to any particular theory, this may represent basal growth rather than tip growth, and multiple growth patterns activated from a single activation point. An alternative mechanism to be investigated is tip growth, where the metal nucleated tip is sintered (decreasing in size) as growth progresses, and the continued growth with it may reduce the diameter of the nanocarbon product. The CNTs appear as short, very linear spikes. The carbon nanotubes (CNTs) are frustoconical in shape, with their diameter decreasing as they extend away from their origin. Small percentages of plate-like and garnet-like material were scattered throughout the floral arrangement. While novel as the majority of molten electrolytic CNM products, nanoflowers have been observed and described not only from carbon but also from gold, platinum, and silver, as well as from zinc and titanium oxides.

[0214]

[0154] [Table 3]

[0215]

[0155] Example 3 Electrochemical operating parameters for synthesizing CNM products with desired allotropes of nanodragons, nanotrees, nanobelts, and nanorods.

[0216]

[0156] Figure 8 shows SEM images of CNM products of carbon nanodragons, nanotrees, nanobelts, and nanorod allotropes by electrolytic separation of CO2 in Li2CO3 at 770°C. Moving from left to right within the panels, the products were analyzed by SEM with increasing magnification. Starting from the left, the scale bars in panel K are: 50, 10, 5, and 5 μm; in panel Q: 100, 100, 5, 1, and 100 μm; in panel Y: 50, 5, and 5 μm; in panel Z: 30, 10, 5, and 1 μm.

[0217]

[0157] Figure 9A shows TEM and HAADF elemental analysis of nanoflower allotropes synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. Panel 904 shows the elemental intensity profile obtained along the white arrow. Panel 906 shows the elemental intensity profile obtained along the white arrow to the left in the panel. Figure 9B shows TEM and HAADF elemental analysis of nanodragon carbon allotrope 902 synthesized by molten carbonate electrolysis according to an embodiment of the present disclosure. Panel 910 shows the integral atomic fraction on region E #1 where carbon is substantially 100% (no copper content is considered).

[0218]

[0158] Figure 10 shows the HAADF elemental analysis of nanotree carbon allotropes synthesized by molten carbonate electrolysis. Panel 1010 shows the elemental intensity profile obtained along the white line from left to right in Panel I below, where 1011 shows the carbon content, 1012 shows the iron content, and 1013 shows the nickel content.

[0219]

[0159] Figure 11 shows a schematic diagram illustrating the observed CVD-synthesized amorphous branched carbon nanotree growth catalyzed by iron carbide (included as yellow domains). In the left panel, a-f and g-k show fractions of yellow iron carbide nucleation sites resulting in one or more purple carbon branches (modified from Takai, A.; Ataee-Esfahani, H.; Doi, Y.; FuiqE, M.; Yamauchi, Y.; Kuroda, K. Pt nanoworms: creation of a bumpy surface on one-dimensional (1D) Pt nanowires with the assistance of surfactants embedded in mesochannels. Chem. Comm. 2011, 47, 7701-7703). The right panel shows a schematic diagram illustrating the structure of CVD-synthesized carbon nanobelts (modified from He, Z.; Maurice, J.-L. Lee, CS; Cojocaru, CS; Pribat, D. Growth mechanisms of carbon nanostructures with branched carbon nanofibers synthesized by plasma-enhanced chemical vapor deposition. Cryst. Eng. Comm. 2014, 16, 2990-29995).

[0220]

[0160] Figure 12 shows the TEM and HAADF elemental analysis of nanobelt carbon allotropes synthesized by molten carbonate electrolysis. Panel 1206 shows the elemental intensity profile obtained along the white line to the left in lower panel E, 1207 shows the HAADF data, 1208 shows the carbon content, 1209 shows the iron content, and 1210 shows the chromium content.

[0221] [

[0161] ]Figure 13 shows TEM and HAADF elemental analysis of nanorod carbon allotropes synthesized by molten carbonate electrolysis. The upper right panel shows the integrated atomic fraction on region #1, where the carbon content is about 90.6% and oxygen is about 9.4%. The lower right panel shows the integrated atomic fraction on region #1, where the carbon content is about 93% and oxygen is about 7%.

[0222] [

[0162] ]Variations in the electrochemical conditions for CNT product formation for electrolysis #XVI result in a change in the allotrope from carbon nanotubes to another fascinating form herein referred to as nanodragons, which are presented in Table 3 and Figures 8 and 9B. Changes from the initial synthesis that produced CNTs under similar conditions include an Inconel 718 anode instead of nichrome C and a higher current density of 0.4 A / cm 2 instead of 0.1 A / cm 2 (showing 100% Coulombic efficiency), and the electrolyte was not aged. Unlike other uniquely electrochemically synthesized nanocarbon forms, carbon nanodragons do not consist of simple repetitive geometries; rather, nanodragons contain a complex combination of cylinders, small plates, and spheres. As shown in Figure 9B, nanodragons generally have an elongated CNT body with small "legs" or protrusions extending away from the elongated body. The protrusions include smaller branched CNTs, small nodules of metal growth, or any combination thereof.

[0223] [

[0163] ]It is known that the addition of low levels of lithium oxide resulted in high-quality CNTs. The use of specific anodes (Inconel 718 with two layers of Inconel 600) maintained the quality of the product, but the morphology of the CNTs changed substantially. The inventors have already observed greater transition metal nodule growth from CNTs. The addition of Li2O results in branched carbon nanotrees, included as electrolysis #XVII in Table 3 and Figure 8. The electrolysis was at 0.13 A / cm 2The process was performed at 0.08 A / cm², exhibiting a Coulombic efficiency of 98.7%. The nanotrees show clear growth of smaller CNT branches emanating from larger CNT trunks. The red circular areas in the right panel of electrolysis #XVII in Figure 8 show examples of branched y-sections. The addition of low levels of iron oxide results in high-quality CNTs. However, with 24 hours of aging of the electrolyte and subsequent additions as shown in Table 3 and electrolysis #XVIII in Figure 8, alternative planarized nanocarbon allotropes are observed, which we refer to herein as nanobelts. The electrolysis was performed at 0.08 A / cm². 2 It was run and showed a Coulomb efficiency of 79%. The nanobelt structure appears to consist of planarized (or "shrunken") carbon nanotubes.

[0224]

[0164] TEM and HAADF elemental analyses of nanoflower, nanodragon, nanobelt, and nanotree structures are shown in Figures 9A, 9B, 10, 12, and 13.

[0225]

[0165] Figure 9A shows the elemental composition of a novel nanoflower nanocarbon allotrope synthesized by molten carbonate electrolysis, measured by TEM and HAADF. As shown, the main component of the nanoflower is one or more interconnected tapered tubes containing bulbous sections at regular intervals. The walls consist of graphene layers, as indicated in Figure 9A and measured by separation observed between dense TEM carbon planes, characterized by typical intergraphene wall separation of 0.33–0.34 nm. As seen in the HAADF image, the nanoflower contains not only Cu but also small amounts of cobalt.

[0226]

[0166] In Figure 9B, the nanodragon structure was observed as a complex graphite structure. Structures with an appearance similar to Pt rather than C have already been observed and described as a rough surface on a one-dimensional Pt nanowire. The nanotree allotrope, which consists of CNTs but differs from conventional CNT structures that generally do not contain fused CNTs, is shown in Figure 10. However, the nanotree morphology contains intersecting CNTs as seen in Figure 10, and its structure appears to be fused and branched from one another. A nanocarbon CVD growth branching mechanism has been suggested, catalyzed by fractions of nucleation sites that result in carbon branching, as shown in Figure 11. In Figures 10 and 12, it can be seen that the interiors of the nanotree and nanobelt can contain nickel and iron, or nickel, respectively, within the structure. As seen in Figure 12, the nanobelt product is flat and consists of a graphene layer in addition to the measured presence of nickel, and the mechanism of this unusual flat morphology was revealed by TEM. CVD nanobelt CNT structures have already been synthesized in the schematic structure exemplified on the right side of Figure 11.

[0227]

[0167] Low current density (0.08 A / cm²) without aging of the electrolyte (newly melted electrolyte) 2, (showing 80% Coulomb efficiency), long-term growth (18 hours) of carbon nanotubes with a Monel cathode, an iridium anode, containing 0.81% Ni, and a non-ramping current activation process, resulting in the squat ring-like nanorod allotrope as seen in Figure 13, and including it in Table 4 as Electrolysis XIX. Among the allotropes presented in this specification, the product was unusual from two physicochemical perspectives. First, the TEM of Figure 13 reveals no evidence of a layered graphene structure. However, as shown in a later section, this morphology exhibits XRD peaks and Raman spectra typical of a graphite-layered graphene structure. Second, as seen in the elemental analysis of Figure 13, the nanorods are the only new melt-synthesized nanocarbon structure, and a significant concentration of oxygen (7.0 - 9.4 wt%) was observed. In the growth where the length of the CNT along its diameter increases over time, in the bulbous rod-like morphology, it seems consistent with the long-term growth being dominated by an increase in diameter rather than length.

[0228]

[0168] Example 4 Raman Spectroscopy and XRD Analysis of Various Nanocarbon Allotropes

[0229]

[0169] Figure 14 shows SEM images of nanocarbon allotropes synthesized by electrolytic separation of CO2 in molten carbonate according to embodiments of the present disclosure. Top and middle rows: Introduced and synthesized nanocarbon allotropes according to embodiments of the present disclosure. Bottom row shows nanocarbon allotropes already synthesized. Top row (from left to right): Conical CNF (Panel A), Nanobamboo (Panel B), Nanopearl (Panel C), Ni-coated CNT (Panel D), Nanoflower (Panel F), and Nanodragon (Panel F). Middle row: Nanorod (Panel G), Nanobelt (Panel H), Nanoonion (Panel I), Hollow Nanoonion (Panel J), and Nanotree (Panel K). Downward row (from left to right): CNTs, nanoscaffolds (panel L, image from Wang, X., Licht, G.; Liu, X.; Licht, S. One pot facile transformation of CO2 to an unusual 3-D nan-scaffold morphology of carbon. Sci Rep. 2020, 10, 21518), nanoplatelets, graphene (two-step process, image from Liu, X., Wang, X., Licht, G., & Licht, S. Transformation of the greenhouse gas carbon dioxide to graphene. J. CO2 Util., 36, 2020, 288-294), nanohelicals (Liu, X.; Licht, G.; Licht, S. The green synthesis of exceptional braided, helical carbon nanotubes and nanospiral platelets made directly from CO2. Mat. Today Chem 2021, 22, (Image from 100529).

[0230]

[0170] Figure 15 shows Raman's descriptions of CNM products consisting of various labeled nanocarbon allotropes and packed carbon nanotube assemblies synthesized by electrolytic separation of CO2 in Li2CO3 at 770°C under systematically different electrochemical operating parameters. Table A below provides reference numbers and associated features used in Figures 165 16A and 16B.

[0231]

[0171] [Table 4]

[0232]

[0172] Figure 16 shows the XRD analysis of CNM products consisting of various nanocarbon allotropes synthesized by electrolytic separation of CO2 in Li2CO3 at 770°C under various systematically varying electrochemical conditions.

[0233]

[0173] The top and middle rows of Figure 14 compare microscopic images of novel carbon allotropes fabricated according to embodiments of the present disclosure with structures in a second row already formed by fusion electrolysis. The novel electrolytically synthesized structures shown are conical CNF, nanobamboo, nanopearl, Ni-coated CNT, nanoflower, nanodragon, nanorod, nanobelt, nanoonion (also synthesized by alternative methods), hollow nanoonion, and nanotree. Previously distinct nanocarbon structures synthesized were carbon nanotubes, nanoplatelets, graphene (two-step synthesis by CO2 fusion electrolysis and other exfoliation), and nanohelics.

[0234]

[0174] Figure 15 shows the effect of various electrolysis conditions on the Raman spectrum and XRD of a new carbon product of CO2 electrolysis in Li2CO3 at 770°C. Graphite fingerprints are shown from 1880–2300 cm⁻¹. -1 It is located in the area and is involved in various collective vibrations of sp hybrid CC couplings. Tangent G band (approximately 1580 cm²) -1 E 2GDerived from a symmetric graphite-like in-plane mode, it can be divided into several modes, two of which are the clearest: G1 (1577 cm²). -1 ) and G2 (1610cm -1 The Raman spectrum shows two sharp peaks, approximately 1350 and 1580 cm⁻¹. -1 These show disordered induced modes (D-band) and high-frequency E 2G Each corresponds to the primary mode (G band), with an additional peak, the 2D band, at 2700 cm. -1 This was shown. The G' peak at approximately 2300 appeared to be related to collective stretching oscillations of sp hybrid CC couplings.

[0235]

[0175] In this specification, I D / I G The intensity ratio between the D band and the G band (I D / I G ) is a useful parameter for evaluating the relative number of defects and the degree of graphitization, and therefore I D / I G The ratio can be presented as a range of values ​​(or as a specific numerical value) to distinguish one type of nanocarbon structure from others, such as the allotropes described herein. Table 4 summarizes the Raman band peak positions calculated for various carbon allotropes (I D / I G ) and (I 2D / I G ) Includes peak ratio. Higher ratio I D / I G , or I G Frequency shifts are considered a measure of the increasing number of defects in the carbon-graphite structure. Potential defects in the graphite structure are typical carbon sp² in the hexagonal carbon configuration within the graphene layer containing that structure. 2 bond, sp 3 This could involve substitution, increasing pores or lost carbon within graphene, and enhancing defects that cause the formation of heptagonal and pentagonal structures rather than the conventional hexagonal graphene building blocks of graphene.

[0236]

[0176] [Table 5]

[0237]

[0177] Typically, I relating to multi-walled carbon nanotubes D / I G The range is from 0.2 to 0.6. Compared to these values, excluding hollow nanoonions, the novel carbon allotropes produced by embodiments of this disclosure are generally 0.6I D / I G They show higher values ​​than this, which is evidence of an even higher number of defects and is probably consistent with the greater morphological complexity of these new allotropes. Nanobamboo, nanopearl, nanorod, and nanobelt each show relatively high levels of defects, which are often sp 3 This is attributed to the increased number of pores, twists, and turns in the structure, resulting from the higher presence of carbon. As observed in Table 4, the increasing I D / I G The order of the ratios is: CNT < Hollow Nano Onion < Dragon < Flower < Nano Tree < Bamboo < Pearl < Rod <CNF<ベルト That is the case.

[0238]

[0178] The shift of the G-band frequency ν to higher frequencies is generally observed in I D / I G The fluctuations correlate with the fluctuations caused by nearby ratios, with the exception of the unusually large shift observed for nanobamboo.

[0239]

[0179] High levels of Ni, Cr, or Co added to electrolytes (nanobamboo, nanopearl, and nanoflower allotropes) also appear to correlate with an increase in defects, and the very high levels of Ni powder used in nanorod synthesis are I G Frequency shift and I D / I GThis correlates with very high levels of defects, as indicated by the increase in [amount]. Already, increased concentrations of iron oxide added to the Li2CO3 electrolyte correlated with increased disorder within the graphite structure. Interestingly, synthesis with low levels of added iron oxide powder (but only added 24 hours before aging of the electrolyte) yields allotropes with the highest levels of defects, nanobelt allotropes.

[0240]

[0180] Lower defects are associated with applications requiring high conductivity and strength, while higher defects are associated with applications that enable high diffusion rates through structures such as those related to increased intercalation and supercapacitors with higher anode capacity and higher charge in Li-ion batteries.

[0241]

[0181] Along with an XRD library of related compound spectra, the XRDs of novel nanocarbon allotrope products prepared according to embodiments of this disclosure are presented in Figure 16, summarized in Tables 2 and 3, and SEMs are presented in Figures 2, 7, and 8. Each spectrum shows a strong, sharp diffraction peak at 2θ=27°, characteristic of the graphite structure, and there is no indication of a broad peak indicating amorphous carbon. In addition to graphite (carbon), the product XRDs are divided into groups that contain metal salts. Nanobamboo contains lithium nickel oxide (Li2Ni8O) 10 The simplest composition is shown, consisting only of ). Next, the most complex compositions are found in Figure 18 to be the nanodragon, hollow nanoonion nano, and nanotree allotropes, which contain iron carbide salt Fe3C, lithium nickel oxide, and carbon. In Figure 18, panel 1802 shows the elemental intensity analysis obtained along the white arrow in the left of panel D. Panel 1804 shows the integral atomic fraction on the region in the green box, where carbon is approximately 94.3%, iron is approximately 2.5%, and nickel is approximately 3.2%. In panel 1806, the integral atomic fraction on the region in the green box is approximately 100% carbon. Next, the most complex composition is shown in the figure in the lower left corner, the aforementioned metal salt (Li2Ni8O 10The nanoflowers are shown with respect to the Fe3C) and lithiated chromium(III) salts, respectively. Finally, it should be noted that both nanopearls and nanobelts contain additional lithiated copper salts (lithium copper oxide, Li2CuO2), and they were synthesized with Muntz brass and Monel cathodes, respectively, both containing copper. In order to penetrate the nanocarbon, the copper may need to dissolve from the cathode, which was under cathode bias. This did not occur in the other nanocarbon allotrope products of this disclosure. The nanobelt XRD spectrum is distinctly different from the others, with a main peak at 2θ=43°, which reflects a higher concentration of metal than in the other products. Li2Ni8O 10 The presence of reduced defects, already described by Raman spectra for the hollow nanoonion morphology, along with the presence of XRDs of LiCrO2 and Fe3C, provides evidence that the simultaneous presence of Ni, Cr, and Fe as nucleating agents can reduce defects in the structure compared to Ni. On the other hand, the presence of enhanced defects, already described by Raman spectra for the nanobelt and nanopearl morphology, along with the presence of XRDs of LiCuO2, provides evidence that copper salts increase defects in the structure compared to Ni, Fe, or Cr as transition metal nucleating agents. Finally, it should be noted that the single addition of cobalt powder (among all electrolytics) to electrolytics XIV and XV must correlate with the subsequent observed formation of nanoflower allotropes. However, the majority of this cobalt does not proceed toward products such as those analyzed by XRD in Figure 16, and is only observed in trace amounts by HAAFD TEM (to be revealed and investigated in future studies), and likely plays another role in promoting the formation of this unusual product.

[0242]

[0182] Without being bound by any particular theory, the nanocarbon allotropes fabricated by embodiments of this disclosure may result in unusual physicochemical properties and suggest usefulness for applications such as utilizing the high strength, high thermal, magnetic, electrical, piezoelectric, and tribological properties of graphene-based materials, although these properties are distributed in various ways across the unusual geometries of these novel allotropes. For example, alternative applications such as high-capacity lithium anodes, rare electronics, EMF shielding, improved lubricants, and new structural or polymer composites are envisioned.

[0243]

[0183] Examples 1 to 4 describe nanocarbon allotropes prepared according to embodiments of the present disclosure, which were analyzed by SEM, TEM, TEM with HAADF, Raman, and XRD. Except for the nanorod structures, each structure was graphite-like, containing graphene layers arranged in various geometric shapes. The graphene layers exhibited characteristic interlayer spacings of 0.33–0.34 nm. Each structure was pure carbon, except for the presence of Ni, Fe, Cr, and sometimes Cu, which can act as nucleation growth sites. Generally, intersecting graphene layers do not fuse, and in nanotree allotropes, the graphene layers bend at the intersections, resulting in the observed branched structures.

[0244]

[0184] Many of the structures, including nanobamboo, nanopearl, Ni-coated CNT, and conical CNF, exhibit walls containing concentric graphene layers. Nanodragon and nanobelt structures include layered planar or planar-twist graphene layers. Some of the observed structures, including nanotrees, as well as hollow and filled nanoonions, exhibit concentric, highly spherical graphene layers that are generally composed of carbon and contain low levels of internal transition metals. Without being bound by any particular theory, embodiments of the present disclosure may provide novel synthetic routes for the formation of nanoonions via the addition of phosphates to electrolytes, which can be facilitated by phosphates that selectively bind transition metal ions.

[0245]

[0185] All electrochemical methods progressing from electrolysis #IV produce high-purity products of the described allotropes, with the exception of small amounts (6%) of conical CNF and moderate-purity (85%) nanobelt carbon products in most nanobamboo carbons. The Coulomb efficiency of the electrolysis is 0.08 A / cm². 2 It ranges from 79 to 80% at a lower current density, 0.2 A / cm². 2 At or higher current densities, purity exceeded 99%. Each high-purity product exhibited a sharp XRD graphite peak and moderate levels (0.3–1.3) of Raman I, showing moderate levels of defects in the carbon structure. D / I G The ratios were shown. In addition to the majority of pure graphite carbon, XRD also revealed various single or mixed transition metal salts of iron carbide, or nickel, chromium, or copper lithium oxides.

[0246]

[0186] TEM HAADF of the novel nanocarbon allotropes showed that their internal cores were almost metal-free (voids, walls 100% carbon), but in other regions, the voids were filled with transition metals Ni, Fe, and / or Cr. Except for the nanorod allotropes, each allotrope contained a distinct graphene layer with graphene properties, the interlayer spacing of which was 0.33–0.34 nm. Depending on the allotrope, adjacent graphene layers were organized into planar, cylindrical, or spherical geometric shapes. When internal transition metals were present within the allotrope chip, the layered graphene walls were observed to bend to be highly spherical around the metal supporting the transition metal nucleated CNT growth mechanism. The use of nickel anodes or excess nickel added to the electrolyte resulted in coated nickel-coated CNTs when stainless steel was used as the electrolytic cathode. Generally, intersecting graphene layers do not fuse, but in nanotree allotropes with trunk CNTs and branch CNTs extending away from the trunk CNTs, the graphene layers bend (or are bent) to become part of the CNT intersections that coincide with the branching.

[0247]

[0187] Without adhering to any particular theory, molten carbonate electrolysis of CO2 provides a viable pathway for the synthesis of a portfolio of rare and valuable nanocarbon allotropes, as shown in Examples 1–4. Mass production of these allotropes from CO2 could provide a valuable incentive for consuming this greenhouse gas. Such allotropes are rare, or have never existed before, and are not generally commercially available. However, those in use, such as nanoonions—known to be produced by the thermal decomposition of nanodiamonds or by CVD—have a high carbon footprint and associated costs exceeding $1 million / ton. CNT production by molten carbonate electrolysis of CO2 is a low-cost synthesis, comparable in cost to the separation of aluminum oxide in the industrial production of aluminum. The novel allotrope synthesis conditions consist of small variations in a scaled molten carbonate electrolysis process, via a clear and equivalent pathway that has been scaled up to contribute to CO2 consumption and climate change mitigation.

[0248]

[0188] Example 5 Electrolytic operation parameters for producing CNM products with high purity / high yield of CNTs

[0249]

[0189] Further embodiments of the present disclosure relate to electrochemical process conditions that yield high-purity, high-yield CNT products by electrolysis of CO2 in lithium carbonate at 770°C. A detailed investigation of the material composition and morphology of the product was carried out, particularly around the transition metal nucleation zone of CNT growth. The latter part of this finding reveals the molten electrochemical conditions that produce the macroscopic assembly of CNTs.

[0250]

[0190] Figure 17 shows SEM images of high-purity, high-yield CNM products of carbon nanotubes under various electrochemical conditions by electrolytic separation of CO2 in Li2CO3 at 770°C. Washed products were collected from the cathode following the electrolysis described in Table 5. Products were analyzed by SEM while increasing magnification, moving from left to right across the panels. The panel scale bars (starting from left) are: Panel A: 100, 50, and 10 μm; Panel B: 100, 20, and 5 μm; Panel C: 40, 5, and 2 μm; Panel E: 200, 40, and 10 μm.

[0251]

[0191] [Table 6]

[0252]

[0192] By systematically varying the electrochemical process conditions for high-purity CNT synthesis, other electrochemical conditions supporting high-purity, low-defect synthesis of linear (non-helical) CNTs were determined. Examples of the variously varying conditions include: cathode composition, anode composition, additives to the lithium carbonate electrolyte, current density, and electrolysis time. Electrode types include the use of cathode metal electrodes such as Muntz brass Monel or nickel alloys. Anode types include noble metal anodes, e.g., iridium, various nickel-containing anodes containing nickel, nichrome A or C, Inconel 600, 625, or 718, or specific layered combinations of these metals. Variously varying electrolyte additives include Fe2O3 and nickel or chromium powder, and electrolysis is varied over a wide range of electrolysis current densities. Several electrolysis studies in this specification that yield high-purity, high-yield carbon nanotubes are described in Table 5. Scanning electron microscopy (SEM) images of the products of various CNT synthesis methods, such as those carried out by CO2 electrolysis in molten Li2CO3 at 770°C, are shown in Figure 17.

[0253]

[0193] For electrolysis #A, the top row of Table 5 presents the electrochemical conditions, and the top row of Figure 17 shows the already described electrochemical conditions: 0.1 wt% Fe2O3 electrolysis (same lithium carbonate electrolyte, same Muntz brass cathode and nichrome C anode, same 0.6 A / cm²). 2 The current density and electrolysis duration (30 minutes) are repeated, but using stainless steel 304, a simpler (from a material standpoint) alumina (ceramic Al2O3) instead of an electrolytic cell casing, and the SEM of the product is presented. The use of alumina casing in this discovery restricts the pathways through which the metal enters and reduces the parameters for evaluating or achieving the electrolytic system. However, it should be noted that no corrosion was observed in stainless steel 304, and no significant effect was observed on the electrolytic product when switching from stainless steel to alumina. The CNT product was still 97% pure, with a Coulomb efficiency of 99%, which quantifies the available charge measured for the number of electrons measured per equivalent of C in the product (current multiplied by electrolysis time), and the length of the carbon nanotubes was 50-100 μm.

[0254]

[0194] In the second row of Figure 17 (Panel #B), the current density changes to 0.15 A / cm². 2 The current density decreases to 4 hours, and the electrolysis time increases to 4 hours. The results of these modifications are a decrease in product purity to 94%, a reduction in CNT length to 20–80 μm, and a moderate decrease in Coulomb efficiency to 98%. At this current density, the addition of 0.1 wt% Ni together with 0.1 wt% Fe2O3 results in 96% purity, non-linear, zigzag, twisted CNTs, as observed in row 3 of Figure 2, panel #C. These twists may be induced by a reduction in the control of excessive nucleation in linear CNT growth. In the most magnified of these product images (right side of Figure 17, 2 μm scale bar resolution), evidence of excessive nucleation is observed in larger nodules seen at the tips and junctions of the CNTs.

[0255]

[0195] 0.08 A / cm 2At low current densities, with an electrolyte additive of 0.1 wt% Fe2O3, conventional Muntz brass and nichrome electrodes show a significant drop in CNT product purity to 70%. Coulomb efficiency tends to decrease with current density, and in this case, the synthesis's Coulomb efficiency was 82%. Product purity can be increased by purifying the mixture of transition metals available in the electrolyte or by increasing the surface area. Alloy compositions of metals used as electrodes are presented in Table 1. Metal variability was further refined by combining the metals in Table 1 as anodes, for example, using solid sheets of one type of Inconel alloy layered with one or more screens of another Inconel alloy. This technique was performed with an Inconel 625 anode with three layers of (spot-welded) 100-mesh Inconel 600 screens, a return to a single electrolyte additive (0.1 wt% Fe2O3), and a very low current density of 0.08 A / cm². 2 This is used in the bottom row of Figure 17 (Panel #E). As seen in Panel #E of Figure 17, the product was of high purity (97%), consisted of CNTs with lengths of 20-50 μm, and had a Coulomb efficiency of 75%. Although not shown, Table 5 (Electrolysis #G) shows the same electrode and the same 0.08 A / cm². 2 Electrolysis conditions are included. However, J = 0.15 A / cm 2 Upon addition of both electrolytes, 0.1 wt% Fe2O3 and 0.1 wt% Ni, the product is twisted carbon nanotubes (CNTs) as shown in Figure 17, panel #17, with a purity of 96% and a Coulomb efficiency of 80%.

[0256]

[0196] Figure 18 shows TEM and HAADF of the CNM product of high-purity, high-yield CNTs under electrolytic #E (Table 5) electrochemical conditions by electrolytic separation of CO2 in Li2CO3 at 770°C. In the top row, the product is analyzed by TEM with a scale bar of 20 nm (left panel) or 1 nm (right). Moving from left to right in the second row, there are scale bars of 100, 5, 5, and 1 nm. The scale bars in the third row are 100 or 50 nm. The scale bars in the bottom row are 20, 1, and 1 nm.

[0257]

[0197] The synthesis listed in Table 5 defines the electrochemical growth conditions for high-purity growth of carbon nanotubes, each exhibiting a characteristic concentric multilayer graphene cylindrical wall. This is observed in Figure 18, presenting TEM and HAADF of a typical example (product of electrolysis #E, as further described in Table 5 and Figure 17) and providing schematic structural and mechanistic information of carbon nanotubes synthesized by molten electrolysis. As seen in the top row of the figure, the carbon nanotube is formed by continuous concentric layers of cylindrical graphene. The graphene is identified by its characteristic inter-graphene layer separation of 0.33–0.34 nm, measured in the figure by the spacing between the dark layers of uniform block electron permeability, in the enlarged upper right side of the figure. This CNT has an outer diameter of 74 nm and an inner diameter of 46 nm, and by counting the dark rows, the number of graphene layers in this CNT is determined to be 41. The right side of the third row of Figure 18 shows the measured carbon element profile of the CNT. This profile is swept laterally from the outside of the tube (carbon-free) by passing through the left wall (carbon), then through the void inside the tube (low carbon from the outer back wall), then through the right wall (carbon), and finally reaching the outside of the tube at the outside left side (carbon-free). Similarly, the integral elemental profile of region 1 of this panel is shown, indicating 100.0% carbon (fitting error 1.3%).

[0258]

[0198] On the right side of the second row of Figure 18, parallel 0.34 nm spacings for the graphene layer of the CNT wall are also observed. This panel also includes the dark region of trapped metal within the CNT and serves as a snapshot of the CNT growth over time. In the third row of Figure 18, the HAADF analysis of region #1 has the elemental composition for this region, including the wall, where the trapped internal metal is 94.4% carbon, 2.5% Fe, and 3.2% Ni, distributed according to the individual C, Fe, and Ni HAADF maps included in Figure 18. The second row of Figure 18 also shows the tip of the CNT containing the trapped metal. The transition metal acts as a nucleating agent, supporting the formation of the curved graphene layer shown at the tip of the CNT, which is a major component of the CNT growth mechanism. Although it occurs in a completely different physicochemical environment than chemical vapor deposition (CVD), this molten carbonate electrolysis process of transition metal nucleated CNTs appears similar to that described as occurring in CVD CNT growth. This occurs at the gas / solid interface rather than the liquid / solid interface, despite the fact that CVD is not a chemical / electrochemical process.

[0259]

[0199] Example 6 Electrolytic operation parameters for producing CNM products with high aspect ratio CNTs

[0260]

[0200] Figure 19 shows SEM images of the CNM product of high aspect ratio (and high purity and yield) CNTs separated by electrolysis #F of Table 5, with CO2 separated in Li2CO3 at 770°C, according to an embodiment of the present disclosure. The product is analyzed by SEM from left to right in the panel of Figure 19, with increasing magnification. The scale bars in panels Fa to Ff (clockwise from top) are 500, 400, 100, 5, 5, and 10 μm.

[0261]

[0201] Figure 19 shows SEM images of the products of electrochemical configurations that yield high Coulomb efficiency (99.5%), longest length (100–500 μm), and highest purity (98%) CNTs of those studied herein (described as electrolytic #F in Table 5). These are even shorter CNTs that yield nearly high purity, as in the case of the previous configuration. The synthesis used a Li2CO3 electrolyte with a 0.1 wt% Fe2O3 additive, a Muntz brass cathode, and an Inconel 718 anode, equipped with a layered Inconel 600 screen. However, this synthesis used a 2-layer Inconel 600 screen instead of a 3-layer screen, and also yielded a higher current density (0.08 A / cm²). 2 Instead, 0.4 A / cm 2 Using ) and even shorter electrolysis times (4 hours instead of 15 hours), we found optimizations for CNT purity and length. With a diameter of <0.2 μm, these CNTs can have an aspect ratio >1,000. As correlated with the alloy compositions in Table 5, a smaller number of Inconel 600 layers reflect the potential need to incorporate the anode molybdenum available in that alloy, but at controlled, even lower concentrations, the resulting high purity, high aspect ratio CNTs are realized. As shown in Figure 19, the CNTs are densely packed and parallel on a large scale, and may contain candidates useful for use in nanofiltration as discussed herein.

[0262]

[0202] Figure 20 shows the TEM and HAADF analysis of the CNM product of high-purity, high-yield CNTs produced by electrolytic separation of CO2 in Li2CO3 at 770°C under electrochemical conditions of #F (Table 5). In the upper row, the product is analyzed by TEM with a scale bar of 1 μm (left panel) or 100 nm (right). From left to right, the middle right scale bars are 50, 20, and 1 nm. Each HAADF measurement in the lower panel has a scale bar of 200 nm. Panel 2002 shows the elemental intensity data obtained along the white arrows shown in the panel, moving to the left. Panel 2004 shows the integrated atomic fraction data in the green box above, where carbon is substantially 100%. Panel 2006 shows the integrated atomic fraction data obtained from the green box above (with a white arrow inside), where carbon is approximately 92.9%, iron is approximately 6.8%, and nickel is approximately 0.3%.

[0263]

[0203] Figure 20 shows the TEM and HAADF analysis of the high aspect ratio CNT product of electrolytic #F (as described in Table 5 and by SEM in Figure 19). As seen on the right side of the middle row in Figure 20, the CNT wall consists of parallel carbon layers separated by characteristic 0.33–0.24 nm graphene intercalation. As seen in the elemental analysis of region #1 in the bottom row, the region consists of a hollow tube composed of 100% carbon. However, there are also extensive portions of the tube that are intermittently filled with metal, as seen in the TEM of the top two rows and the bottom row of the HAADF elemental profile. In the bottom row of Figure 20, the lateral cross-sectional elemental CNT profile scanned from the outside through region #2, through the CNT, and then out the opposite wall shows that the wall is composed of carbon, while the internal region also contains iron as the major metal, presenting with some nickel.

[0264]

[0204] Example 7 Electrolytic operation parameters for producing CNM products as thin CNT allotropes

[0265]

[0205] Figure 21 shows SEM images of CNM products of high-purity, high-yield CNTs under various electrochemical conditions by electrolytic separation of CO2 in Li2CO3 at 770°C. The washed product is collected from the cathode following the electrolysis described in Table 5. The scale bars (starting from left) are: panel J: 100, 4, and 2 μm; panel I: 100, 10, and 4 μm; panel K: 40, 5, and 3 μm; panel L: 40, 50, and 5 μm.

[0266]

[0206] Figure 22 shows TEM and HAADF of the CNM product of carbon nanotubes, showing nodules or buds under electrochemical conditions (Table 5, and SEM in the top row of Figure 22) by electrolytic separation of CO2 in Li2CO3 at 770°C. In the top row of Figure 22, the product is analyzed at scale bars from left to right: 200, 100, 20, and 100 nm. The scale bars in the second row are 1 μm, followed by 20, 5, 200, and 1 nm. The scale bars in the third row are 200, 20, 1, 5, and 200 nm. The scale bars in the bottom row are 50, 1, 1, and 200 nm.

[0267]

[0207] Figure 21 demonstrates that additional modifications to the electrolysis conditions can yield high-purity carbon nanotubes by CO2 molten electrolysis. Top row, panel #H shows the case of a moderate current density of 0.4 A / cm², as in the case of a high current density (Figure 17, panel #A). 2 (The same electrolyte, Muntz brass cathode, and nichrome C anode yield longer (100-200 μm), higher purity (96%) CNTs with near 100% Coulomb efficiency. In the second row (Figure 21, panel A), switching from the cathode material to Monel yields shorter 20-50 μm CNTs with 97% purity and still near 100% Coulomb efficiency. Although not shown, Table 5 (Electrolysis #D) shows the results of switching from nichrome C to a pure nickel anode (while retaining the Monel cathode, and with an electrolyte additive of J=0.2 A / cm²). 2This involves a substantial decrease in CNT purity to 70%, with the remainder of the product consisting of nanoonions. (Figure 21, panel #K, 0.4A~0.1A / cm²) 2 The decrease in current density to yields 97% pure CNTs with a length of 30-60 μm, where the Coulomb efficiency drops only slightly to 97%. In the single panel #L located in the lower left corner of Figure 21, excess Fe2O3 is added, which is observed to already cause a loss of control over the specificity of the synthesis. In this case, the overall purity of the CNTs remains high at about 95%, which consists of two distinctly different forms of CNTs in the product: the majority of the product, about 75%, are twisted CNTs, and a small number of products, about 20%, are straight CNTs. Finally, in the middle and bottom right panel #M of Figure 21, the noble metal iridium is used as the anode (along with the Monel cathode) at a low current of 0.08 A / cm². 2 It is used with current density. The transition metal released from the anode can contribute to the reduction of transition metal ions at the cathode during the formation of its stable oxide upper layer, and can act as a nucleation site for CNTs. This cannot be said here due to the high stability of iridium. Instead, 0.81 wt% Cr is prepared as an electrolyte additive, as a single high-concentration transition metal. The product is the thinnest (<50 nm diameter) of the shown, highly pure (97%) CNTs, with a length of 50-100 μm for an aspect ratio >1,000, and formed with an 80% Coulomb efficiency.

[0268]

[0208] SEM of several CNM products, particularly electrolytic #H, #B, and #C, shows evidence of nodules that appear to be “buds” attached to CNTs. These nanobud allotropes are most consistent in electrolytic #H and are further explored by TEM and HAADF in Figure 22. As seen in the top row of Figure 22, the nanobuds generally have spherical symmetry extending away from the longitudinal axis of the CNT and are not spread out in this structure, but the nanobuds appear to be equivalent to bunches of grapes growing on a vine. The nanobuds generally contain low levels of transition metal nucleating metals, for example 0.3% Fe is evident, and the rest of the structure is generally pure carbon, sometimes containing a metallic core. As seen on the left side of the second row, the CNT walls continue to show regular 0.33–0.34 inter-graphene wall separations, as seen on the right side of the row, and the junctions of adjacent CNTs may have fused or entirely different graphene structures. Similarly, as seen in the third row of Figure 17, adjacent nanobuds on a CNT may have graphene walls that bend and share to join, or, as seen in the fourth row, appear to be distinctly different (entangled, unfused) structures instead.

[0269]

[0209] Example 8 Electrolytic operation parameters for preparing CNM products with macroscopic assemblies of nanocarbon allotropes

[0270]

[0210] In addition to synthesizing individual CNTs, this Example 8 provides a series of electrolytics that generate useful macroscopic assemblies of CNTs. There is growing interest in densely packed CNTs for nanofiltration, partly due to their high density as conductive wires for artificial neural networks. The macroscopic assemblies fabricated by embodiments of this disclosure are referred to as nanosponges, densely packed parallel CNTs, and nanoweb CNTs in Table 6 and Figure 23.

[0271]

[0211] [Table 7]

[0272]

[0212] Figure 23 shows SEM images of CNM products consisting of carbon nanotubes arranged and configured in various packed macroscopic structures, also called macroassemblies adapted to various applications including nanofiltration as described herein. Washed products are collected from the cathode following electrolysis as described in Table 6. From left to right in the panel, the products are analyzed by SEM at increasing magnification. Identified allotropic components include nanosponges, densely packed linear CNTs, and nanoweb CNTs. From left to right in the panel, the products are analyzed by SEM at increasing magnification. Scale bars in the panel (starting from left) are: panel N: 500, 40, and 20, and 8 μm; panel P: 400, 10, and 5 μm; panel d: 300, 40, and 5 μm; panel Q: 500 μm, 40, 20, and 8 μm.

[0273]

[0213] The nanosponge allotrope is subjected to a process where nichrome C acts as both the cathode and anode, 0.81% Ni powder is added to a Li2CO3 electrolyte at 770°C, and the initial current increases upward (0.008, 0.016, 0.033, and 0.067 A / cm²). 2 (5 minutes each), followed by 0.2 A / cm² for 4 hours. 2 Formed by electrolysis at a current density of #N, 97% pure nanosponges were generated with a Coulomb efficiency of 99%. As already described, long, densely packed parallel carbon nanotubes were formed by electrolysis at #F, with 0.1 wt% Fe2O3 on a Li2CO3 electrolyte, a Muntz brass cathode, an Inconel 718 anode, and a 2-layer Inconel 600 screen at 0.15 A / cm². 2The nanoweb was generated by adding the following. In contrast to the parallel assembly generated by electrolysis #F, the nanoweb is appropriately described for carbon nanotubes woven from electrolysis #P and #Q, which is presented in the lower row of Table 6 and in Figure 23. Two different routes to nanoweb assembly are summarized. The first is a 0.1% Fe2O3 additive, a Muntz brass cathode, and an Inconel 718 anode with a 3-layer Inconel 600 screen at 0.08 A / cm². 2 This is used to generate 97% pure nanowebs with a Coulomb efficiency of 79%. The second pathway involves adding approximately 0.81 wt% Ni powder, a Monel cathode, and a nichrome C anode at 0.28 A / cm². 2 It is used to generate 92% pure nanowebs with a Coulomb efficiency of 93%.

[0274]

[0214] The densely packed linear CNTs define inter-CNT spacings ranging from 50 to 300 nm, and the CNTs are highly aligned and can also be described as substantially parallel to one another, providing an unusual opportunity for nanofiltration, both in domains of this size and in 1D filtration from 3D morphology. Nanosponges lack this alignment feature, and Figure 23 shows that nanosponges define nanofiltration pores of approximately 100 to 500 nm in size, while nanoweb allotropes provide nanofiltration with pore sizes of approximately 200 nm to 1 μm.

[0275]

[0215] Example 9 Raman spectroscopy and XRD characterization of CNM products from Examples 5-8

[0276]

[0216] Figure 24 shows Raman spectroscopic analysis of CNM products consisting of various labeled CNT assemblies synthesized by electrolytic separation of CO2 in Li2CO3 at 770°C under various systematically varying electrochemical conditions described in Table 7.

[0277]

[0217] [Table 8]

[0278]

[0218] Figure 25 shows the XRD analysis of CNM products consisting of various labeled CNT assemblies synthesized by electrolytic separation of CO2 in Li2CO3 at 770°C under various systematically varying electrochemical conditions described in Table 7.

[0279]

[0219] Figure 24 shows the Raman spectral effect of variations in CNT electrolysis conditions on CNT assembly products from CO2 electrolysis in Li2CO3 at 770°C. The Raman spectrum shows the disorder-induced mode (D band) and high-frequency E 2G Two sharp peaks corresponding to the primary mode (G-band), approximately 1350 and 1580 cm. -1 And an additional peak, a 2D band at 2700cm -1 This is shown. In the spectrum, the graphite fingerprint is located at 1880–2300 cm⁻¹. -1 It is located in and is related to various collective oscillations of sp hybrid CC couplings.

[0280]

[0220] Interpretation of the Raman spectrum provides insight into potential applications of various carbon allotropes. From Figure 24, the intensity ratio between the D band and the G band (I D / I G ) was calculated or observed I G Frequency shift is a useful parameter for evaluating the relative number of defects, and the degree of graphitization is presented in Table 7. In particular, for the nanosponges, nanowebs, and densely packed linear CNT assemblies shown in Figure 23, the nanoweb CNT assembly is shown in Table 7. D / I G The densely packed CNT assembly exhibits a low degree of disorder, with a value of =0.36. D / I G The nanosponge exhibits an intermediate degree of disorder of =0.49, and I D / I G =0.62 shows the highest degree of disorder, and at this point I G Please note that this is accompanied by a frequency shift.

[0281]

[0221] I D / I G In assemblies where the ratio increases: CNT Nanoweb <Densely packed CNT <CNTナノスポンジ That is the case.

[0282]

[0222] It has already been demonstrated that the increasing concentration of iron oxide added to the Li2CO3 electrolyte correlates with the increasing degree of disorder within the graphite structure. These defect levels are each described in the literature as I D / I G It should be noted that the defect rate remains relatively low, as is abundant in reports of multi-walled carbon nanotubes fabricated by other synthesis processes in >1. Lower defect rates are associated with applications requiring high electrical and strength, while higher defect rates are associated with applications that enable high diffusion rates through structures such as those related to increased intercalation and higher anode capacity in Li-ion batteries and higher-charge supercapacitors.

[0283]

[0223] Along with the XRD library of related compound spectra, the XRDs of the CNT assembly products prepared as shown in Figure 23 and Table 6 are presented in Figure 25. Each spectrum shows a strong diffraction peak at 2θ=27°, characteristic of the graphite structure. The nanosponge XRD spectrum is distinctly different from the others, with a main peak at 2θ=43°, and the XRD spectral match indicates Li2Ni8O 10 This shows the presence of nickel as LiCrO2 and chromium as LiCrO2. This nanosponge XRD shows little to no iron carbide. On the other hand, both the nanoweb and densely packed linear CNTs show additional significant peaks at 2θ = 42 and 44°, which indicate the presence of iron carbide, Fe3C, Li2Ni8O 10The presence of XRDs of LiCrO2 and Fe3C, along with the reduced presence of defects already described by Raman spectra for other densely packed CNTs, provides evidence that the simultaneous presence of Ni, Cr, and Fe as nucleating agents can reduce defects in the CNT structure compared to Ni and Cr alone.

[0284]

[0224] Example 10 Scale-up electrolytic operation parameters for producing CNM products with high-purity desired nanocarbon allotropes

[0285]

[0225] This example demonstrates that various nanocarbon allotropes can be electrosynthesized in high purity and high yield using larger electrodes and simpler, modified conditions. Each of the three cases used in this Example 10 generates three different and high-purity allotrope products: (i) CNTs; (ii) carbon nanoonions; or (iii) carbon nanopearls, using similar electrolytic operation parameters, but with different anode shapes and different electrolytic current densities, each of which may affect which metal enters the electrolyte. Each of the three electrosynthesis processes is approximately 39 cm high × 34.5 cm wide (approximately 1,345.5 cm) per surface. 2 The electrolysis was carried out in a molten Li2CO3 electrolyte at 750°C, containing a Muntz brass cathode having a bilateral active surface area (with a surface area of ​​). The cathode was sandwiched between stainless steel 304 anodes. In the first two cases (i) and (ii), the electrolysis was carried out at approximately 0.2 A / cm with a 98% CO2 inlet at 1.9 L / min. 2 In the third case (iii), the current density is constant, and the CO2 inlet is approximately 0.07 A / cm² at 0.8 L / min. 2The experiment was run at a lower, constant current density. In addition to current density, a further difference between the three cases was the shape of the stainless steel anode flanking both sides of the cathode. In the first case (i), the anode was a solid steel plate, which produced a product with high-purity CNT allotropes. After washing to remove excess electrolyte, the TGA of the product and its derivative are shown in Figure 26, while increased magnification SEM images are seen in the lower panel of Figure 27. As seen in the TGA, the product exhibited a low residue rate of 6.7% and high T inflection The TGA purity is 596.9°C and exhibits a highly graphitic (oxidation-resistant) structure, while SEM images reveal the high-purity carbon nanotube morphology of the product. The actual sample purity is lower than the TGA residue rate of 6.7%. 6.7% represents the oxidized (consumed) mass of the (metal) residue. For carbon nanotubes, an even higher carbon nanotube TGA purity can be obtained by increasing the anode-to-cathode distance (i.e., inter-electrode space) from approximately 2.5 cm (1”) to approximately 10 cm (4”), resulting in a TGA purity of approximately 0.2 A / cm². 2 At a constant current density of 0.2 A / cm², a residual rate of approximately 4% is achieved when using a larger electrode with a width of 91.14 cm (36”). 2 At this current density, the current applied to the electrodes was several thousand amperes. The results are reproducible with CO2 directly captured from air and with CO2 from exhaust gases of natural gas power plants. Larger spacing adapted to a longer deposition time of 16 hours, resulting in a thicker deposition of approximately 3.5 inches from each face of the sandwiched cathode. While not bound by any theory, the inventors hypothesized that larger, more adaptable CNT growth requires less additional nucleating metal, which results in the observed increase in TGA purity (and the observed decrease in residual relative mass of TGA).

[0286]

[0226] In the second case (ii), the anode was a novel steel (woven) screen, which generated high-purity carbon nanoonion products, as seen in Figure 28. Furthermore, a novel (new) stainless steel 304 electrolytic case was used. The novel electrolytic case tends to be activated to generate high-purity carbon nanotubes following the initial electrolytic operation. After washing to remove excess electrolyte, the TGA and derivative of the product are shown in Figure 28, while an increased magnification SEM image is shown in Figure 29. As seen in Figure 28, the product has a low residue rate of approximately 4.01% and a high T inflection The temperature is 542.8°C. These results show a graphitic (oxidation-resistant) structure, while SEM images reveal the steel-purity carbon nanoonion allotrope of the product. In this case, repeated subsequent electrolysis causes this anode to generate high-purity carbon nanotube products. This subsequent carbon nanotube formation follows improved anodic emission of transition metals to nucleate carbon nanotube formation compared to the use of a new electrolytic case and anode configuration. Without adhering to any theory, this carbon nanoonion formation follows suppressed emission of transition metals from the mesh electrode and the new steel case to nucleate carbon nanotube formation compared to the use of a new electrolytic case and desired anode configuration.

[0287]

[0227] The melting point of Li2CO3 is 723°C. Another method observed to generate carbon nanoonions is the use of a simpler flat stainless steel anode instead of a screen, which has been found to be even more effective in both the first and subsequent electrolysis, initiating the electrolysis at an even lower temperature where the electrolyte is only partially melted. This also forms highly pure carbon nanoonion products. For example, in repeated experimental operations of the electrolytic reaction, the CNM products with carbon nanoonions demonstrated TGA residues of 5.3% and 7.4%. Without adhering to any theory, this carbon nanoonion formation follows another example of the suppressed formation of nucleation sites on the cathode, which inhibits carbon nanotube formation and prefers highly pure carbon nanoonion formation.

[0288]

[0228] In the third case (iii), the anode was a perforated steel sheet. After washing to remove excess electrolyte, the TGA and derivative of the product are shown in Figure 30, while the SEM image at increased magnification is shown in Figure 31. As seen in Figure 30, the product has a moderate residue of 15.1%, indicating a higher metal content in the product, and a high T inflection =597.7° shows a graphite (oxidation-resistant) structure, while SEM reveals the high-purity carbon nanoonion morphology of the product. While not bound by any theory, this carbon nanopearl product formation may be induced by a higher metal content in the product, which may be related to increased metal release from the perforated sheet anode structure.

Claims

1. A method for producing carbon nanomaterial (CNM) products, (a) A step of heating a carbonate electrolyte medium to obtain a molten carbonate electrolyte medium, (b) A step of positioning the molten carbonate electrolyte medium between the high nickel content anode and cathode of the electrolytic cell, (c) A step of introducing a carbon source into the electrolytic cell, (d) A step of applying current to the cathode and anode of the electrolytic cell, (e) A step of collecting the CNM product from the cathode. A method comprising, wherein the CNM product comprises a desired allotrope selected from the group consisting of conical carbon nanofibers, nanobamboo, and nanotrees, the nanotree comprises a trunk CNT having a plurality of branch CNTs extending away from the trunk carbon nanotube (CNT), and the high nickel content anode is made of pure nickel or an alloy containing more than 50% by weight of nickel.

2. The method according to claim 1, wherein the high nickel-content anode comprises an alloy containing at least 50% by weight of nickel.

3. The method according to claim 1, wherein the high nickel-content anode is a composite anode comprising a first layer of a first alloy containing at least 50% by weight of nickel and a second layer of a second alloy containing at least 50% by weight of nickel, wherein the first alloy and the second alloy are different.

4. The method according to claim 1, wherein the anode and the cathode are made together from pure nickel, and the desired allotrope is a minimum relative amount of 30% by weight of nanobamboo.

5. The method according to claim 1, further comprising the step of adding a nickel-containing additive to the carbonate electrolyte medium or the molten carbonate electrolyte medium in proportion to the amount of the carbonate electrolyte medium or the molten carbonate electrolyte medium, wherein the anode is a composite anode comprising a first layer of a first alloy containing at least 50% by weight of nickel and a second layer of a second alloy containing at least 50% by weight of nickel, wherein the first alloy and the second alloy are different, and the desired allotrope is a minimum relative amount of 85% by weight of nanobamboo.

6. The method according to claim 1, wherein the molten carbonate electrolyte medium is newly melted and the CNM product contains a minimum relative amount of 6% by weight of conical carbon nanofibers.

7. The method according to claim 1, further comprising the step of introducing a lithium-containing additive into the carbonate electrolyte medium or the molten carbonate electrolyte medium, wherein the anode is a composite anode comprising a first layer of a first alloy containing at least 50 wt% nickel and a second layer of a second alloy containing at least 50 wt% nickel, wherein the first alloy and the second alloy are different, and the desired allotrope is a minimum relative amount of 95 wt% nanotree.

8. The method according to claim 7, wherein the lithium-containing additive is lithium oxide, and is added in an amount between about 0.05% by weight and 0.5% by weight relative to the amount of the carbonate electrolyte medium or the molten carbonate electrolyte medium.

9. The method according to claim 1, further comprising the step of introducing a magnetic additive component into the electrolytic cell, wherein the magnetic additive component comprises a magnetic material additive component, a magnetic carbide growth component, or any combination thereof, and the desired allotrope is magnetic and moves when in a magnetic field.

10. The method according to claim 1, further comprising the step of introducing a doping additive component into the electrolytic cell, wherein the desired allotrope is doped, and atoms of the doping additive component are directly incorporated throughout the doped desired allotrope to impart to the doped desired allotrope a desired physical and / or chemical property different from that of an undoped desired allotrope.

Images