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60 results about "Material Pore Size" patented technology

A quantitative or qualitative measurement of the physical dimensions of the pores in a material.

SAPO-34/ZSM-5 composite molecular sieve and synthesis method of composite molecular sieve

InactiveCN104556143AAdjustable acid distributionWide distribution of acidityMolecular-sieve and base-exchange phosphatesMolecular sieveMaterial Pore Size
The invention relates to an SAPO-34/ZSM-5 composite molecular sieve and a synthesis method of the composite molecular sieve, solving the problems of single pore diameter, low acidity and low reaction activity of the porous materials which are synthesized by the prior art. The synthesis method of the composite molecular sieve comprises the following steps: firstly mixing a silicon source, an aluminum source, a phosphorus source and an organic template agent according to a certain ratio, then adding a certain quantity of ZSM-5 molecular sieves, uniformly mixing and carrying out hydrothermal crystallization, and synthesizing the SAPO-34/ZSM-5 composite molecular sieve by controlling nucleation and crystal growth conditions, wherein the composite molecular size is adjustable in ratio of two phases; an XRD diffraction spectrum of the composite molecular size has a maximum d interval at the positions of 7.92+/-0.1, 8.79+/-0.1, 9.52+/-0.1, 12.85+/-0.1, 16.00+/-0.1, 20.56+/-0.1, 23.01+/-0.05, 23.24+/-0.05, 23.86+/-0.05, 25.83+/-0.1, 30.55+/-0.1 and 31.32+/-0.1. The composite molecular sieve can be applied to industrial production for preparing aromatic hydrocarbon by reacting methyl alcohol/dimethyl ether.
Owner:CHINA PETROLEUM & CHEM CORP +1

Mordenite/beta zeolite/MCM-22 triphase coexisting molecular sieve and method for synthesizing same

The invention relates to a mordenite/beta zeolite/MCM-22 triphase coexisting molecular sieve and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the porous coexisting material by adding a seed crystal containing an MCM-22 precursor and well controlling the nucleating and growing process of a molecular sieve during a synthesis process of triphase coexisting molecular sieve. The coexistence phase ratio of the triphase coexisting molecular sieve is adjustable, and a mole relation of the components of the synthesized triphase coexisting molecular sieve is nSiO2 :Al2O3, wherein n is between 4 and 400; the triphase coexisting molecular sieve has more than three phases; the XRD diffraction pattern of the triphase coexisting molecular sieve comprises a technical proposal that a maximum value of a distance d is at positions between 13.58-0.1 and 13.58+0.1 A, 12.35-0.1 and 12.35+0.1 A, 11.32-0.1 and 11.32+0.1 A, 11.08-0.1 and 11.08+0.1 A, 8.83-0.05 and 8.83+0.05 A, 8.96-0.05 and 8.96+0.05 A, 6.71-0.1 and 6.71+0.1 A, 6.17-0.1 and 6.17+0.1 A, 4.51-0.1 and 4.51+0.1 A, 4.15-0.05 and 4.15+0.05 A, 3.90-0.05 and 3.90+0.05 A, 3.42-0.05 and 3.42+0.05 A, 3.29-0.04 and 3.29+0.04 A, 3.19-0.04 and 3.19+0.04 A, and 3.02-0.1 and 3.02+0.1 A; therefore, the problems are solved well. The triphase coexisting molecular sieve can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha.
Owner:CHINA PETROLEUM & CHEM CORP +1

Coexisting molecular sieve and synthesis method thereof

The invention relates to a coexisting molecular sieve and a synthesis method thereof, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the coexisting molecular sieve by adding a seed crystal containing a laminated structure precursor and well controlling the nucleating and growing process of a molecular sieve during a synthesis process of mordenite. The coexistence phase ratio of the coexisting molecular sieve is adjustable, and a mole relation of the components of the synthesized coexisting molecular sieve is nSiO2 :Al2O3, wherein n is between 4 and 400; the coexisting molecular sieve has more than two phases, the XRD diffraction pattern of the coexisting molecular sieve comprises a technical proposal that a maximum value of a distance d is at positions between 13.52-0.1 and 13.52+0.1 A, 12.35-0.1 and 12.35+0.1 A, 11.08-0.1 and 11.08+0.1 A, 8.96-0.05 and 8.96+0.05 A, 8.83-0.05 and 8.83+0.05 A, 6.71-0.1 and 6.71+0.1 A, 6.71-0.1and6.71+0.1 A,4.51-0.1 and 4.51+0.1 A, and 3.29-0.02 and 3.29+0.02 A; therefore, the problems are solved well. The coexisting molecular sieve can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha.
Owner:CHINA PETROLEUM & CHEM CORP +1

Beta zeolite /Magadiite/mordenite coexisting material and method for synthesizing same

The invention relates to a beta zeolite /Magadiite/mordenite coexisting material and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single and nonadjustable in pore-size distribution. The method prepares the beta zeolite /Magadiite/mordenite coexisting material. A mole relation of the components of the synthesized beta zeolite /Magadiite/mordenite coexisting material is nSiO2 :Al2O3, wherein n is between 10 and 1,000; the beta zeolite /Magadiite/mordenite coexisting material has two coexisting phases; the XRD diffraction pattern of the beta zeolite /Magadiite/mordenite coexisting material comprises a technical proposal that a maximum value of a distance d is at positions between 15.73-0.1 and 15.73+0.1 A, 13.52-0.1 and 13.52+0.1 A, 11.32-0.1 and 11.32+0.1 A, 11.14-0.05 and 11.14+0.05 A, 9.96-0.1 and 9.96+0.1 A, 8.96-0.1 and 8.96+0.1 A, 7.74-0.1 and 7.74+0.1 A, 6.71-0.1 and 6.71+0.1 A, 5.14-0.1 and 5.14+0.1 A, 4.51-0.1 and 4.51+0.1 A, 4.14-0.05 and 4.14+0.05 A, 3.96-0.05 and 3.96+0.05 A, 3.86-0.04 and 3.86+0.04 A, 3.65-0.05 and 3.65+0.05 A, 3.47-0.1 and 3.47+0.1 A, 3.30-0.05 and 3.30+0.05 A, 3.14-0.1 and 3.14+0.1, and 3.02-0.05 and 3.02+0.05 A; therefore, the problems are solved well. The beta zeolite /Magadiite/mordenite coexisting material can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha and ethylene and propylene through the dehydration of methanol.
Owner:CHINA PETROLEUM & CHEM CORP +1

ZSM-5/Magadiite/mordenite coexisting material and method for synthesizing same

The invention relates to a ZSM-5/Magadiite/mordenite coexisting material and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single and nonadjustable in pore-size distribution. The method prepares the ZSM-5/Magadiite/ mordenite coexisting material. A mole relation of the components of the synthesized ZSM-5/Magadiite/ mordenite coexisting material is nSiO2 :Al2O3, wherein n is between 10 and 2,000; the ZSM-5/Magadiite/ mordenite coexisting material has three coexisting phases; the XRD diffraction pattern of the ZSM-5/Magadiite/mordenite coexisting material comprises a technical proposal that a maximum value of a distance d is at positions between 15.73-0.1 and 15.73+0.1 A, 13.52-0.1 and 13.52+0.1 A, 11.22-0.2 and 11.22+0.2 A, 9.96-0.1 and 9.96+0.1 A, 8.96-0.1 and 8.96+0.1 A, 7.73-0.1 and 7.73+0.1 A, 6.71-0.1 and 6.71+0.1 A, 5.99-0.1 and 5.99+0.1 A, 5.14-0.1 and 5.14+0.1 A, 4.51-0.1 and 4.51+0.1 A, 3.98-0.05 and 3.98+0.05 A, 3.86-0.05 and 3.86+0.05 A, 3.66-0.1 and 3.66+0.1 A, 3.47-0.05 and 3.47+0.05 A, 3.30-0.05 and 3.30+0.05 A, 3.14-0.1 and 3.14+0.1, and 2.99-0.05 and 2.99+0.05 A; therefore, the problems are solved well. The ZSM-5/Magadiite/mordenite coexisting material can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha and ethylene and propylene through the dehydration of methanol.
Owner:CHINA PETROLEUM & CHEM CORP +1

Has multi-level porous ssz-13 molecular sieve catalyst and its synthesis method and application

The invention discloses a hierarchical porous SSZ-13 molecular sieve catalyst, a method for synthesizing the same and application of the hierarchical porous SSZ-13 molecular sieve catalyst. The method includes that long-chain silane is selected to be used as an auxiliary for crystallization synthesis reaction, molar ratios of alkali sources, silicon sources, aluminum sources, template agents, the long-chain silane and water are regulated, and segmented dynamic / static crystallization modes are adopted. Synthesizing procedures include steps of gel forming and aging, crystallizing, washing, template agent removing and activating, ion exchanging and activating and the like. High-crystallinity hierarchical porous SSZ-13 molecular sieves with micropore-mesopore ordered distribution can be obtained by the aid of the method. The obtained molecular sieves have distribution of two types of pore sizes in a 2-5 nm range and a 5-15 nm range, the volumes of micropores are larger than 0.20 cm<3> / g, the volumes of mesopores are larger than 0.35 cm<3> / g, the specific surface areas are larger than 400 m<2> / g, and the yield of crystallization products can reach 85% at least. The hierarchical porous SSZ-13 molecular sieve catalyst, the method and the application have the advantages that the SSZ-13 molecular sieves not only have merits of micropore zeolite, but also have merits of mesopore materials which have large pore sizes and are favorable for macromolecule diffusion, the hierarchical porous SSZ-13 molecular sieve catalyst has a broad application prospect in the fields of petrochemical engineering, MTO (methanol to olefin) reaction, tail gas purification and fine chemical engineering, and the like.
Owner:CHINA CATALYST HLDG CO LTD

ZSM-5/beta zeolite/MCM-22 triphase coexisting molecular sieve and method for synthesizing same

The invention relates to a ZSM-5 / beta zeolite / MCM-22 triphase coexisting molecular sieve and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the triphase coexisting molecular sieve by adding a seed crystal containing an MCM-22 precursor during a synthesis process of diphase coexisting molecular sieve. A mole relation of the components of the synthesized triphase coexisting molecular sieve is nSiO2 :Al2O3, wherein n is between 10 and 1,000; the triphase coexisting molecular sieve has more than three phases; the XRD diffraction pattern of the triphase coexisting molecular sieve comprises a technical proposal that a maximum value of a distance d is at positions between 13.35-0.1 and 13.35+0.1 A, 11.32-0.04 and 11.32+0.04 A, 11.22-0.4 and 11.22+0.4 A, 11.08-0.05 and 11.08+0.05 A, 9.97-0.1 and 9.97+0.1 A, 8.82-0.1 and 8.82+0.1 A, 7.74-0.1 and 7.74+0.1 A, 6.17-0.1 and 6.17+0.1 A, 5.14-0.1 and 5.14+0.1 A, 4.15-0.1 and 4.15+0.1 A, 3.90-0.05 and 3.90+0.05 A, 3.71-0.1 and 3.71+0.1 A, 3.45-0.05 and 3.45+0.05 A, 3.29-0.04 and 3.29+0.04 A, 3.19-0.04 and 3.19+0.04 A, and 2.98-0.1 and 2.98+0.1 A; therefore, the problems are solved well. The triphase coexisting molecular sieve can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha.
Owner:CHINA PETROLEUM & CHEM CORP +1

Controllable-through-hole montmorillonite porous material adsorbent and preparation method thereof

The invention discloses a controllable-through-hole montmorillonite porous material adsorbent and a preparation method thereof. First, a pore-forming agent is well mixed into an MMT (montmorillonite) nano material, such that a mixture is obtained; polyvinyl alcohol PVA colloid is added into the mixture for granulation; drying is carried out; the obtained granules are ground and sieved, such that particles are obtained; the particles are aged; the aged powder is subjected to dry-press molding, such that an MMT blank is obtained; calcination is carried out, wherein heating rate and calcination temperature are controlled; after a temperature-maintaining process, the material is cooled with the furnace, such that the montmorillonite porous material adsorbent is obtained. The adopted pore-forming agent is a mixture of one or more selected from polymethylmethacrylate, starch, waste papermaking fiber, waste textile fiber and waste leather fiber. The pore-forming agent is decomposed into gas penetrating the blank under high temperature, such that through holes are formed, and a water permeation function is realized. With the control over pore-forming agent diameter, pore-forming agent mass percentage and calcination heating rate, material pore size and porosity are controllable. The preparation process is simple; cost is low; and no secondary pollution is caused.
Owner:SHAANXI UNIV OF SCI & TECH

ZSM-5/ZSM-23/Y zeolite triphase coexisting molecular sieve and method for synthesizing same

The invention relates to a ZSM-5/ZSM-23/Y zeolite triphase coexisting molecular sieve and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the ZSM-5/ZSM-23/Y zeolite triphase coexisting molecular sieve by adding a seed crystal containing a Y zeolite precursor during a synthesis process of triphase coexisting molecular sieve, and well controlling the nucleating and growing process of a molecular sieve during a synthesis process of triphase coexisting molecular sieve. The coexistence phase ratio of the ZSM-5/ZSM-23/Y zeolite triphase coexisting molecular sieve is adjustable, and a mole relation of the components of the synthesized triphase coexisting molecular sieve is nSiO2 :Al2O3, wherein n is between 10 and 1,000; the triphase coexisting molecular sieve has more than three phases; the XRD diffraction pattern of the triphase coexisting molecular sieve comprises a technical proposal that a maximum value of a distance d is at positions between 14.52-0.1 and 14.52+0.1 A, 11.22-0.1 and 11.22+0.1 A, 10.1-0.05 and 10.1+0.1 A, 9.97-0.05 and 9.97+0.05 A, 7.87-0.2 and 7.87+0.2 A, 5.98-0.1 and 5.98+0.1 A, 5.71-0.1 and 5.71+0.1 A, 5.59-0.1 and 5.59+0.1 A, 4.53-0.1 and 4.53+0.1 A, 3.90-0.1 and 3.90+0.1 A, 3.71-0.05 and 3.71+0.05 A, 3.43-0.05 and 3.43 +0.05 A, 2.99-0.05 and 2.99+0.05A, 2.86-0.05 and 2.86+0.05 A, and 2.53-0.1 and 2.53+0.1 A; therefore, the problems are solved well. The triphase coexisting molecular sieve can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha.
Owner:CHINA PETROLEUM & CHEM CORP +1

ZSM-5/beta zeolite/MCM-49 triphase coexisting molecular sieve and method for synthesizing same

The invention relates to a ZSM-5/beta zeolite/MCM-49 triphase coexisting molecular sieve and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the ZSM-5/beta zeolite/MCM-49 triphase coexisting molecular sieve by adding a seed crystal containing an MCM-49 precursor during a synthesis process of diphase coexisting molecular sieve. A mole relation of the components of the synthesized triphase coexisting molecular sieve is nSiO2 :Al2O3, wherein n is between 10 and 1,000; the triphase coexisting molecular sieve has more than three phases; the XRD diffraction pattern of the triphase coexisting molecular sieve comprises a technical proposal that a maximum value of a distance d is at positions between 12.26-0.1 and 12.26+0.1 A, 11.32-0.04 and 11.32+0.04 A, 11.22-0.04 and 11.22+0.04 A, 11.08-0.05 and 11.08+0.05 A, 9.97-0.1 and 9.97+0.1 A, 8.82-0.1 and 8.82+0.1 A, 7.74-0.1 and 7.74+0.1 A,6.14-0.1 and 6.14+0.1 A, 5.14-0.1 and 5.14+0.1 A, 4.15-0.1 and 4.15+0.1 A, 3.90-0.05 and 3.90+0.05 A,3.71-0.1 and 3.71+0.1 A,3.45-0.05 and 3.45+0.05,3.29-0.04 and 3.29+0.04 A ,3.20-0.04 and 3.29+0.04 A ,3.08-0.04 and 3.08+0.04 A, and 2.98-0.05 and 2.98+0.05 A; therefore, the problems are solved well. The triphase coexisting molecular sieve can be used in the industrial production of ethylene and propylene through the catalytic pyrolysis of naphtha.
Owner:SHANGHAI RES INST OF PETROCHEMICAL TECH SINOPEC

Method for improving measurement accuracy of pore structure parameters

The invention provides a method for improving the measurement accuracy of pore structure parameters. The method is suitable for the field of measurement of pore diameter and specific surface area parameters of nano porous materials. The method specifically comprises the following steps: testing an adsorption-desorption curve of a to-be-tested material sample by using a specific surface area and pore size analyzer; obtaining pore size range data of the to-be-tested material according to the test data; selecting a specific numerical value in the pore diameter range of the to-be-detected materialby utilizing a giant regular ensemble (GCMC) molecular simulation system, building a simulation calculation structure model, and continuously increasing or decreasing the chemical potential of a mainfluid to obtain an adsorption hysteresis loop consisting of a stable state and a metastable state of the fluid in a nanopore; and selecting a particle system with an intermediate state at a given adsorption pressure position in the adsorption hysteresis loop. Analog computation involved in the method can be embedded into analysis software of a test instrument, the operation is simple, and the accuracy of detection results of the pore diameter and the specific surface area of the nano-porous material can be effectively improved.
Owner:XI'AN PETROLEUM UNIVERSITY +1

Three-dimensional porous graphene aerogel wave-absorbing material and preparation method thereof

The invention discloses a three-dimensional porous graphene aerogel wave-absorbing material and a preparation method thereof. The method comprises the following steps: respectively measuring a graphene oxide aqueous solution, a reducing agent and an anti-freezing agent, and obtaining a mixed solution after magnetic stirring and ultrasonic dispersion; transferring the mixed solution into a glass bottle, sealing and placing the glass bottle in a drying oven for pre-reduction to obtain pre-reduced graphene hydrogel; freezing the pre-reduced graphene hydrogel, and then unfreezing the pre-reduced graphene hydrogel at room temperature to obtain freeze-thawed pre-reduced graphene hydrogel; sealing the frozen and thawed pre-reduced graphene hydrogel and placing in a drying oven for continuous reduction, and obtaining graphene hydrogel; putting the graphene hydrogel into an ethanol/water mixed solution to be aged, performing freeze drying, and obtaining the three-dimensional graphene oxide aerogel. The pore size and the volume of the three-dimensional graphene wave-absorbing material can be freely controlled, and free design of absorption of different electromagnetic waves can be realized by controlling the pore size and the volume of the wave-absorbing material.
Owner:NANJING UNIV OF INFORMATION SCI & TECH

Magadiite-beta zeolite coexisting material and method for synthesizing same

The invention relates to a magadiite-beta zeolite coexisting material and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single and nonadjustable in pore-size distribution. The method prepares a magadiite-beta zeolite coexisting material by well controlling the nucleating and growing process of a molecular sieve during a synthesis process of beta zeolite molecular sieve material. The coexistence phase ratio of the magadiite-beta zeolite coexisting material is adjustable, and a mole relation of the components of the synthesized magadiite-beta zeolite coexisting material is nSiO2 :Al2O3, wherein n is between 20 and 2,000; the magadiite-beta zeolite coexisting material has two coexistence phases, the XRD diffraction pattern of the magadiite-beta zeolite coexisting material comprises a technical proposal that a maximum value of a distance d is at positions between 15.73-0.1 and 15.73+0.1 A, 11.14-0.1 and 11.14+0.1 A, 9.97-0.1 and 9.97+0.1 A, 7.74-0.1 and 7.74+0.1 A, 5.14-0.1 and 5.14+0.1 A, 3.86-0.05 and 3.86+0.05 A, 3.66-0.05 and 3.66+0.05 A, 3.45-0.05 and 3.45+0.05 A, 3.30-0.05 and 3.30+0.05 A, and 3.14-0.1 and 3.14+0.1 A; therefore, the problems are solved well. The magadiite-beta zeolite coexisting material can be used in the industrial production of ethylene and propylene through the dehydration of methanol.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for reducing three-dimensional structure of non-woven material through fiber central axis

The invention relates to a method for reducing a three-dimensional structure of a non-woven material through a fiber central axis. The method comprises the following steps: extracting a central axis of a fiber through a same-field multi-layer multi-focal-plane non-woven material microscopic image so as to restore the three-dimensional form and position of the central axis in the non-woven material; collecting and fusing multilayer microscopic images; performing the circular segmentation of the fibers, selection of circle center points, calculation of the depth of the circle center points, extraction of the central axes of the fibers and reduction of the closed three-dimensional surfaces of the fibers; extracting the depth of a source point on the central axis of the fiber and the section radius of the fiber at the source point, and then restoring the three-dimensional coordinates of the fiber axis and the closed surface in a spatial interpolation mode. Compared with other reconstruction methods, the method provided by the invention truly restores the relationship between fiber longitudinal directions, and provides a high-quality three-dimensional model for subsequent research on key parameters such as pore size and distribution, pore inner surface area, pore volume, air fluid resistance and pressure difference of the non-woven material.
Owner:DONGHUA UNIV

Device for testing the aperture of porous material and testing method thereof

The invention provides a device for testing the aperture of a porous material. The device comprises: a lower chamber, wherein an air inlet and a first pressure detection port are formed in the side edge of the lower chamber, a first sample detection port is formed in the top of the lower chamber, an air inlet which is externally connected with an air inlet control device, a first pressure detection port which is externally connected with a first pressure sensor, and the opening of the first sample detection port is upward; and an upper chamber which is mounted and fixed above the lower chamber, wherein a liquid adding opening and a second pressure detection opening are formed in the side surface of the upper chamber. The invention further provides a corresponding testing method which has the beneficial effects that the dry-method detection and the wet-method detection of the porous material are completed on the same equipment in sequence, and only one piece of equipment is needed, so that the cost is saved; in addition, the wet method is carried out after the dry method is finished, and the porous material does not need to move, so that the dry method and the wet method are used for detecting at the same position of the porous material, deviation caused by movement is avoided, and the correctness of a final result is ensured.
Owner:LONGYAN QIANGLONG METAL FIBER
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