135 results about "Torrefaction" patented technology

A method for torrefaction of wood which includes providing a first endless conveyor belt; heating the first endless belt; and positioning a planar wood product on the first belt to heat the wood product by conduction to achieve torrefaction. Other forms provide a second endless belt that disposed in sandwich relation to wood to be torrefied. Some embodiments of the method provide a metal chamber having opposed planar sides dimensioned and configured for receiving a wood sheet with the respective opposed sides of the wood sheet in intimate thermal contact with respective opposed sides of the metal chamber. Other embodiments include the apparatus for torrefaction of an associated wood sheet.

The present invention features methods and apparatus for the pyrolysis or torrefaction of a carbon-containing feedstock before it is converted to syngas. In some embodiments, biomass is first pretreated by torrefaction and/or pyrolysis, followed by devolatilization and/or steam reforming to produce syngas. Various mixtures of such pretreated biomass, combined with fresh biomass, can be employed to produce syngas. The syngas can be converted to alcohols, such as ethanol, or to other products.

Apparatus for biomass torrefaction which includes a serpentine elongated housing, the housing having three generally U-shaped axial portions having first and second axial extremities and an intermediate section, the first and second axial extremities are disposed in normal use at a higher elevation than the first and second axial extremities, the intermediate section being configured for holding a liquid. Other forms of the invention include the method for biomass torrefaction which includes providing a quantity of biomass, providing a liquid heat transfer fluid, providing at least a first housing for holding the heat transfer liquid, elevating the temperature of the liquid heat transfer liquid, heat treating the biomass by passing it through the heat transfer liquid in the first housing at a temperature and duration sufficient to accomplish torrefaction of the wood. In some forms of the method, the process further includes the step of pelletizing the biomass prior to performing the treating step.

There is described a processor for use in the microwave torrefaction of biomass material which comprises, a micronised biomass char material and a method of producing a biomass char material, and a method of producing L-glucosan.

The present invention provides an autothermal torrefaction device, which can be either stationary of mobile. Embodiments of the present invention include a torrefaction chamber having a chamber inlet for receiving biomass and at least one chamber outlet. The torrefaction chamber can be substantially surrounded by an exterior housing defining an outer jacket and having a jacket inlet and a jacket outlet. The outer jacket and torrefaction chamber define a space therebetween such that a burner unit including an inlet operatively connected to the chamber outlet and an outlet operatively connected to the jacket inlet allows vapors produced or released from within the torrefaction chamber to travel into the burner unit for combustion of at least a portion of the vapors and subsequently travel through the space between the jacket and the torrefaction chamber to provide heat necessary for autothermal torrefaction of biomass.

The present invention features methods and apparatus for the pyrolysis or torrefaction of a carbon-containing feedstock before it is converted to syngas. In some embodiments, biomass is first pretreated by torrefaction and/or pyrolysis, followed by devolatilization and/or steam reforming to produce syngas. Various mixtures of such pretreated biomass, combined with fresh biomass, can be employed to produce syngas. The syngas can be converted to alcohols, such as ethanol, or to other products.

A process for increasing the energy density of a biomass, which includes establishing a temperature and pressure within a reaction chamber that includes water and is at or above a desired reaction condition wherein the desired reaction condition is sufficient to increase the energy density of a reacted biomass; introducing a biomass into the reaction chamber such that the desired reaction condition is maintained or equilibrates thereto; and subjecting the biomass to the desired reaction condition for an amount of time effective to increase the energy density of the reacted biomass relative to the biomass prior to reaction.

A method and related apparatus for torrefaction of associated biomass which includes providing an enclosed chamber having a body and a door having an open position allowing passage into and out of the enclosed chamber and a closed position in which the door is disposed in sealing engagement with the body, providing the enclosed chamber with walls capable of sustaining both a negative pressure and a positive pressure within the enclosed chamber; moving the door to an open position; depositing a liquid heat transfer fluid within the enclosed chamber at a temperature sufficient to achieve torrefication of the biomass and a first quantity of biomass material in the enclosed chamber that is substantially totally immersed in the liquid heat transfer fluid whereby heat transfer occurs between the liquid heat transfer fluid and the biomass immersed therein; moving the door to a closed position in sealing engagement with the body; and allowing the pressure within the enclosed chamber to rise to a pressure above the vapor pressure of the heat transfer fluid as a result of the expansion of liquids and gases entrained within the biomass.

A method of treating a biomass material to produce a fuel comprising the steps of preheating the biomass material to a temperature ranging from about 80° C. to about 100° C. and drying the biomass material until the biomass material has a maximum water content of no more than 3%. Microwave radiation is applied to the pre-dried biomass material in a range of 3.0 to 8.0 GHz to heat the biomass material to a temperature ranging from about 230° C. to about 280° C. resulting in torrefaction of the biomass material. The biomass material is then cooled.

This invention provides processes to convert biomass into energy-dense biomass for combustion, alone or in combination with another solid fuel. In some variations, biomass is extracted to produce an extract liquor containing hemicellulosic oligomers and cellulose-rich solids; hemicellulosic oligomers are removed; and the cellulose-rich solids are torrefied to produce energy-dense biomass. In some embodiments, hydrotorrefaction is employed to produce hydrophobic, energy-dense biomass in an energy-efficient process that avoids intermediate drying between extraction/hydrolysis and torrefaction. The energy-dense biomass may be pelletized or directly combusted or gasified. The hemicellulosic oligomers may be hydrolyzed to fermentable sugars and then fermented to ethanol or other products, or further reacted to produce furfural or other products.

The invention provides a preparation method for roasting-free hydrotreating catalyst, the catalyst takes Al 2 O 3, SiO 2, TiO 2, and a composite oxide of two of the Al 2 O _{3, the SiO 2 as carriers, and takes group 6B metals and group 8 metals as active metal components, a right amount of organic chelating agent is added into metal impregnation liquid, to adjust the pH value of the impregnation liquid, the active metal components are supported to the upper part of the carrier by adopting a co-impregnation method or a multi-step impregnation method, the carriers supporting the metal components are dried for 4 to 10 hours at 120 DEG C, without roasting, thereby the highly active hydrofining catalyst can be directly obtained. The metal components of the catalyst prepared by the invention have better dispersibility and sulfidization, thus the catalyst has good activity of hydrogen desulfurization and hydrodenitrification to petroleum fraction.}

Improved, fuel-efficient systems are provided for the processing of biomass, such as wood or crop residues, food waste or animal waste in order to selectively obtain torrefied and/or carbonized final products. In general, the processes involve thermally drying incoming biomass using a dryer employing the hot gas output of a fuel-operated burner. Next, the dried product is torrefied in an indirect torrefaction reactor so as to evolve light volatile organic compounds which are used as a gaseous fuel source for the burner. The torrefied product can be recovered, or some or all of the torrefied product may be directed to a carbonization reactor coupled with a reactor burner. Carbonization serves to remove most of the remaining VOCs which are used as a gaseous fuel input to the dryer. In certain instances, portions of the dried biomass are directed to the burners, as an additional source of fuel.

Systems and methods for integrating thermochemical processing of biomass and anaerobic digestion are provided. Light oxygenated organic compounds are produced as byproducts of thermochemical biomass processing e.g. by torrefaction and/or pyrolysis, and are converted to methane by anaerobic digestion. Thermochemical processing units may or may not be co-located with the anaerobic digestion units, with co-location providing benefits for e.g. rural agricultural enterprises.

A process for treating lignocellulosic material, such as wood for example, the process including the steps of: a) providing lignocellulosic material; b) evaluating parameters of the lignocellulosic material; c) preparing the lignocellulosic material; d) heating the lignocellulosic material in a treatment chamber following a given profile based on parameters of the lignocellulosic material; e) stabilizing the lignocellulosic material; and f) cooling down the lignocellulosic material. The process enables to improve the quality of the wood being treated, while ensuring a greater repeatability and uniformity of coloring results, and overcoming drawbacks associated with conventional torrefaction methods.

Improved, fuel-efficient systems are provided for the processing of biomass, such as wood or crop residues, food waste or animal waste in order to selectively obtain thermally processed final products, such as a combination of torrefied and carbonized final products. The processes involve thermally drying incoming biomass using a dryer employing the hot gas output of a fuel-operated burner. Next, the dried product is torrefied in an indirect torrefaction reactor so as to evolve light volatile organic compounds which are used as a gaseous fuel source for the burner. Some or all of the torrefied product can be recovered, or some or all of the torrefied product is then directed to a separate carbonization reactor coupled with a reactor burner. Carbonization serves to remove most of the remaining VOCs which are used as a gaseous fuel input to the dryer.

The invention provides methods and systems for the production of at least one product from the microbial fermentation of a gaseous susbtrate, wherein the gaseous substrate is derived from a biomass liquefaction process. The invention provides a method for improving efficiency of the fermentation by passing biomass accumulated in the fermentation process to the biomass liquefaction process for conversion to a gaseous substrate. In a particular aspect of the invention, the biomass liquefaction process is selected from pyrolysis or torrefaction.

This invention discloses a process for producing V2O5 from vanadium-containing stone coal or vanadium slag. The process comprises: adding M-1 type additive to vanadium-containing stone coal or vanadium slag, torrefying, leaching with diluted H2SO4 to obtain vanadium salt solution, extracting vanadium aggregate from the vanadium salt solution by using N-1 type aggregation agent, removing impurities, adding P-1 type separation agent for separation, precipitating vanadium, oxidizing to obtain V2O5, recovering Al and Fe from the system, and producing Al2 (SO4)3 and iron red. The process has such advantages as no Cl2 or HCl generation, high torrefaction yield (70-90%), no wastewater, little environmental pollution, high product yield, low production cost, high recovery rate of Al and Fe, high product purity (higher than 99%), simple process and stable oepration.

A method for torrefaction of biomass using a torrefaction reactor vessel having stacked trays including: feeding the biomass to an upper inlet of the vessel; cascading the biomass down through the trays by passing the biomass through an opening in each of the trays to deposit the biomass on a lower tray; heating the biomass material with an oxygen deprived gas; extracting moisture from below each of the upper trays; as the biomass undergoes torrefaction in the lower trays retaining the gas with the biomass until the biomass falls from the stacked trays to a pile of biomass in the reactor vessel; exhausting gases containing organic compounds through a gas outlet at an elevation between the stacked trays and the pile of biomass, and discharging torrefied biomass from the torrefaction reactor vessel.

This invention discloses a heat integrated and energy saving process for producing high quality pyrolysis oil from biomass by utilizing a torrefaction pretreatment step for biomass pyrolysis processing wherein the pretreatment step improves the quality of the pyrolysis oil by reducing acidity. This invention further utilizes the gaseous product of the torrefaction step through a combustion process for heat production and recovery.

This invention relates to a method for preparing rare earth Eu-activated calcium sulfide or alkaline earth metal sulfide red-fluorescent material. The method comprises: (1) weighing calcium carbonate or alkaline earth metal carbonate, europium oxide and sulfur according to the chemical formula of Ca1-xSn : Eux or MyCa1-x-ySn : Eux (x = 0.001-0.04 mol, n = 1-3, M = one or more of Mg, Sr, Ba and Zn, and y = 0-1); (2) grinding and mixing the raw materials completely, and placing in a torrefaction container; (3) torrefying at 900-1200 deg.C for 30-120 min to obtain red-fluorescent powder. The method has such advantages as simple operation, low cost and no harm to operators. The emitting peak of the fluorescent material can change within the range of 50 nm, thus is suitable for different circumstances.