WO2023086012A1 - Method and system for generating syngas - Google Patents

Method and system for generating syngas Download PDF

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Publication number
WO2023086012A1
WO2023086012A1 PCT/SG2022/050728 SG2022050728W WO2023086012A1 WO 2023086012 A1 WO2023086012 A1 WO 2023086012A1 SG 2022050728 W SG2022050728 W SG 2022050728W WO 2023086012 A1 WO2023086012 A1 WO 2023086012A1
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WO
WIPO (PCT)
Prior art keywords
syngas
woodchips
pathway
vessel
biochar
Prior art date
Application number
PCT/SG2022/050728
Other languages
French (fr)
Inventor
Shao Lin LIM
Original Assignee
Green Energy Investment Holding Pte Ltd
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Publication date
Application filed by Green Energy Investment Holding Pte Ltd filed Critical Green Energy Investment Holding Pte Ltd
Priority to US18/574,171 priority Critical patent/US20240318091A1/en
Publication of WO2023086012A1 publication Critical patent/WO2023086012A1/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/007—Screw type gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/08—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/06—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated according to the moving bed type
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/08—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
    • C10B49/10—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form according to the "fluidised bed" technique
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B51/00—Destructive distillation of solid carbonaceous materials by combined direct and indirect heating
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/16—Features of high-temperature carbonising processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/18—Modifying the properties of the distillation gases in the oven
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/158—Screws
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0916—Biomass
    • C10J2300/092—Wood, cellulose
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/12—Heating the gasifier
    • C10J2300/1223—Heating the gasifier by burners

Definitions

  • This invention relates generally to a method and system for generating syngas.
  • Low density agricultural biomass for example bark and wood chips
  • Low density agricultural biomass for example bark and wood chips
  • a common problem that makes the process uneconomical is the prohibitive cost of transporting these bulky materials to a central processing site.
  • Application of fluid bed fast pyrolysis technology to Such materials therefore relies upon a significant reduction or elimination of these material transportation costs. It would be desirable to provide “self-contained fast pyrolysis process equipment that is compact, mobile and has the ability to be set up and operated close to the source of the feed materials.
  • the process employed in using the equipment should be forgiving in terms of particle size and biomass moisture content.
  • the process should also take advantage of rapid heat transfer and short solids residence time to reduce vessel size and increase throughput.
  • Non-limiting examples of biomass include: wood in any suitable such as sawdust, shavings, pellets, woodchips and other wood residue, municipal waste, sewage, coal, bitumen, fossil fuels, food waste and plant matter.
  • Combustible gases may be liberated from biomass by heating the biomass in an oxygen- reduced atmosphere. The heating may be done by partially oxidizing the biomass or by way of a separate heat source. The heating causes the biomass to release combustible gases which are also known as “syngas”, “synthesis gas”, “producer gas” and “product gas”.
  • Syngas produced from biomass may be used for various applications.
  • the gases may be burned to generate heat, processed to make synthetic fuels (the synthetic fuels may comprise gaseous, liquid or solid fuels), used to run an engine, used as a fuel for a fuel cell or used as a fuel to run a turbine.
  • Syngas liberated from biomass may include fractions, such as tars and heavier hydrocarbons, that can condense in ducts and other equipment. This can cause significant operational and maintenance problems. There is a need for practical and energy-efficient methods and apparatus for producing clean syngas from biomass, specifically from woodchips
  • a method for generating syngas comprising heating woodchips in a vessel comprising a pathway and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis with the woodchips forming biochar and releasing syngas when undergoing pyrolysis.
  • the method further comprises displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis, and discharging the filtered syngas from the vessel.
  • a system for generating syngas comprising a vessel comprising a pathway for heating woodchips therein, and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis with the woodchips forming biochar and releasing syngas when undergoing pyrolysis.
  • the pathway is shaped and adapted for displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis with the filtered syngas being dischargeable from the vessel.
  • FIG. 1 shows an exemplary system diagram of a system for generating syngas comprising a vessel and a pathway in accordance with an aspect of the invention
  • FIG. 2 shows an exemplary system diagram of the system for generating syngas of FIG. 1 for further processing of the syngas discharged from the vessel;
  • FIG. 3 shows an exemplary process flow diagram of a method for generating syngas for implementing with the system for generating syngas of FIG. 1 in accordance with another aspect of the invention.
  • FIG. 4 shows an exemplary system diagram of the system for generating syngas of FIG. 1 with the syngas being displaced substantially against the flow of woodchips along the pathway.
  • syngas method 100 a method for generating syngas 100
  • system 20 a system for generating syngas 20
  • the syngas method 100 comprises a step 110 of heating woodchips 22 in a vessel 24 comprising a pathway 26 and a heat generator 28 in thermal communication with the pathway 26 to thermally degenerate the woodchips 22 by pyrolysis.
  • the woodchips 22 is for forming biochar 30 and for releasing syngas 32 when undergoing pyrolysis.
  • the syngas method 100 further comprises a step 112 of displacing the generated syngas 32 along the pathway 26 to thereby filter the syngas 32 through at least one of the woodchips 22 and the biochar 30 undergoing pyrolysis, and a step 114 of discharging the filtered syngas 32 from the vessel 24.
  • the woodchips 22, in whichever stage of pyrolysis will act to function as a filter medium to remove, trap or scrub the impurities from the syngas 32 to thereby clean the syngas 32.
  • the pathway 26 is for displacing the woodchips 22, at different stages of charring, across the heat generator 28 and to displace the generated syngas 32 through at least one of the woodchips 22 and the biochar 30 undergoing pyrolysis.
  • the vessel 24 is a pressure vessel made from heat resistant and high strength material such as steel.
  • the heat generator 28 is capable of generating heat at and beyond 400 degrees Celsius. Further preferably, the heat generator 28 is capable of generating heat at and beyond 900 degrees Celsius to achieve flash pyrolysis of the woodchips 22, for example flash vacuum pyrolysis.
  • the pathway 26 comprises a closed-loop circuit for recirculating the syngas for filtering through at least one of the woodchips 22 and the biochar.
  • the pathway 26 may be formed from one or more passageways (not shown).
  • the step 112 of displacing the generated syngas 32 along the pathway 26 comprises a step 120 of displacing the woodchips 22 along the pathway 26 by a conveyor system 34, for example a screw conveyor system, for heating by the heat generator 28 for forming the biochar 30.
  • the conveyor system 34 may partially or completely rely on gravity feeding of the woodchips 22 along the pathway 26 for pyrolysis, or flash pyrolysis, thereof.
  • the step 112 of displacing the generated syngas 32 along the pathway 26 may further comprise a step 122 of displacing the generated syngas 32 by a displacement system 36 along the pathway 26 and substantially through the woodchips 22 undergoing pyrolysis.
  • the woodchips 22 are preferably pre-heated before being introduced into the vessel 24.
  • the displacement system 36 can be, for example, an air blower or through the use of coanda effect/flow configuration. In one implementation, the displacement system 36 may be form integral with the heat generator 28.
  • the heat generator 28 is one an electrical heater and a heat-exchanger and the released, or generated, syngas 32 is at least one of hydrogen, methane, carbon monoxide, and carbon dioxide.
  • the heat-exchanger used may be an ablative heat-exchanger fueled by, for example, flue gas.
  • the syngas method 100 further comprises a step 130 of injecting the woodchips 22 into the pathway 26 of the vessel 24, by a displacement screw conveyor 38 or the like displacement system, prior to the step 110 of heating the woodchips 22 in the vessel 24.
  • the syngas method 100 further comprises a step 132 of ejecting the biochar 30 from the vessel 24 in response to the syngas 32 been substantially discharged therefrom.
  • the step 114 of discharging the filtered syngas 32 from the vessel 24 comprises a step 140 of discharging the filtered syngas 32 to one of a downstream process 40 and a storage system 42, and a step 142 of generating at least one of heat energy and mechanical energy from the filtered syngas 32 by a gas engine as part of the downstream process 40.
  • the syngas system 20 comprises the vessel 24 comprising and defining the pathway 26 and the heat generator 28 in thermal communication with the pathway 26.
  • the syngas system 20 further comprises the conveyor system 34, the displacement system 36 and displacement screw conveyor 38.
  • the syngas system 20 can further comprise at least one of installations or systems for performing the downstream process 40 and the storage system 42.
  • the vessel 24 further comprises a first opening 50 for receiving the woodchips 22 into the vessel 24 to be heated to pyrolysis and a second opening 52 for the removal or discharge of the biochar 30 from the vessel 24.
  • each of the first opening 50 and the second opening 52 has a door, lid, gate or access control system that is operable and adapted for substantially impeding escape of fluids, for example the syngas 32, from the vessel 24 when pressurized and for defining the pathway 26, in part.
  • Discharge, or ejection, of the biochar 30 from the vessel 24 can be one or both of gravity assisted and mechanized using a displacement system similar to the displacement screw conveyor 38.
  • the vessel 24 can comprise only one opening serving both the functions of the first opening 50 and the second opening 52 for introducing woodchips 22 and ejecting or removal of biochar 30 from the vessel.
  • the same displacement screw conveyor 38 or the like displacement system may be used for displacing the woodchips 22 into and for removal of biochar 30 from the vessel 24, through the opening.
  • the filtered syngas 32 may be discharged from the vessel 24 by way of the pressure in the vessel with or without the existence or use of the displacement system.
  • the syngas 32 is preferably displaced substantially against the direction of flow of the woodchips 22 travelling along the pathway 28 during pyrolysis, or flash pyrolysis, to improve filtration thereof.
  • the syngas 32 may additionally or alternatively be displaced substantially along or perpendicular to the direction of flow of the woodchips 22 travelling along the pathway 28.
  • Discharge of the filtered syngas 32 may be at one or both of the first opening 50 and the second opening 52. Additionally or alternatively, the filtered syngas 32 may be discharged through a port 53 defined by or formed with the vessel 24.
  • the vessel 24 can further comprise a discharge valve 54, whether operated automatically by pressure relief or timedelay, remotely through wired or wireless control or manually through operating of the discharge valve 54, for controlling or metering discharge of the filtered syngas 32 from the vessel 24.
  • the discharge valve 54 is configured and disposed at one of the port 53, the first opening 50 and the second opening 52.
  • the port 53 may be defined adjacent one of the first opening 50 and the second opening 52.
  • aspects of particular embodiments of the present disclosure address at least one aspect, problem, limitation, and/or disadvantage associated with existing syngas generating approaches. While features, aspects, and/or advantages associated with certain embodiments have been described in the disclosure, other embodiments may also exhibit such features, aspects, and/or advantages, and not all embodiments need necessarily exhibit such features, aspects, and/or advantages to fall within the scope of the disclosure. It will be appreciated by a person of ordinary skill in the art that several of the above-disclosed structures, components, or alternatives thereof, can be desirably combined into alternative structures, components, and/or applications. In addition, various modifications, alterations, and/or improvements may be made to various embodiments that are disclosed by a person of ordinary skill in the art within the scope of the present disclosure, which is limited only by the following claims.

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  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
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Abstract

Disclosed herein is a method for generating syngas comprising heating woodchips in a vessel comprising a pathway and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis with the woodchips forming biochar and releasing syngas when undergoing pyrolysis. The method further comprises displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis, and discharging the filtered syngas from the vessel.

Description

METHOD AND SYSTEM FOR GENERATING SYNGAS
TECHNICAL FIELD
This invention relates generally to a method and system for generating syngas.
Background
Low density agricultural biomass, for example bark and wood chips, is typically widely dispersed within a given geographical area, difficult to collect and expensive to transport economically. In the fast pyrolysis of low-density agricultural biomass, a common problem that makes the process uneconomical is the prohibitive cost of transporting these bulky materials to a central processing site. Application of fluid bed fast pyrolysis technology to Such materials therefore relies upon a significant reduction or elimination of these material transportation costs. It would be desirable to provide “self-contained fast pyrolysis process equipment that is compact, mobile and has the ability to be set up and operated close to the source of the feed materials. To make it easier for farmers and workmen, particularly in the developing world, to take advantage of Such mobile equipment, it would also be desirable that the equipment be simple to operate and flexible in terms of the choice of fuel source. The process employed in using the equipment should be forgiving in terms of particle size and biomass moisture content. The process should also take advantage of rapid heat transfer and short solids residence time to reduce vessel size and increase throughput.
To date, conventional fast pyrolysis processes employ multiple vessels, are complex to operate, are inflexible and/or are not suitable for mobile operation. Compact systems that combine the combustion chamber and pyrolysis reactor in a single vessel usually involve mixing of fluids and/or solids between the two portions of the vessel; this leads to contamination and/or destruction of the most valuable condensable liquid products in the product gas. The need therefore exists for an improved apparatus for pyrolysis of low-density agricultural biomass and a process for use thereof. Combustible gases can be generated by thermo-chemical conversion of biomass. Biomass may be any suitable carbon-containing fuel. Non-limiting examples of biomass include: wood in any suitable such as sawdust, shavings, pellets, woodchips and other wood residue, municipal waste, sewage, coal, bitumen, fossil fuels, food waste and plant matter. Combustible gases may be liberated from biomass by heating the biomass in an oxygen- reduced atmosphere. The heating may be done by partially oxidizing the biomass or by way of a separate heat source. The heating causes the biomass to release combustible gases which are also known as “syngas”, “synthesis gas”, “producer gas” and “product gas”.
Syngas produced from biomass may be used for various applications. For example, the gases may be burned to generate heat, processed to make synthetic fuels (the synthetic fuels may comprise gaseous, liquid or solid fuels), used to run an engine, used as a fuel for a fuel cell or used as a fuel to run a turbine. Syngas liberated from biomass may include fractions, such as tars and heavier hydrocarbons, that can condense in ducts and other equipment. This can cause significant operational and maintenance problems. There is a need for practical and energy-efficient methods and apparatus for producing clean syngas from biomass, specifically from woodchips
Summary
In accordance with a first aspect of the invention, there is disclosed a method for generating syngas comprising heating woodchips in a vessel comprising a pathway and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis with the woodchips forming biochar and releasing syngas when undergoing pyrolysis. The method further comprises displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis, and discharging the filtered syngas from the vessel. In accordance with a second aspect of the invention, there is disclosed a system for generating syngas comprising a vessel comprising a pathway for heating woodchips therein, and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis with the woodchips forming biochar and releasing syngas when undergoing pyrolysis. The pathway is shaped and adapted for displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis with the filtered syngas being dischargeable from the vessel.
Brief Description of the Drawings
FIG. 1 shows an exemplary system diagram of a system for generating syngas comprising a vessel and a pathway in accordance with an aspect of the invention;
FIG. 2 shows an exemplary system diagram of the system for generating syngas of FIG. 1 for further processing of the syngas discharged from the vessel;
FIG. 3 shows an exemplary process flow diagram of a method for generating syngas for implementing with the system for generating syngas of FIG. 1 in accordance with another aspect of the invention; and
FIG. 4 shows an exemplary system diagram of the system for generating syngas of FIG. 1 with the syngas being displaced substantially against the flow of woodchips along the pathway.
Detailed Description
An exemplary embodiment of the present invention, a method for generating syngas 100 (“syngas method 100”), implementable with a system for generating syngas 20 (“syngas system 20”), is described hereinafter with reference to FIG. 1 to FIG. 4. The syngas method 100 comprises a step 110 of heating woodchips 22 in a vessel 24 comprising a pathway 26 and a heat generator 28 in thermal communication with the pathway 26 to thermally degenerate the woodchips 22 by pyrolysis. The woodchips 22 is for forming biochar 30 and for releasing syngas 32 when undergoing pyrolysis. The syngas method 100 further comprises a step 112 of displacing the generated syngas 32 along the pathway 26 to thereby filter the syngas 32 through at least one of the woodchips 22 and the biochar 30 undergoing pyrolysis, and a step 114 of discharging the filtered syngas 32 from the vessel 24. As the syngas 32 is generated together with tar, soot and the like impurities, the woodchips 22, in whichever stage of pyrolysis, will act to function as a filter medium to remove, trap or scrub the impurities from the syngas 32 to thereby clean the syngas 32.
Preferably, when in use, the pathway 26 is for displacing the woodchips 22, at different stages of charring, across the heat generator 28 and to displace the generated syngas 32 through at least one of the woodchips 22 and the biochar 30 undergoing pyrolysis. Preferably, the vessel 24 is a pressure vessel made from heat resistant and high strength material such as steel. Further, the heat generator 28 is capable of generating heat at and beyond 400 degrees Celsius. Further preferably, the heat generator 28 is capable of generating heat at and beyond 900 degrees Celsius to achieve flash pyrolysis of the woodchips 22, for example flash vacuum pyrolysis. The pathway 26 comprises a closed-loop circuit for recirculating the syngas for filtering through at least one of the woodchips 22 and the biochar. The pathway 26 may be formed from one or more passageways (not shown).
Preferably, the step 112 of displacing the generated syngas 32 along the pathway 26 comprises a step 120 of displacing the woodchips 22 along the pathway 26 by a conveyor system 34, for example a screw conveyor system, for heating by the heat generator 28 for forming the biochar 30. Alternatively, the conveyor system 34 may partially or completely rely on gravity feeding of the woodchips 22 along the pathway 26 for pyrolysis, or flash pyrolysis, thereof. The step 112 of displacing the generated syngas 32 along the pathway 26 may further comprise a step 122 of displacing the generated syngas 32 by a displacement system 36 along the pathway 26 and substantially through the woodchips 22 undergoing pyrolysis. The woodchips 22 are preferably pre-heated before being introduced into the vessel 24. The displacement system 36 can be, for example, an air blower or through the use of coanda effect/flow configuration. In one implementation, the displacement system 36 may be form integral with the heat generator 28.
The heat generator 28 is one an electrical heater and a heat-exchanger and the released, or generated, syngas 32 is at least one of hydrogen, methane, carbon monoxide, and carbon dioxide. The heat-exchanger used may be an ablative heat-exchanger fueled by, for example, flue gas.
The syngas method 100 further comprises a step 130 of injecting the woodchips 22 into the pathway 26 of the vessel 24, by a displacement screw conveyor 38 or the like displacement system, prior to the step 110 of heating the woodchips 22 in the vessel 24. The syngas method 100 further comprises a step 132 of ejecting the biochar 30 from the vessel 24 in response to the syngas 32 been substantially discharged therefrom.
The step 114 of discharging the filtered syngas 32 from the vessel 24 comprises a step 140 of discharging the filtered syngas 32 to one of a downstream process 40 and a storage system 42, and a step 142 of generating at least one of heat energy and mechanical energy from the filtered syngas 32 by a gas engine as part of the downstream process 40.
The syngas system 20 comprises the vessel 24 comprising and defining the pathway 26 and the heat generator 28 in thermal communication with the pathway 26. Preferably, the syngas system 20 further comprises the conveyor system 34, the displacement system 36 and displacement screw conveyor 38. The syngas system 20 can further comprise at least one of installations or systems for performing the downstream process 40 and the storage system 42.
Preferably, the vessel 24 further comprises a first opening 50 for receiving the woodchips 22 into the vessel 24 to be heated to pyrolysis and a second opening 52 for the removal or discharge of the biochar 30 from the vessel 24. It is preferred that each of the first opening 50 and the second opening 52 has a door, lid, gate or access control system that is operable and adapted for substantially impeding escape of fluids, for example the syngas 32, from the vessel 24 when pressurized and for defining the pathway 26, in part. Discharge, or ejection, of the biochar 30 from the vessel 24 can be one or both of gravity assisted and mechanized using a displacement system similar to the displacement screw conveyor 38. In some implementations, the vessel 24 can comprise only one opening serving both the functions of the first opening 50 and the second opening 52 for introducing woodchips 22 and ejecting or removal of biochar 30 from the vessel. In such an implementation, the same displacement screw conveyor 38 or the like displacement system may be used for displacing the woodchips 22 into and for removal of biochar 30 from the vessel 24, through the opening.
As pressure is built up in the vessel 24 as a result of the generated syngas 32, the filtered syngas 32 may be discharged from the vessel 24 by way of the pressure in the vessel with or without the existence or use of the displacement system. The syngas 32 is preferably displaced substantially against the direction of flow of the woodchips 22 travelling along the pathway 28 during pyrolysis, or flash pyrolysis, to improve filtration thereof. Although this is preferred, the syngas 32 may additionally or alternatively be displaced substantially along or perpendicular to the direction of flow of the woodchips 22 travelling along the pathway 28.
Discharge of the filtered syngas 32 may be at one or both of the first opening 50 and the second opening 52. Additionally or alternatively, the filtered syngas 32 may be discharged through a port 53 defined by or formed with the vessel 24. The vessel 24 can further comprise a discharge valve 54, whether operated automatically by pressure relief or timedelay, remotely through wired or wireless control or manually through operating of the discharge valve 54, for controlling or metering discharge of the filtered syngas 32 from the vessel 24. When implemented, the discharge valve 54 is configured and disposed at one of the port 53, the first opening 50 and the second opening 52. The port 53 may be defined adjacent one of the first opening 50 and the second opening 52.
Aspects of particular embodiments of the present disclosure address at least one aspect, problem, limitation, and/or disadvantage associated with existing syngas generating approaches. While features, aspects, and/or advantages associated with certain embodiments have been described in the disclosure, other embodiments may also exhibit such features, aspects, and/or advantages, and not all embodiments need necessarily exhibit such features, aspects, and/or advantages to fall within the scope of the disclosure. It will be appreciated by a person of ordinary skill in the art that several of the above-disclosed structures, components, or alternatives thereof, can be desirably combined into alternative structures, components, and/or applications. In addition, various modifications, alterations, and/or improvements may be made to various embodiments that are disclosed by a person of ordinary skill in the art within the scope of the present disclosure, which is limited only by the following claims.

Claims

8
Claims
1. A method for generating syngas comprising: heating woodchips in a vessel comprising a pathway and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis, the woodchips forming biochar and releasing syngas when undergoing pyrolysis; displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis; and discharging the filtered syngas from the vessel.
2. The method as in claim 1, the pathway comprising a closed-loop circuit for recirculating the syngas for filtering through at least one of the woodchips and the biochar.
3. The method as in claim 1, displacing the generated syngas along the pathway comprising: displacing the woodchips along the pathway by a conveyor system for heating by the heat generator for forming the biochar, the conveyor system being one of a displacement screw conveyor and a gravity feed system.
4. The method as in claim 1, displacing the generated syngas along the pathway comprising: displacing the generated syngas by a displacement system along the pathway and substantially through the woodchips undergoing pyrolysis.
5. The method as in claim 1, the heat generator being one an electrical heater; a heatexchanger and an ablative heat-exchanger.
6. The method as in claim 1, further comprising: 9 injecting the woodchips into the pathway of the vessel by a displacement screw conveyor. The method as in claim 1, further comprising: ejecting the biochar from the vessel in response to the syngas being substantially discharged therefrom. The method as in claim 1, discharging the filtered syngas from the vessel comprising: discharging the filtered syngas from a port to one of a downstream process and a storage system, wherein the port being defined by the vessel and configured for facilitating flow of the filtered syngas in a direction that is substantially against the flow of the woodchips along the pathway. The method as in claim 8, further comprising: generating at least one of heat energy and mechanical energy from the filtered syngas by a gas engine as part of the downstream process. The method as in claim 1, the syngas being at least one of hydrogen, methane, carbon monoxide, and carbon dioxide. A system for generating syngas comprising: a vessel comprising: a pathway for heating woodchips therein; and a heat generator in thermal communication with the pathway to thermally degenerate the woodchips by pyrolysis, the woodchips forming biochar and releasing syngas when undergoing pyrolysis, 10 wherein the pathway is shaped and adapted for displacing the generated syngas along the pathway to thereby filter the syngas through at least one of the woodchips and the biochar undergoing pyrolysis, wherein the filtered syngas is dischargeable from the vessel.
12. The system as in claim 11, the pathway comprising a closed-loop circuit for recirculating the syngas for filtering through at least one of the woodchips and the biochar.
13. The system as in claim 11, further comprising: a conveyor system for displacing the woodchips along the pathway for heating by the heat generator for forming the biochar, the conveyor system being one of a displacement screw conveyor and a gravity feed system.
14. The system as in claim 11, further comprising: a displacement system for displacing the generated syngas along the pathway and substantially through the woodchips undergoing pyrolysis.
15. The system as in claimll, the heat generator being one an electrical heater, a heatexchanger; and an ablative heat exchanger.
16. The system as in claim 11, further comprising: a displacement screw conveyor for injecting the woodchips into the pathway of the vessel by.
17. The system as in claim 11, the biochar being ejected from the vessel in response to the syngas been substantially discharged therefrom.
18. The system as in claim 11, the filtered syngas being discharged from a port to one of a downstream process and a storage system, the port being defined by the vessel and 11 configured for facilitating flow of the filtered syngas in a direction that is substantially against the flow of the woodchips along the pathway. The system as in claim 18, at least one of heat energy and mechanical energy is generated from the filtered syngas by a gas engine as part of the downstream process. The system as in claim 11, the syngas being at least one of hydrogen, methane, carbon monoxide, and carbon dioxide.
PCT/SG2022/050728 2021-11-13 2022-10-11 Method and system for generating syngas WO2023086012A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5792340A (en) * 1990-01-31 1998-08-11 Ensyn Technologies, Inc. Method and apparatus for a circulating bed transport fast pyrolysis reactor system
JP2003213268A (en) * 2002-01-21 2003-07-30 Maekawa Seisakusho:Kk Batch type carbonization treatment apparatus
WO2005047436A1 (en) * 2003-11-05 2005-05-26 Biomass Energy Solutions, Inc. Process and apparatus for biomass gasification
WO2006130977A1 (en) * 2005-06-08 2006-12-14 The University Of Western Ontario Apparatus and process for the pyrolysis of agricultural biomass
US20170120211A1 (en) * 2014-06-09 2017-05-04 Hatch Ltd. Plug flow reactor with internal recirculation fluidized bed

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5792340A (en) * 1990-01-31 1998-08-11 Ensyn Technologies, Inc. Method and apparatus for a circulating bed transport fast pyrolysis reactor system
JP2003213268A (en) * 2002-01-21 2003-07-30 Maekawa Seisakusho:Kk Batch type carbonization treatment apparatus
WO2005047436A1 (en) * 2003-11-05 2005-05-26 Biomass Energy Solutions, Inc. Process and apparatus for biomass gasification
WO2006130977A1 (en) * 2005-06-08 2006-12-14 The University Of Western Ontario Apparatus and process for the pyrolysis of agricultural biomass
US20170120211A1 (en) * 2014-06-09 2017-05-04 Hatch Ltd. Plug flow reactor with internal recirculation fluidized bed

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