EP2396465A2 - Methods for producing biomass-based fuel with pulp processing equipment - Google Patents
Methods for producing biomass-based fuel with pulp processing equipmentInfo
- Publication number
- EP2396465A2 EP2396465A2 EP10708007A EP10708007A EP2396465A2 EP 2396465 A2 EP2396465 A2 EP 2396465A2 EP 10708007 A EP10708007 A EP 10708007A EP 10708007 A EP10708007 A EP 10708007A EP 2396465 A2 EP2396465 A2 EP 2396465A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- biomass
- pulp
- pellets
- processing plant
- pellet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
- C10L5/14—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders
- C10L5/143—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders with lignin-containing products
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/26—Multistage processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/08—Removal of fats, resins, pitch or waxes; Chemical or physical purification, i.e. refining, of crude cellulose by removing non-cellulosic contaminants, optionally combined with bleaching
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/28—Cutting, disintegrating, shredding or grinding
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/30—Pressing, compressing or compacting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/32—Molding or moulds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Definitions
- the present disclosure relates to processing energy resources, and, more particularly, to methods for producing biomass-based fuel with pulp processing equipment.
- Biomass of various types may be used to manufacture densified fuel.
- Biomass may take the form of wood, woody biomass, or other biomass such as, without limitation, sugarcane bagasse, straw, switchgrass, or other agricultural material where biomass may be a byproduct of other processes or where biomass may be a feedstock grown for the purpose of making directly or indirectly, a fuel.
- pellets and “briquettes” commonly refer to fragments of biomass, treated biomass, coal, or some or all in combination that have been compacted to form a densified fuel produced in various sizes and shapes.
- various size feedstocks such as sawdust or chips ranging in size from less than 1" to over 3" along the longest dimension, may be processed and pelletized.
- Material may be dried and extruded through dies sized for the desired cross-sectional area and of varying lengths.
- Floor-mounted machines or presses with dyes may receive prepared feedstock and discharge extruded pellets sized (e.g., by cutting or trimming) to desired lengths at the outlet of the machines or presses.
- white pellet may refer to the use of suitably sized and pelletized wood that has had minimal if any treatment beyond chipping and grinding prior to being introduced into the pellet machine or press. White pellets may be used in residential heaters, in district heating, and/or in industrial power generation, including coal-fired power generation plants.
- white pellets Industrial use of white pellets may be limited by the white pellets' inherent properties including sensitivity to water, low hardness, and lack of durability, leading to the production of dust as the pellets abrade through handling and/or as a result of moisture absorption. These properties, independently and together, may cause the pellets to rapidly disintegrate. Due to such limitations, white pellets require specific storage and handling accommodations to protect the pellets from the elements and to mitigate dust concentrations that may create an explosion hazard. Consequently, using white pellets in coal-fired power generation plants in concentrations from 1% to 100% may require significant adaptations to both plant operating procedures and capital equipment considering, for example, that coal may be typically stored and handled outdoors with exposure to the elements,
- black pellet may refer to a pellet with a lignin binder and/or coating induced by processing the biomass feedstock prior to introducing the biomass into the pellet machine or press.
- Steam explosion may be used in manufacturing densified fuel as a means to free lignin from cellular structures of biomass, thereby allowing the lignin to commingle with the fiber portion of the biomass and, when compacted by the pellet machine or press, forming both a waterproof or water-resistant internal binder as well as a waterproof or water-resistant protective surface coating that enhances the durability of pellets and briquettes.
- pellets and briquettes may have improved abrasion properties and may be stored outdoors in a manner similar to outdoor storage of coal. Having physical characteristics similar to coal may facilitate the introduction of pellets into coal handling processes of conventional coal plants, resulting in both capital cost and operating cost savings as compared to the use of white pellets.
- the present disclosure relates to processing energy resources, and, more particularly, to methods for producing biomass-based fuel with pulp processing equipment.
- a method of manufacturing biomass-based pellets includes liberating lignin from biomass-based feedstock via pulp digester.
- the method may include pelletizing the biomass-based feedstock and the liberated lignin to form the biomass- based pellets.
- a method for converting a pulp processing plant to a biomass-based pellet manufacturing plant includes installing a pellet mill in the pulp processing plant.
- the method may include re-routing output from a pulp digester, such that the output enters the pellet mill and bypassing unnecessary equipment.
- a method for mitigating the costs of establishing a biomass-based pellet manufacturing plant includes identifying an existing pulp processing plant, obtaining permission to access and convert the pulp processing plant, and converting the pulp processing plant for manufacture of biomass-based pellets.
- Figure 1 illustrates a block diagram indicating a method of mitigating the costs of establishing a biomass-based pellet manufacturing plant in accordance with certain embodiments of the present invention.
- Figure 2 illusttates a block diagram indicating a method for converting a pulp processing plant to a biomass-based pellet manufacturing plant in accordance with certain embodiments of the present invention.
- Figure 3 illustrates a block diagram indicating a converted ⁇ il ⁇ processing plant in accordance with certain embodiments of the present disclosure.
- a biomass-based pellet may include without limitation a fragment or piece of any shape, size, or division, including a briquette
- a biomass-based pellet, and biomass- based material may include, at least in part and without limitation, material consisting of or derived from wood, woody biomass, or any other biomass such as bamboo, sugarcane bagasse, straw, switehgrass, husks, or other agricultural material where biomass may be a byproduct of other processes or where biomass may be a feedstock grown for the purpose of manufacturing a fuel.
- existing pulp making, papermaking, and/or cellulosic ethanol equipment may be used to produce biomass-based exploded or otherwise treated product that may be ready for densification to achieve a biomass- based pellet.
- this type of pellet is called a "high-density" or "black” pellet.
- existing technology e.g., equipment widely used for preprocessing wood in the pulp and paper industry, may be adapted to accomplish the liberation of lignin present in biomass-based feedstock.
- An existing pulp processing plant may be used with some or all equipment intact and, with the addition of pelletizing equipment, may produce a steam-exploded biomass-based pellet without building new steam explosion facilities.
- Conversion of conventional pulp processing plant digestion technology may be adapted to so that chemical treatment, which may be typical to pulping processes, may not be necessary in a converted pulp processing plant.
- Existing equipment may be converted to steam explosion equipment and coupled with densification processes to manufacture biomass-based pellets.
- the costs associated with establishing biomass-based pellet manufacturing may be reduced by first identifying 100 an existing pulp processing plant. This identification may include researching several pulp processing plants and determining whether any of them is in financial distress and/or in need of financial stimulation.
- the existing pulp processing plant may be a paper mill, a freestanding pulp processing facility, or any other pulp processing source.
- permission 105 may be obtained to access and convert the pulp processing plant to a biomass-based pellet manufacturing facility. This permission 105 may be obtained through contract agreement, purchase of assets, merger, acquisition, lease agreement, or any other grant of rights to access and conversion, including altering intended use of an asset already owned,
- costs may be further reduced by identifying 115 an existing source of biomass-based feedstock, before, after, or in conjunction with identification 100 of pulp processing plant.
- sources of biomass-based feedstock may include nearby forests, grasslands, or any of a number of other renewable biomass-based feedstock sources.
- permission 120 may be obtained to access and use the biomass-based feedstock for manufacture of biomass-based pellets. This permission 120 may be obtained through contract agreement, purchase of assets, merger, acquisition, lease agreement, or any other grant of rights to access and use, including altering intended use of an asset already owned.
- an additional step of obtaining permission 125 to transport the biomass-based feedstock from the existing source to the pulp processing plant may be included either in addition to, or in place of the step of obtaining permission to access and use the biomass-based feedstock.
- this permission may include a contract for purchase of goods, including quantities requirements and term of contract provisions.
- a pulp processing plant may be converted for use in biomass-based pellet manufacturing. Such a conversion may involve converting 200 an existing pulp digester for use in the manufacture of biomass-based pellets, installing 205 a pellet mill in the pulp processing plant, re-routing 210 output from the pulp digester, such that the output enters the pellet mill, and/or bypassing 215 unused components in the pulp processing plant.
- Converting 200 an existing pulp digester may involve removal of some or all equipment used for chemical treatment and/or lignin removal.
- Installing 205 a pellet mill may involve leasing, purchasing, or otherwise acquiring a pellet mill of the type described below with reference to Figure 3, and ensuring that it is delivered to the pulp processing plant for installation in a location suitable for use with the rest of the equipment useful for bi ⁇ mass-based pellet manufacture.
- Re-routing 210 the output from the pulp digester may not require physical changes to equipment, and may be as simple as moving a conveyor, or may involve complex movements of equipment.
- re-routing 210 the output from the pulp digester may include re-routing and/or bypassing intermediate equipment, such as, for example, a blow tank.
- Bypassing 215 unused components may include bypassing particular equipment useful in pulp processing plant operations but unnecessary in biomass-based pellet manufacture. When bypassed equipment is unnecessary, the method may further include removing 220 and/or selling 225 the bypassed equipment.
- Biomass-based feedstock may be collected from a location near converted pulp processing plant 300.
- biomass-based feedstock may be timber collected from forestland adjacent to converted pulp processing plant 300.
- biomass-based feedstock may be delivered to pulp processing plant 300 from a remote location.
- biomass-based feedstock may be bamboo grown in another country and delivered to pulp processing plant 300, either intact, or pre-processed to some extent. Any of a number of other sources for biomass-based feedstock may also be suitable. Depending on the source and condition of the biomass-based feedstock, it may undergo additional treatment in existing facilities 305 prior to entry into pulp digester 325.
- Existing facilities 305 may include any number and variety of existing papermaking and/or cellulosic ethanol production equipment.
- existing facilities 305 may include one or more of storage yard 310, debarking equipment 315, chipping equipment 320, pulp digester 325, and blow tank 330, which may or may not be coupled together by any conveying equipment or other means of transferring material.
- debarking equipment 315 may or may not be coupled together by any conveying equipment or other means of transferring material.
- one or more of the units of existing facilities 305 may be modified or even omitted.
- biomass-based feedstock may be stored in storage yard 310 for some time prior to use.
- Storage yard 310 may be a location, with certain equipment if desired, adapted for one or more of receiving, storing, and preparing biomass-based material for processing.
- storage yard 310 is a wood yard suitable for use with wood-based materials.
- debarking equipment 315 may be any equipment and/or machinery configured to prepared biomass-based material for further processing by removing material, for example, by removing bark from surfaces of logs.
- Biomass-based feedstock may pass through flume shower 360 or other equipment suitable to wash off dirt or other impurities in biomass-based feedstock, when using unprocessed biomass-based feedstock.
- Flume shower 360 may be part of existing facilities 305, or flume shower 360 may be added to existing facilities 305 for use in biomass-based pellet manufacture. In some instances, flume shower 360 may be modified or omitted, depending on the particular application.
- Chipping equipment 320 may be any equipment and/or machinery configured to reduce biomass-based material into smaller parts.
- a grinder (not shown) may be used for further reduction in size of biomass-based feedstock.
- Biomass-based feedstock may pass through dryer 365, if desired, to reduce moisture content to a level suitable for use in pulp digester 325.
- dryer 365 may be used to obtain moisture content between 0% and 15% by weight.
- Dryer 365 may be a rotary dryer, steam dryer, superheated steam dryer, low temperature dryer, or any of a number of other devices for adjusting moisture content.
- Existing pulp processing plants may typically use pulp digester 325 in a cooking process, along with significant amounts of chemicals and/or enzymes sometime referred to as "cooking liquor.”
- the cooking process may be used to separate Iignin and/or sugars from fiber and maintain separation in dilute slurry.
- the Iignin and fiber are typically moved to separate vessels in existing pulp processing plants, with no further comingling of fiber and Iignin.
- chemicals and/or enzymes may be added to biomass-based feedstock in a chemical treatment operation (not shown) to produce a biomass-based slurry for use in pulp digester 325.
- chemicals and enzymes may be omitted.
- Biomass-based feedstock may enter pulp digester 325 through an opening sized accordingly.
- Pulp digester 325 may include any vessel and associated equipment configured to receive biomass-based feedstock (or slu ⁇ y) and process it under desired pressures and at desired temperatures.
- Pulp digester 325 may include one or more vessels configured to operate in a batch manner, in a multi-batch or semi-continuous manner, or in a continuous manner. Examples of other existing pulp digesters 325 may include, but are not limited to, Masonite guns, standard Kraft digesters, standard sulfite digesters, chemithermomechanical pulping, thermomechanical pulping, groundwood pulping, and pressurized groundwood pulping.
- the supply of biomass-based feedstock (or slurry) may cease and the pulp digester 325 may be closed off.
- the supply of biomass-based feedstock (or slurry) may be continuous.
- pulp digester 325 will, over a predetermined amount of time, treat or cook the biomass-based feedstock (or slurry), using steam, either with or without chemical additives and/or water, to liberate lignin from the biomass-based feedstock by steam explosion.
- pulp digester 325 may be opened to adjacent blow tank 330, allowing removal of cooked biomass-based material, which includes the biomass-based feedstock and the liberated lignin, from pulp digester 325 via explosion into blow tank.
- Cooked biomass-based material may transferred to the blow tank 330 on a batch and/or continuous basis.
- Blow tank 330 may include any vessel and associated equipment configured to receive treated, or cooked biomass-based material, which may be in a slurry state with cooking liquor and/or steam, from pulp digester 325.
- pulping technologies may involve pressures below 150 psi (pounds per square inch), chemical additives, one or more cooking processes, and a dilute slurry that may comprise approximately 50% dry solids,
- Certain embodiments may accomplish steam explosion at pressures in approximate ranges of 225 psi to 375 psi and/or may produce a product of 85% to 92% dry solids, while keeping lignin with fiber for pellet processing.
- Steam impregnating raw fuel may pre-soften the material.
- Certain embodiments may use chemicals with the steam impregnation to further soften or accelerate softening raw fiber prior to cooking. Such chemicals may include sodium sulfite, caustic soda, or any other suitable chemical, as would be appreciated by one of ordinary skill in the art having the benefit of this disclosure.
- Other embodiments may include addition of supplementary lignin and/or omit steam explosion from the process of liberating lignin.
- Cooked biomass-based material may pass from blow tank 330 through dryer 370, if desired, to reduce moisture content to a level suitable for use with pelletizing equipment 340.
- dryer 370 may be used to obtain moisture content between 0% and 15% by weight.
- Dryer 370 may be a rotary dryer, steam dryer, superheated steam dryer, o ⁇ any of a number of other devices for adjusting moisture content.
- Cooked biomass-based material may be transferred, either directly, or via one or more of blow tank 330 and dryer 370, from pulp digester 325 to pelletizing equipment 340, which may include one or more of a pellet mill 345, pellet cooling equipment 350 and pellet storage 355.
- Cooked biomass-based material may be processed by pellet mill 345 to form biomass-based pellets.
- Pellet mill 345 may be any device suitable for extrusion or other compression of cooked biomass-based material to create biomass-based pellets. After exiting pellet mill 345, biomass-based pellets may pass through or otherwise encounter pellet cooling equipment 350 for cooling.
- Pellet cooling equipment 350 may be any equipment or means for cooling biomass-based pellets, including, but not limited to, air circulation or water quenching.
- pellet cooling equipment 350 may not be needed, and biomass-based pellets may be cooled during storage. Biomass-based pellets may then be stored at pellet storage 355. Because high-density biomass-based pellets are moisture and abrasion resistant, pellet storage 355 may be, for example, indoor storage, outdoor storage, covered storage, or uncovered storage. Additionally biomass-based pellets may be used in standard coal handling equipment, including railcars, conveyors, storage, and ⁇ tiher processing facilities, eliminating the need for significant capital investment in order to coal fire biomass-based pellets with coal.
- a typical existing pulp processing plant may include balance of the existing plant 335, which may constitute equipment that may not be needed in manufacturing and processing biomass-based pellets. Balance of the existing plant 335 may be removed or left in place, as desired or as needed to accommodate pellet equipment 340.
- steam may refer not only to water vapor, but may also include other vapors useful in the applications indicated above.
- the methods disclosed herein provide the potential for significantly lowering costs of producing biomass-based fuel and initiating large-scale manufacturing and processing of biomass to make biomass-based feedstock for power generation units such as cogeneration, boilers and other types of power plants.
- Conversion of existing pulp processing plants according to the present disclosure offers significant economies compared to new construction of high-pressure steam explosion.
- Methods according to the present disclosure may be applied to existing pulp and feedstock production sites in any number of various wood and pulp and paper countries to facilitate business related to manufacturing, processing and delivering biomass-based fuel.
- Other technical advantages will be apparent to those of ordinary skill in the art in view of the specification, claims, and drawings.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US15255609P | 2009-02-13 | 2009-02-13 | |
| PCT/US2010/023929 WO2010093812A2 (en) | 2009-02-13 | 2010-02-11 | Methods for producing biomass-based fuel with pulp processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP2396465A2 true EP2396465A2 (en) | 2011-12-21 |
Family
ID=42237234
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP10708007A Withdrawn EP2396465A2 (en) | 2009-02-13 | 2010-02-11 | Methods for producing biomass-based fuel with pulp processing equipment |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20100206499A1 (en) |
| EP (1) | EP2396465A2 (en) |
| JP (2) | JP2012518060A (en) |
| KR (2) | KR20160119866A (en) |
| AU (2) | AU2010213719A1 (en) |
| BR (1) | BRPI1008497A2 (en) |
| CA (1) | CA2752604A1 (en) |
| WO (1) | WO2010093812A2 (en) |
Families Citing this family (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8968515B2 (en) | 2006-05-01 | 2015-03-03 | Board Of Trustees Of Michigan State University | Methods for pretreating biomass |
| US9206446B2 (en) | 2006-05-01 | 2015-12-08 | Board Of Trustees Of Michigan State University | Extraction of solubles from plant biomass for use as microbial growth stimulant and methods related thereto |
| US8394611B2 (en) | 2006-05-01 | 2013-03-12 | Board Of Trustees Of Michigan State University | Process for the treatment of lignocellulosic biomass |
| CA2760840C (en) | 2009-08-24 | 2014-12-02 | Board Of Trustees Of Michigan State University | Pretreated densified biomass products and methods of making and using same |
| US10457810B2 (en) * | 2009-08-24 | 2019-10-29 | Board Of Trustees Of Michigan State University | Densified biomass products containing pretreated biomass fibers |
| US8945245B2 (en) | 2009-08-24 | 2015-02-03 | The Michigan Biotechnology Institute | Methods of hydrolyzing pretreated densified biomass particulates and systems related thereto |
| EP2561084A4 (en) | 2010-04-19 | 2013-10-23 | Univ Michigan State | DIGESTIBLE LIGNOCELLULOSIC BIOMASS, WOOD EXTRACTION PRODUCTS AND METHODS OF MAKING SAME |
| US9057037B2 (en) | 2010-04-20 | 2015-06-16 | River Basin Energy, Inc. | Post torrefaction biomass pelletization |
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- 2010-02-11 CA CA2752604A patent/CA2752604A1/en not_active Abandoned
- 2010-02-11 EP EP10708007A patent/EP2396465A2/en not_active Withdrawn
- 2010-02-11 BR BRPI1008497A patent/BRPI1008497A2/en not_active IP Right Cessation
- 2010-02-11 KR KR1020167026849A patent/KR20160119866A/en not_active Ceased
- 2010-02-11 WO PCT/US2010/023929 patent/WO2010093812A2/en not_active Ceased
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