CN200996005Y - Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass - Google Patents
Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass Download PDFInfo
- Publication number
- CN200996005Y CN200996005Y CN 200620009199 CN200620009199U CN200996005Y CN 200996005 Y CN200996005 Y CN 200996005Y CN 200620009199 CN200620009199 CN 200620009199 CN 200620009199 U CN200620009199 U CN 200620009199U CN 200996005 Y CN200996005 Y CN 200996005Y
- Authority
- CN
- China
- Prior art keywords
- ash
- biomass
- high temperature
- pyrolysis
- pyrolysis reactor
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A pyrolysis biomass oil production device using circulating fluidized bed boiler high temperature ash includes a circulating fluidized bed boiler, a cyclone separator A, a high temperature ash obtaining device, a biomass powder cabin, a biomass feed sealing device, a spirally feeding device, a pyrolysis reactor, a cyclone separator B, a venture spraying and cooling device, a liquid collector, a solid biological carbon and circulating ash return device, a circulating water pump and a suction fan, which is characterized in that the top of the pyrolysis reactor is connected respectively with the lower straight pipe of the cyclone separator A through the high temperature ash obtaining device and with a feed cabin through a speed variable spiral feed device. The upper outlet of the pyrolysis reactor is connected with the cyclone separator B. The outlet on the bottom of the pyrolysis reactor is equipped with the solid biological carbon and circulating ash return device.
Description
Technical field
The utility model belongs to the utilization and the conversion field of biomass energy, and relating to a kind of is Wood Adhesives from Biomass the pyrolytic reaction device of bio oil.
Background technology
In numerous Wood Adhesives from Biomass technology, pyrolysis can be that fuel and chemical and cost are lower with Wood Adhesives from Biomass comparatively simply, becomes a focus of the research of biomass utilization in the world.Different according to pyrolytic process residence time of raw material and temperature, pyrolytic process can be divided into three major types: conventional pyrolysis, fast pyrogenation and sudden strain of a muscle are separated.Fast pyrogenation is meant under the condition of secluding air or little air, adopts medium temperature of reaction, and very short gas residence time is carried out pyrolytic process fast to biomass, through quenching and concentrated, obtains bio oil at last again.Bio oil is easy to store and transportation, and calorific value is about the over half of traditional fuel oil, can be used as the raw material of synthesis of chemicals again, can be directly used in the kiln burning.The maximum liquid yield of fast pyrogenation can reach 80%, and the research focus of pyrolytic technique concentrates on fast pyrogenation at present.Units such as domestic Shandong Technology Univ, East China University of Science, Zhejiang University, China Science ﹠ Technology University, process study institute of the Chinese Academy of Sciences, Guangzhou energy institute of the Chinese Academy of Sciences, Agricultural University Of Shenyang have carried out the research of biomass fast pyrogenation aspect, have obtained certain achievement.Wherein, Chinese Academy of Sciences's process study and Chinese Academy of Sciences's Guangzhou energy wait the biomass pyrolysis liquefaction device of developing, they propose the pyrolytic reaction solid product and are transmitted back in the boiler by returning charge U valve (L valve), but, charcoal finishes easy generation the in back in pyrolytic reaction and reunites and bond, cause the fluidisation variation, therefore be difficult to realize continuously operation reliably with returning charge U valve.Other biological matter fast pyrolysis process also owing to technical sophistication, is difficult to apply.
Summary of the invention
The purpose of this utility model is to provide a cover circulating fluidized bed high temperature ash pyrolysis biomass-making oil device, is thermophore with the high-temp circulating ash of circulating fluidized bed, and the fast pyrogenation biomass material is produced bio oil, produces the inflammable gas and the charcoal of part simultaneously.
The technical scheme that its technical problem that solves the utility model adopts is: circular fluid bed high temperature ash pyrolysis biomass-making oil device, comprise circular fluid bed, cyclonic separator A, high temperature is got apparatus for ash, biomass powder storehouse, the biomass entrance lock, helixes feed equipment, pyrolysis reactor, cyclonic separator B, the Venturi spray cooling device, fluid collection device, solid biologic charcoal and circulating ash send-back device, water circulating pump, suction fan, it is characterized in that this device is provided with pyrolysis reactor, the top of pyrolysis reactor is got apparatus for ash by high temperature respectively and is connected with the bottom straight length of cyclonic separator A, add feed bin by the connection of adjustable speed helixes feed equipment, the top outlet of pyrolysis reactor is connected with cyclonic separator B, and the outlet at bottom of pyrolysis reactor is provided with solid biologic charcoal and circulating ash send-back device.Be provided with baffle in the pyrolysis reactor.The solid biologic charcoal is connected with the grey backpass ductwork of circulating ash send-back device with cyclonic separator B lower part outlet and circular fluid bed.The bottom of biological feed bin is provided with air-lock device.
The heat that biomass pyrolytic needs is provided by the accumulation of heat of circulating fluidized bed high temperature ash, by the direct contact heat transfer of high temperature ash with biomass material, can realize being rapidly heated and pyrolysis of biomass, make biomass discharge gas, the circulating ash of solid product and release of heat is then returned boiler by the spiral send-back device of reactor bottom.Gas enters cyclonic separator B and carries out gas solid separation subsequently, the solid loopback boiler after the separation, and clean gas then enters the rapid condensation device and carries out quick cooling, and gained liquid is bio oil, and noncondensable gas is then as combustion gas loopback boiler.So just realized effective utilization of pyrolysis product-gas, solid and liquid.
Advantage of the present utility model:
(1) can under the condition that does not influence the normal operation of circular fluid bed, utilize the heat thermo-cracking biomass material of circulating ash to produce the bio oil product.
(2) pyrolysis product does not coagulate inflammable gas and the directly loopback boiler combustion of solid biologic charcoal, substitutes the part fossil oil, save energy.
(3) high temperature ash and biomass powder enter in the pyrolysis reactor by helixes feed equipment respectively, can control the feeding coal of the two respectively, and then can regulate pyrolytic reaction and be in optimum state.
(4) complete assembly does not have complex component, and is simple, is easy to amplify.
Description of drawings
Accompanying drawing is a structural representation of the present utility model.
Among the figure, 1, circular fluid bed, 2, cyclonic separator A, 3, high temperature is got apparatus for ash, and 4, biomass powder storehouse, 5, the biomass entrance lock, 6, helixes feed equipment, 7, pyrolysis reactor, 8, cyclonic separator B, 9, the Venturi spray cooling device, 10, fluid collection device, 11, solid biologic charcoal and circulating ash send-back device, 12, water circulating pump, 13, suction fan.
Embodiment
Embodiment: a kind of circulating fluidized bed high temperature ash pyrolysis biomass-making oil device, comprise with lower member: circular fluid bed 1, cyclonic separator A2, high temperature is got apparatus for ash 3, biomass powder storehouse 4, biomass entrance lock 5, helixes feed equipment 6, pyrolysis reactor 7, cyclonic separator B8, Venturi spray cooling device 9, fluid collection device 10, solid biologic charcoal and circulating ash send-back device 11, water circulating pump 12, suction fan 13 is formed, circular fluid bed 1 outlet links to each other with cyclonic separator A2, cyclonic separator A2 bottom straight length is got apparatus for ash 3 with high temperature and is linked to each other, and high temperature is got apparatus for ash 3 outlets and linked to each other with pyrolysis reactor 7 tops; After crushed biomass powder is connected to pyrolysis reactor 7 tops after by biomass entrance lock 5 and adjustable speed helixes feed equipment 6 in the biomass powder storehouse 4.The outlet of pyrolysis reactor 7 tops links to each other with cyclonic separator B8, and the pneumatic outlet of cyclonic separator B8 is connected with Venturi spray cooling device 9, and 9 outlets of Venturi spray cooling device are connected to fluid collection device 10 tops.Fluid collection device 10 links to each other with Venturi spray cooling device 9 by water circulating pump 12, and the escape pipe on fluid collection device 10 tops then links to each other with circulation fluidized bed boiler 1 behind suction fan 13.The bottom material outlet of pyrolysis reactor 7 bottom material outlets and cyclonic separator B8 links to each other with circulating ash send-back device 11 with the solid biologic charcoal, and 11 outlets of circulating ash send-back device link to each other with the grey loopback pipeline of circular fluid bed 1.
High temperature is got the straight length of apparatus for ash 3 in cyclonic separator A2 bottom, opens a bypass so that most of circulating ash turns back in the boiler at this.Being installed in high temperature on the straight length gets material envelope that apparatus for ash 3 tops guarantee to have certain altitude and collaborates preventing.Because circulating ash has higher temperature (800-900 ℃), gets the works better of apparatus for ash 3 for guaranteeing high temperature, rotation axis carries out water-cooled, the work of driven by motor chain drive rotation axis.
The characteristics of biomass powder e Foerderanlage are after the biomass powder is by biomass entrance lock 5 and helixes feed equipment 6, enter in the pyrolysis reactor 7, made full use of the width of reactor, increased reaction area, improve heat transfer efficiency, shortened the pyrolytic reaction time.Pyrolysis reactor 7 inside are equipped with baffle.For preventing that local overheating from appearring in auger exit easily, cause the biomass powder to cause transportation not smooth because of being subjected to the fine and close aggregate of thermosetting, auger adopts the water-cooled axle.
High temperature ash and biomass powder enter in the pyrolysis reactor by helixes feed equipment respectively, can control the feeding coal of the two respectively, and then can regulate pyrolytic reaction and be in optimum regime.
Claims (4)
1. circular fluid bed high temperature ash pyrolysis biomass-making oil device, comprise circular fluid bed, cyclonic separator, high temperature is got apparatus for ash, biomass powder storehouse, the biomass entrance lock, helixes feed equipment, pyrolysis reactor, cyclonic separator, the Venturi spray cooling device, fluid collection device, solid biologic charcoal and circulating ash send-back device, water circulating pump, suction fan, it is characterized in that, apparatus for ash is got by high temperature respectively in the top of pyrolysis reactor to be connected with the bottom straight length of cyclonic separator A, add feed bin by the connection of adjustable speed helixes feed equipment, the top outlet of pyrolysis reactor is connected with cyclonic separator B, and the outlet at bottom of pyrolysis reactor is provided with solid biologic charcoal and circulating ash send-back device.
2. circular fluid bed high temperature ash pyrolysis biomass-making oil device according to claim 1 is characterized in that, is provided with baffle in the pyrolysis reactor.
3. circular fluid bed high temperature ash pyrolysis biomass-making oil device according to claim 1 is characterized in that the solid biologic charcoal is connected with the grey backpass ductwork of circulating ash send-back device with cyclonic separator B lower part outlet and circular fluid bed.
4. circular fluid bed high temperature ash pyrolysis biomass-making oil device according to claim 1, its feature exists, and is provided with air-lock device in the bottom of biological feed bin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620009199 CN200996005Y (en) | 2006-11-06 | 2006-11-06 | Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620009199 CN200996005Y (en) | 2006-11-06 | 2006-11-06 | Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200996005Y true CN200996005Y (en) | 2007-12-26 |
Family
ID=38994436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620009199 Expired - Fee Related CN200996005Y (en) | 2006-11-06 | 2006-11-06 | Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200996005Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101845314A (en) * | 2009-11-02 | 2010-09-29 | 郑州汇绿科技有限公司 | Novel pyrolytic system for producing bio-oil by forestry and agricultural residues |
| CN102061184A (en) * | 2010-09-01 | 2011-05-18 | 安徽易能生物能源有限公司 | Method for designing unpowered solid thermal carrier pyrolytic technique |
| WO2014048328A1 (en) * | 2012-09-25 | 2014-04-03 | 中国东方电气集团有限公司 | Dual-bed system to prevent the pollution of boiler heating surface |
| WO2014048329A1 (en) * | 2012-09-25 | 2014-04-03 | 中国东方电气集团有限公司 | System for solving high-sodium coal combustion contamination by using pyrolysis-combustion dual-bed |
| CN105001895A (en) * | 2015-07-17 | 2015-10-28 | 广州迪森热能技术股份有限公司 | Bio-oil preparation system |
| CN105733627A (en) * | 2016-04-01 | 2016-07-06 | 华中科技大学 | Biomass rapid pyrolysis and coal-fired boiler coupling system |
-
2006
- 2006-11-06 CN CN 200620009199 patent/CN200996005Y/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101845314A (en) * | 2009-11-02 | 2010-09-29 | 郑州汇绿科技有限公司 | Novel pyrolytic system for producing bio-oil by forestry and agricultural residues |
| CN102061184A (en) * | 2010-09-01 | 2011-05-18 | 安徽易能生物能源有限公司 | Method for designing unpowered solid thermal carrier pyrolytic technique |
| CN102061184B (en) * | 2010-09-01 | 2013-07-17 | 安徽易能生物能源有限公司 | Method for designing unpowered solid thermal carrier pyrolytic technique |
| WO2014048328A1 (en) * | 2012-09-25 | 2014-04-03 | 中国东方电气集团有限公司 | Dual-bed system to prevent the pollution of boiler heating surface |
| WO2014048329A1 (en) * | 2012-09-25 | 2014-04-03 | 中国东方电气集团有限公司 | System for solving high-sodium coal combustion contamination by using pyrolysis-combustion dual-bed |
| US9927119B2 (en) | 2012-09-25 | 2018-03-27 | Dongfang Electric Corporation | Dual-bed system for preventing boiler heating surface from being contaminated |
| US9989247B2 (en) | 2012-09-25 | 2018-06-05 | Dongfang Electric Corporation | Pyrolysis-combustion dual-bed system for eliminating contamination by combustion of high-sodium coal |
| CN105001895A (en) * | 2015-07-17 | 2015-10-28 | 广州迪森热能技术股份有限公司 | Bio-oil preparation system |
| CN105733627A (en) * | 2016-04-01 | 2016-07-06 | 华中科技大学 | Biomass rapid pyrolysis and coal-fired boiler coupling system |
| CN105733627B (en) * | 2016-04-01 | 2018-09-21 | 华中科技大学 | A kind of biomass fast pyrogenation and coal-burning boiler coupled system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101624531B (en) | Device for preparing bio-oil by utilizing biomass spouted fluidized bed through pyrolysis and fractional condensation | |
| CN201473491U (en) | Biomass fast thermal decomposition device | |
| CN200996005Y (en) | Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass | |
| CN101225315B (en) | Method and device for biomass compound gasification | |
| CN202530040U (en) | Continuous biomass dry-distillation carbonization apparatus | |
| CN105586095B (en) | A kind of biomass microwave pyrolytic gasification reaction unit | |
| CN201593035U (en) | Gas production device using spiral dry distillation and decomposition of biomass | |
| CN100340637C (en) | Mobile biomass liquefaction system | |
| CN106939171A (en) | Biomass downlink cycle bed millisecond pyrolysis liquefaction technique | |
| CN106256877B (en) | A kind of carbonizing and gasifying composite furnace | |
| CN103756731A (en) | Interactive cyclic solid fuel gasification device with double fluidized beds and method | |
| CN102533296A (en) | Oil shale rotary kiln dry distillation and circulating fluidized bed combustion process | |
| CN102786990A (en) | Biomass and coal fluidized bed co-gasification method | |
| CN105950195A (en) | Cocurrent downward circulating fluidized bed millisecond pyrolysis and liquefaction technology for biomass | |
| CN101885975A (en) | Device and process for bio-oil and carbon powder coproduction | |
| CN108342211A (en) | Novel biomass pyrolysis comprehensive utilization process and system | |
| CN104479719A (en) | Movable device and method for preparing liquid fuel by virtue of straw pyrolysis | |
| CN103409156B (en) | Heat carrier destructive distillation system for coal and method thereof | |
| CN202808710U (en) | Ore catalyst bed biomass flash pyrolysis oil production device | |
| CN101481619A (en) | Self-mixing downflow fluidized bed rapid pyrolysis process for solid organics | |
| CN105885951B (en) | A kind of double bed coupling pyrolysis gasification system directly or indirectly heating combination | |
| CN101845328B (en) | Biomass combined gasification equipment | |
| CN106190214A (en) | Biomass downlink cycle bed millisecond pyrolysis liquefaction device | |
| CN202440467U (en) | Self-heating biomass flash pyrolysis liquefying device | |
| CN200996006Y (en) | Oil producer of circulation fluidized bed boiler by high-temperature ash pyrolytic biomass |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071226 Termination date: 20101106 |