CN107057771A - A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass - Google Patents
A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass Download PDFInfo
- Publication number
- CN107057771A CN107057771A CN201710501677.7A CN201710501677A CN107057771A CN 107057771 A CN107057771 A CN 107057771A CN 201710501677 A CN201710501677 A CN 201710501677A CN 107057771 A CN107057771 A CN 107057771A
- Authority
- CN
- China
- Prior art keywords
- cyclone
- outlet
- biomass
- separator
- gasification
- 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.)
- Pending
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 26
- 238000002309 gasification Methods 0.000 claims abstract description 32
- 230000008676 import Effects 0.000 claims abstract description 11
- 238000000926 separation method Methods 0.000 claims description 8
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 239000002737 fuel gas Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000000463 material Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 230000003134 recirculating effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
- C10J3/56—Apparatus; Plants
-
- 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
Abstract
A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass, belong to biomass gasification technology field, further increase the gasification efficiency of biomass, it includes gasification furnace, primary cyclone, secondary cyclone and three-stage cyclone separator, burner hearth exhanst gas outlet on the upside of gasification furnace is connected by the import of accelerating sections and primary cyclone, the outlet of primary cyclone bottom is connected by one-level feeding back device with the burner hearth of gasification furnace, outlet at the top of primary cyclone is connected by the import of accelerating sections and secondary cyclone, outlet at the top of secondary cyclone is connected by the import of accelerating sections and three-stage cyclone separator, the outlet of secondary cyclone bottom is connected by two grades of feeding back devices with the burner hearth of gasification furnace;The outlet of three-stage cyclone separator bottom is connected with ash collecting device;The primary cyclone, secondary cyclone and three-stage cyclone separator use circulation whirlwind separator;The present invention is used for gasification of biomass.
Description
Technical field
The invention belongs to biomass gasification technology field, and in particular to a kind of Two-way Cycle Biomass Gasification in Circulating Fluidized Bed
Stove.
Background technology
China is large agricultural country, and biomass energy reserves enrich, occupied an important position in whole energy resource system very much, and
And with good development prospect;Gasification of biomass is to carry out thermochemical study to biomass, produces a kind of skill of fuel gas
Art, is the important channel of biomass utilization, and its principle is that biomass is carried out into imperfect combustion under anoxic conditions, is produced small
CO, H of molecule2、CH4Deng fuel gas, have the advantages that environmental protection and utilization rate are higher;Recirculating fluidized bed is due to stable, just
It is the biomass gasification device generally used at present, but gasification of biomass is carried out using existing recirculating fluidized bed in regulation
When residual carbon content be up to ten to five 12 percent, remaining carbon is higher, and the carbon containing combustible gas scale of construction for showing to produce is lower, i.e. biology
The gasification efficiency of matter is lower, and this programme is researched and developed to further improve the gasification efficiency of biomass;Practice have shown that, it is existing
Circle fluidized-bed gasification furnace residual carbon content it is high the reason for be:The material of only one of which separator separation participates in circulation, circulation times
Rate is relatively low, such as the patent No.(Publication number)For:201120162620.7(CN202072674U)、201320525708.X
(CN203513612U)、201420134817.3(CN203741284U)、201620854679.5(CN205917216U)Institute is public
The gasification furnace opened;Because biomass is very light, one cyclonic separative efficiency is relatively low, in order to improve total efficiency of separation, the patent No.(It is open
Number)For:201310294080.1(CN103320174A)Disclosed gasification furnace adds cyclone separator serial number, but should
Patent is gasified in the dipleg of second separator separation ash the first separator of feeding by first return material valve for separator feeding
It is bulky because biomass ash bulk density is small in stove, cause feed back difficult, be frequently occluded so that the second separator is separated
Ash smooth can not be returned in the first separator dipleg, so as to cause the second separator ineffective;In addition, all of above patent is equal
Using conventional cyclones, the resistance of each separator is for one kPa to 1,500 handkerchiefs, and resistance is excessive, and air-introduced machine power consumption is big
Width increase, performance driving economy declines.
The content of the invention
Followed the invention aims to the gasification efficiency for further improving biomass there is provided a kind of Two-way Cycle biomass
Ring fluidized-bed gasification furnace, its technical scheme is as follows:
A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass, it includes gasification furnace, primary cyclone, two grades of cyclonic separations
Burner hearth exhanst gas outlet on the upside of device and three-stage cyclone separator, gasification furnace is connected by the import of accelerating sections and primary cyclone
Connect, the outlet of primary cyclone bottom is connected by one-level feeding back device with the burner hearth of gasification furnace, primary cyclone
The outlet at top is connected by the import of accelerating sections and secondary cyclone, and the outlet at the top of secondary cyclone is by adding
The import connection of fast section and three-stage cyclone separator, the outlet of secondary cyclone bottom passes through two grades of feeding back devices and gasification
The burner hearth connection of stove, primary cyclone and the secondary cyclone feed back all directly into burner hearth, can guarantee that feed back is smooth;
The primary cyclone, secondary cyclone and three-stage cyclone separator use circulation whirlwind separator, circulation
The structure of formula cyclone separator is CN2577970Y by notification number, and the patent of entitled circumfluent cyclone is disclosed, ring
Streaming cyclone separator uses the structure of circumfluent cyclone, separative efficiency high advantage small with windage, three separation
Handkerchief of total windage about 1,800 of device or so, only about 1/2nd or so of three conventional cyclones.
Beneficial effects of the present invention are:Using double circulation structure, loop sets reasonable, and feed back is smooth, and further reduction flies
Grey carbon left, improves gasification efficiency;The cyclone separator windage used is small, and separative efficiency is high, and through experiment, carbon residue in flying ash is low
In 1 15.
Brief description of the drawings:
Fig. 1 is overall structure diagram of the present invention.
Embodiment:
Reference picture 1, a kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass, it includes gasification furnace 1, primary cyclone 2, two
Level cyclone separator 3 and three-stage cyclone separator 4, the burner hearth exhanst gas outlet of the upside of gasification furnace 1 pass through accelerating sections and one cyclonic
The import connection of separator 2, the outlet of the bottom of primary cyclone 2 is connected by the burner hearth of one-level feeding back device 5 and gasification furnace 1
Logical, the outlet at the top of primary cyclone 2 is connected by accelerating sections with the import of secondary cyclone 3, two grades of whirlwind point
Outlet from the top of device 3 is connected by accelerating sections with the import of three-stage cyclone separator 4, and the bottom of secondary cyclone 3 goes out
Mouth is connected by two grades of feeding back devices 6 with the burner hearth of gasification furnace 1, and primary cyclone 2 and secondary cyclone 3 are all direct
The feed back into burner hearth, can guarantee that feed back is smooth;The primary cyclone 2, secondary cyclone 3 and three-stage cyclone separation
Device 4 uses circulation whirlwind separator, and the structure of circulation whirlwind separator is CN2577970Y by notification number, entitled
The patent of circumfluent cyclone is disclosed, and circulation whirlwind separator uses the structure of circumfluent cyclone, with wind
Small, the high advantage of separative efficiency, the handkerchief of total windage about 1,800 of three separators or so are hindered, only about three conventional whirlwind
/ 2nd or so of separator.
The outlet of the bottom of three-stage cyclone separator 4 is connected with ash collecting device 7, is produced for biomass collection after-flame
Flying dust carries out secondary utilize.
The outlet at the top of three-stage cyclone separator 4 is connected with fuel gas combustion equipment 8, available for combustion power generation or generation steam
Heat supply etc..
Claims (3)
1. a kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass, it comprising gasification furnace (1), primary cyclone (2), two grades
Burner hearth exhanst gas outlet on the upside of cyclone separator (3) and three-stage cyclone separator (4), gasification furnace (1) passes through accelerating sections and one-level
The import connection of cyclone separator (2), the outlet of primary cyclone (2) bottom passes through one-level feeding back device (5) and gasification
The burner hearth connection of stove (1), outlet at the top of primary cyclone (2) is entered by accelerating sections and secondary cyclone (3)
Outlet at the top of mouth connection, secondary cyclone (3) is connected by accelerating sections with the import of three-stage cyclone separator (4), its
It is characterised by that the outlet of secondary cyclone (3) bottom is connected by two grades of feeding back devices (6) with the burner hearth of gasification furnace (1);
The primary cyclone (2), secondary cyclone (3) and three-stage cyclone separator (4) are using circulation whirlwind point
From device, circulation whirlwind separator uses the structure of circumfluent cyclone.
2. a kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass as claimed in claim 1, it is characterised in that three-stage cyclone separation
The outlet of device (4) bottom is connected with ash collecting device (7).
3. a kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass as claimed in claim 1, it is characterised in that three-stage cyclone separation
Outlet at the top of device (4) is connected with fuel gas combustion equipment (8).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710501677.7A CN107057771A (en) | 2017-06-27 | 2017-06-27 | A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass |
Applications Claiming Priority (1)
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CN201710501677.7A CN107057771A (en) | 2017-06-27 | 2017-06-27 | A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass |
Publications (1)
Publication Number | Publication Date |
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CN107057771A true CN107057771A (en) | 2017-08-18 |
Family
ID=59613391
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CN201710501677.7A Pending CN107057771A (en) | 2017-06-27 | 2017-06-27 | A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass |
Country Status (1)
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108410511A (en) * | 2018-04-12 | 2018-08-17 | 哈尔滨理工大学 | A kind of gasification process and device that horizontal Two-way Cycle is biomass fluid bed |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2577970Y (en) * | 2002-10-11 | 2003-10-08 | 青岛化院科技公司 | Spiral-flow cyclone dust collector |
CN101024782A (en) * | 2007-04-06 | 2007-08-29 | 东南大学 | Dense-phase conveying-bed coal pressurizing gasifying apparatus and method |
CN102477314A (en) * | 2010-11-29 | 2012-05-30 | 综合能源有限公司 | Method and apparatus used for recovering and utilizing particles in heterogeneous chemical reactor |
CN103896209A (en) * | 2014-03-07 | 2014-07-02 | 陕西延长石油(集团)有限责任公司 | Method for producing synthesis gas by catalytically reforming coal, natural gas and carbon dioxide |
CN106675658A (en) * | 2016-12-15 | 2017-05-17 | 华北电力大学 | Device and method for high-flux circulating fluidized bed low-rank coal gasifying |
CN206843386U (en) * | 2017-06-27 | 2018-01-05 | 哈尔滨工业大学 | A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass |
-
2017
- 2017-06-27 CN CN201710501677.7A patent/CN107057771A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2577970Y (en) * | 2002-10-11 | 2003-10-08 | 青岛化院科技公司 | Spiral-flow cyclone dust collector |
CN101024782A (en) * | 2007-04-06 | 2007-08-29 | 东南大学 | Dense-phase conveying-bed coal pressurizing gasifying apparatus and method |
CN102477314A (en) * | 2010-11-29 | 2012-05-30 | 综合能源有限公司 | Method and apparatus used for recovering and utilizing particles in heterogeneous chemical reactor |
CN103896209A (en) * | 2014-03-07 | 2014-07-02 | 陕西延长石油(集团)有限责任公司 | Method for producing synthesis gas by catalytically reforming coal, natural gas and carbon dioxide |
CN106675658A (en) * | 2016-12-15 | 2017-05-17 | 华北电力大学 | Device and method for high-flux circulating fluidized bed low-rank coal gasifying |
CN206843386U (en) * | 2017-06-27 | 2018-01-05 | 哈尔滨工业大学 | A kind of Two-way Cycle Circulating Fluidized Bed Gasifier For Biomass |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108410511A (en) * | 2018-04-12 | 2018-08-17 | 哈尔滨理工大学 | A kind of gasification process and device that horizontal Two-way Cycle is biomass fluid bed |
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Application publication date: 20170818 |