CN2863799Y - Coal and by-product cogeneration apparatus by using biomass - Google Patents
Coal and by-product cogeneration apparatus by using biomass Download PDFInfo
- Publication number
- CN2863799Y CN2863799Y CNU2005200319460U CN200520031946U CN2863799Y CN 2863799 Y CN2863799 Y CN 2863799Y CN U2005200319460 U CNU2005200319460 U CN U2005200319460U CN 200520031946 U CN200520031946 U CN 200520031946U CN 2863799 Y CN2863799 Y CN 2863799Y
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- Prior art keywords
- oil
- biomass
- vinegar
- gas
- byproduct
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- 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
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Abstract
The utility model relates to a carbonizing machine, especially a coal and by-product cogeneration apparatus by using biomass comprising a retorting carbonization device (1), a covering carbon device (2) and a carbon powder molding device (3). An oil and gas separation condensing device (4) and a gas storage device (6) are increased after the retorting carbonization device (1). An oil vinegar separator (5) is increased after the oil and gas separetion condensing device (4), and an oil storage device (7) and a vinegar storage device (8) are increased after the oil vinegar separator (5). The utility model saves wood and make use of the biomass waste materials as raw materials, can get the wanted carbon without wasting the limited forest resources, which is coincident with the national sustainable development strategies. Besides of the retorting main product carbon, the by-product with utilization value is also get. The utility model has the advantages of reasonable design and a simple structure, and makes good use of the present technology to reduce the cost.
Description
(1) technical field
The utility model relates to a kind of charcoal processing machine, particularly the coproduction setting that the biomass charcoal processing is collected with byproduct.
(2) background technology
The tradition charcoal processing is raw materials used to be based on timber, and the product of acquisition is single charcoal.The inflammable gas that in carbonization of wood process, is produced, wood vinegar, Chang Zuowei wastes such as wood tar oil are by emptying.Along with the enforcement of national sustainable development policy with preserve the ecological environment, further the implementing of the work that prevents erosion, the timber shortage limits the use of day by day and shows especially, and is impossible as the charcoal processing raw material with timber.Traditional charcoal processing technology and emptying byproduct cause the practice of waste and contaminate environment can not continue.
Get charcoal with the dry distillation charring legal system and expanded raw material range, this method can be used the biomass such as the residual branch of straw, trees of farm crop, and the destructive distillation product is mainly biomass charcoal, and byproduct is combustion gas, wood vinegar, wood tar oil etc.It then is a new problem that biomass such as destructive distillation straw also obtain four kinds of products simultaneously.
(3) technology contents
The purpose of this utility model is to provide a kind of biomass charcoal processing and byproduct cogeneration facility.Utilize this equipment not only can obtain, the byproduct that simultaneously can also obtain in the retort process to be produced etc. with the biomass charcoal that destructive distillation obtains as raw material.
In order to realize the utility model purpose, according to following technical scheme.Biomass charcoal processing and byproduct cogeneration facility comprise retorting carbonization device, further increase covering carbon device and carbon powder molding device thereafter.
After retorting carbonization device, increase gas-oil separation condensing works and combustion gas storage facility again.After the gas-oil separation condensing works, increase oil vinegar separator again, further increase Oil container and vinegar storage device behind the oil vinegar separator.
Before described retorting carbonization device, increase biomass processor.Biomass processor is made of raw material pulverizing device and material forming device.
Superiority of the present utility model is:
1. saving timber utilizes the biomass dead meal to be raw material, can obtain required charcoal and not waste the limited forest reserves again, meets the strategy of national sustainable development.
2. when obtaining pyrogenous major product charcoal, can also be had very much and be utilized the byproduct that is worth.
3. reasonable in design, simple in structure, and made full use of prior art to reduce cost.
(4) description of drawings
Accompanying drawing is a structural representation of the present utility model.
(5) embodiment
The utility model concrete structure sees also accompanying drawing.Biomass charcoal processing and byproduct cogeneration facility comprise retorting carbonization device, further increase covering carbon device 2 and carbon powder molding device 3.
After retorting carbonization device 1, increase gas-oil separation condensing works 4 and combustion gas storage facility 6 again.Increase oil vinegar separator 5 after gas-oil separation condensing works 4 again, oil vinegar separator 5 backs further increase Oil container 7 and vinegar storage device 8.
Before retorting carbonization device 1, increase biomass processor 9.Described biomass processor 9 is made of raw material pulverizing device 10 and material forming device 11.
Retorting carbonization device is that biomass briquette is put into dry distillation charring in the charring furnace.The charring furnace of forms such as available tunnel like, drawer type, roller bed type, courtyard formula.Should select for use the temperature in the stove even, good airproof performance, easy to operate, the device of batch production not.Technological temperature is no more than 550 ℃.The device that is adopted in the utility model oneself is developed for us, and the patent No. is 200320113581 tunnel like dry distillation carbonizing furnace.The biomass that enter this device are under the situation of secluding air, and when being heated to more than 250 ℃, elements such as the carbon of composition biomass, hydrogen, oxygen form the gas mixture of hydrocarbon polymer such as multiple complexity such as methane, carbon monoxide, and remaining simple substance is fixed carbon.Temperature is reacted end in the time of 450-550 ℃.
Solid behind the dry distillation charring in the stove is the simple substance charcoal, is sent to carry out trail operation processing in the covering carbon device 2.The mixture of the inflammable gas that biomass material is produced in retort process, wood tar oil, wood vinegar imports and carries out the separation of liquid gas in the condenser.Covering carbon device 2 of the present utility model adopts the cooling of nature steam-type, it is a self heat of utilizing the fresh baked charcoal, wet cloth in the water cooler is heated into vapor state, after producing steam, the condensation but interior pressure of device is increased, original air displacement is gone out,, take away heat and make charcoal obtain cooling simultaneously because steam is excessive.
The gas-liquid condensation separating unit.Be that the mixture of byproduct wood tar oil, wood vinegar and the inflammable gas that will be produced in the dry distillation charring process is introduced in the condenser and cooled off, the liquefaction of tar and acetic acid is separated with inflammable gas and purify.Inflammable gas after the purification is sent into gas storage device, and liquid send next procedure to carry out oil, vinegar separates.This device adopts is that our patent No. is that 01239852 " doing the combined type condensation purifier that wets " and the patent No. are 02228906 " net formula decoking device.This device is the isolated plant of decoking, removal of impurities, gas-liquid separation, utilize different boiling and different specific weight, can separate inflammable gas, wood tar oil, wood vinegar, promptly guaranteed the quality of combustion gas, guarantee that again wood tar oil, wood vinegar etc. obtain effective Separation and Recovery, realize the comprehensive utilization of wood tar oil, wood vinegar, thoroughly eradicated secondary pollution.
Claims (5)
1. biomass charcoal processing and byproduct cogeneration facility comprise retorting carbonization device (1), it is characterized in that further increasing covering carbon device (2) and carbon powder molding device (3).
2. biomass charcoal processing as claimed in claim 1 and byproduct cogeneration facility is characterized in that increasing gas-oil separation condensing works (4) and combustion gas storage facility (6) afterwards again at retorting carbonization device (1).
3. biomass charcoal processing as claimed in claim 2 and byproduct cogeneration facility, it is characterized in that increasing oil vinegar separator (5) afterwards again at gas-oil separation condensing works (4), oil vinegar separator (5) back further increases Oil container (7) and vinegar storage device (8).
4. as claim 1 or 3 described biomass charcoal processing and byproduct cogeneration facility, it is characterized in that increasing biomass processor (9) before at retorting carbonization device (1).
5. biomass charcoal processing as claimed in claim 4 and byproduct cogeneration facility is characterized in that described biomass processor (9) is made of raw material pulverizing device (10) and material forming device (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200319460U CN2863799Y (en) | 2005-09-22 | 2005-09-22 | Coal and by-product cogeneration apparatus by using biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200319460U CN2863799Y (en) | 2005-09-22 | 2005-09-22 | Coal and by-product cogeneration apparatus by using biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2863799Y true CN2863799Y (en) | 2007-01-31 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2005200319460U Expired - Fee Related CN2863799Y (en) | 2005-09-22 | 2005-09-22 | Coal and by-product cogeneration apparatus by using biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2863799Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102020999A (en) * | 2010-12-30 | 2011-04-20 | 天津市树荣生物碳宝科技有限公司 | Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil |
| CN102344835A (en) * | 2011-09-05 | 2012-02-08 | 南京林业大学 | Agriculture and forest biomass secondary process reaction gasification furnace and application thereof |
| CN103571509A (en) * | 2013-11-13 | 2014-02-12 | 绵阳市美日佳日化用品有限责任公司 | Method for rapidly and continuously carbonizing agricultural straws |
| CN108441240A (en) * | 2018-04-02 | 2018-08-24 | 李学斌 | A kind of gasification of biomass production line and biomass gasification method |
-
2005
- 2005-09-22 CN CNU2005200319460U patent/CN2863799Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102020999A (en) * | 2010-12-30 | 2011-04-20 | 天津市树荣生物碳宝科技有限公司 | Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil |
| CN102020999B (en) * | 2010-12-30 | 2013-08-07 | 天津市树荣生物碳宝科技有限公司 | Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil |
| CN102344835A (en) * | 2011-09-05 | 2012-02-08 | 南京林业大学 | Agriculture and forest biomass secondary process reaction gasification furnace and application thereof |
| CN102344835B (en) * | 2011-09-05 | 2013-05-15 | 南京林业大学 | Agriculture and forest biomass secondary process reaction gasification furnace |
| CN103571509A (en) * | 2013-11-13 | 2014-02-12 | 绵阳市美日佳日化用品有限责任公司 | Method for rapidly and continuously carbonizing agricultural straws |
| CN108441240A (en) * | 2018-04-02 | 2018-08-24 | 李学斌 | A kind of gasification of biomass production line and biomass gasification method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHENGZHOU RESEARCH INSTITUTE OF BIOMASS ENERGY & Free format text: FORMER OWNER: LI HAITAO Effective date: 20080919 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20080919 Address after: Room 508, building 174, Dongming Road, Zhengzhou Road, Henan Province, China: 450008 Patentee after: ZHENGZHOU SHENGRUN BIOMASS ENERGY AND CHEMICAL RESEARCH INSTITUTE Address before: Room 174, No. 505, Dongming Road, Zhengzhou, Henan Province, China: 450004 Patentee before: Li Haitao |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070131 Termination date: 20100922 |