CN106635087A - Biomass carbonization pretreatment process - Google Patents
Biomass carbonization pretreatment process Download PDFInfo
- Publication number
- CN106635087A CN106635087A CN201611116760.4A CN201611116760A CN106635087A CN 106635087 A CN106635087 A CN 106635087A CN 201611116760 A CN201611116760 A CN 201611116760A CN 106635087 A CN106635087 A CN 106635087A
- Authority
- CN
- China
- Prior art keywords
- biomass
- carbonization
- pyrolysis
- vapor
- pretreatment process
- 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
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Classifications
-
- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
-
- 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
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
- C10B57/10—Drying
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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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The invention discloses a biomass carbonization pretreatment process, which comprises a step of heating biomass at a temperature of 270 to 280 DEG C to dispel the water steam. The biomass carbonization pretreatment has the advantages that before pyrolysis, biomass is pre-heated to remove water in biomass in advance, the carbonization effect in pyrolysis is improved, the pyrolysis carbonization effect is enhanced, the discharged water is condensed, the environment is not polluted, and raw material drying equipment is not needed.
Description
Technical field
The present invention relates to charring process field, especially a kind of biomass carbonated preprocessing process.
Background technology
Biomass can produce many by-products, such as coal gas, tar in carbonization process.Need to make in carbonization process simultaneously
Substantial amounts of heat is used, high-temperature retorting (about 900~1100 DEG C), medium temperature carbonization (about 660~750 DEG C) can be divided into and low temperature distillation is (about
500~580 DEG C).Which type of pyrolysis temperature selected actually in actual production, because when, because of ground, because of product structure, because of life
Depending on producing purpose, the control of pyrolysis temperature can be adjusted by switch board.
The content of the invention
The present invention is directed to the deficiencies in the prior art, proposes a kind of biomass carbonated preprocessing process, easy to operate, carbonization effect
It is really good.
In order to realize foregoing invention purpose, the present invention provides technical scheme below:A kind of biomass carbonated preprocessing process,
Including procedure below:By biomass in 270~280 DEG C of heating, vapor is discharged.
Further, the vapor to discharging carries out condensation process, obtains condensed water.
If due to containing large quantity of moisture in biomass, during pyrolysis charring, the quality and yield of charcoal can be affected, while secondary
Product species can roll up, and cause the difficulty that reclaims and classify.
Compared with prior art, the present invention has advantages below:Biomass to being pyrolyzed carry out prior the pre-heat treatment, discharge
Moisture in biomass, improves pyrolysis charring effect, and the moisture to discharging carries out condensation process, free from environmental pollution and be not required to another
It is equipped with raw material drying apparatus.
Specific embodiment
Describe the present invention with reference to embodiment, the description of this part be only it is exemplary and explanatory, no
Reply protection scope of the present invention has any restriction effect.
Embodiment 1
A kind of biomass carbonated preprocessing process, including procedure below:By biomass in 270 DEG C of heating, vapor is discharged.
Further, the vapor to discharging carries out condensation process, obtains condensed water.
Embodiment 2
A kind of biomass carbonated preprocessing process, including procedure below:By biomass in 280 DEG C of heating, vapor is discharged.
Vapor to discharging carries out condensation process, obtains condensed water.
Embodiment 3
A kind of biomass carbonated preprocessing process, including procedure below:By biomass in 275 DEG C of heating, vapor is discharged.
Vapor to discharging carries out condensation process, obtains condensed water.
The above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications also should
It is considered as protection scope of the present invention.
Claims (2)
1. a kind of biomass carbonated preprocessing process, it is characterised in that:Including procedure below:Biomass are added at 270~280 DEG C
Heat, discharges vapor.
2. as claimed in claim 1 biomass carbonated preprocessing process, it is characterised in that:Vapor to discharging is carried out at condensation
Reason, obtains condensed water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611116760.4A CN106635087A (en) | 2016-12-07 | 2016-12-07 | Biomass carbonization pretreatment process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611116760.4A CN106635087A (en) | 2016-12-07 | 2016-12-07 | Biomass carbonization pretreatment process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106635087A true CN106635087A (en) | 2017-05-10 |
Family
ID=58818671
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611116760.4A Pending CN106635087A (en) | 2016-12-07 | 2016-12-07 | Biomass carbonization pretreatment process |
Country Status (1)
Country | Link |
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CN (1) | CN106635087A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109248688A (en) * | 2018-10-26 | 2019-01-22 | 山东省科学院能源研究所 | A method of coal-biomass carbon production base NOx occlusion reduction catalyst is prepared in situ |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101028926A (en) * | 2006-03-03 | 2007-09-05 | 郭梦雄 | Process for producing super-fine high-purity white carbon from rice hull and burning heat |
CN103242869A (en) * | 2013-05-09 | 2013-08-14 | 南京师范大学 | Device and method for pyrolyzing and carbonizing biomass at low temperature by utilizing boiler flue gas |
CN104164243A (en) * | 2014-08-08 | 2014-11-26 | 广东省宜华木业股份有限公司 | Method for producing wood moulded charcoal by virtue of wood machining residues |
-
2016
- 2016-12-07 CN CN201611116760.4A patent/CN106635087A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101028926A (en) * | 2006-03-03 | 2007-09-05 | 郭梦雄 | Process for producing super-fine high-purity white carbon from rice hull and burning heat |
CN103242869A (en) * | 2013-05-09 | 2013-08-14 | 南京师范大学 | Device and method for pyrolyzing and carbonizing biomass at low temperature by utilizing boiler flue gas |
CN104164243A (en) * | 2014-08-08 | 2014-11-26 | 广东省宜华木业股份有限公司 | Method for producing wood moulded charcoal by virtue of wood machining residues |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109248688A (en) * | 2018-10-26 | 2019-01-22 | 山东省科学院能源研究所 | A method of coal-biomass carbon production base NOx occlusion reduction catalyst is prepared in situ |
CN109248688B (en) * | 2018-10-26 | 2021-03-02 | 山东省科学院能源研究所 | Method for in-situ preparation of carbon-based NOx adsorption reduction catalyst from coal-biomass |
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Legal Events
Date | Code | Title | Description |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170510 |