CN110885691A - Biomass continuous carbonization system - Google Patents
Biomass continuous carbonization system Download PDFInfo
- Publication number
- CN110885691A CN110885691A CN201811057457.0A CN201811057457A CN110885691A CN 110885691 A CN110885691 A CN 110885691A CN 201811057457 A CN201811057457 A CN 201811057457A CN 110885691 A CN110885691 A CN 110885691A
- Authority
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- China
- Prior art keywords
- kiln
- carbonization
- drying
- combustion chamber
- biomass
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- 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
- 238000003763 carbonization Methods 0.000 title claims abstract description 54
- 239000002028 Biomass Substances 0.000 title claims abstract description 30
- 238000001035 drying Methods 0.000 claims abstract description 41
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 17
- 238000000746 purification Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000428 dust Substances 0.000 claims description 16
- 238000000926 separation method Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 3
- 230000030279 gene silencing Effects 0.000 claims 3
- 239000000446 fuel Substances 0.000 abstract description 7
- 238000002309 gasification Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 15
- 238000003860 storage Methods 0.000 description 7
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 239000010903 husk Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
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
-
- 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
-
- 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)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a biomass continuous carbonization system which comprises a drying kiln, a gasification furnace and a carbonization kiln, wherein the drying kiln provides dried biomass for the carbonization kiln, the gasification furnace provides preheated combustible gas for the carbonization kiln, a combustion chamber for preheating the drying kiln is arranged outside the drying kiln, the top of the carbonization kiln is communicated with the drying kiln and the combustion chamber through a hot gas pipeline, the top of the carbonization kiln is communicated to a heating furnace end of the carbonization kiln through a gas purification system, and a dust-free conveying system is arranged between the drying kiln and the carbonization kiln. According to the invention, the biomass with the water content of more than 30% can be carbonized without adding other drying fuels, and the materials can be dried, so that other fuels are saved, and the self-circulation of carbonization energy is realized; not only greatly facilitates the biomass carbonization operation, but also facilitates the industrialization, and the generated economic benefit is considerable.
Description
Technical Field
The invention relates to the technical field of biomass fuels, in particular to a biomass continuous carbonization system.
Background
The method for preparing carbon by utilizing biomass wastes such as straws, rice husks and sawdust is a new technology which is developed in recent years. However, these biomass wastes come from nature or industrial and agricultural production, generally contain a certain amount of water, and the water content is not equal to 20% -40%, which brings a fatal influence to the biomass continuous carbonization, because the current biomass continuous carbonization equipment can only carbonize the biomass with the water content below 15%, and a drying device adopting electric energy or other fuels as a heat source needs to be additionally added to pre-dry the biomass, so that the production process is complicated, and the production cost is greatly increased, so that the biomass carbonization plants which are hardly successful in the whole country are not available so far.
Disclosure of Invention
In order to solve the problems, the invention provides a continuous carbonization system which can carbonize biomass with water content of more than 30% without adding drying fuel.
The utility model provides a continuous carbomorphism system of living beings, includes drying kiln, gasifier, carbomorphism kiln, drying kiln does carbonization kiln provides the living beings after the drying, the gasifier does carbonization kiln provides preheating combustible gas, drying kiln outside is furnished with the combustion chamber who preheats for it, carbomorphism kiln top passes through the steam pipeline intercommunication drying kiln with the combustion chamber, carbomorphism kiln top pass through gas clean system intercommunication extremely carbonization kiln furnace end, drying kiln with be equipped with dustless conveying system between the carbonization kiln.
Furthermore, the combustion chamber is provided with an auxiliary combustion chamber, and the top of the carbonization kiln is communicated with the auxiliary combustion chamber through a gas pipeline.
Further, the gas purification system comprises a primary coarse purification tower, a secondary coarse purification tower, a cooling tower, a gas-water separation tower, a separation tank and a purification tower in sequence.
Further, dustless conveying system mainly includes high-power fan, prestores the storage bucket, once whirlwind dust remover, secondary whirlwind dust remover, auger conveyer, the dry kiln discharge gate intercommunication the storage bucket prestores, prestore the storage bucket and connect high-power fan, the material is sent into once whirlwind dust remover feed inlet by the malleation, once whirlwind dust remover discharge gate is connected secondary whirlwind dust remover feed inlet, the secondary whirlwind dust remover discharge gate is connected through the feed cylinder auger conveyer, auger conveyer discharge end inserts the carbomorphism kiln feed inlet.
Further, high-power fan sets up in the amortization room, the amortization room is equipped with air intake, air outlet, supplies the door of operation personnel business turn over, the top and the lower part in amortization room all are equipped with the muffler.
The invention has the beneficial effects that: the biomass with the water content of more than 30% can be carbonized without adding other drying fuels, and the material drying can be realized, other fuels are saved, and the self-circulation of carbonization energy is realized; not only greatly facilitates the biomass carbonization operation, but also facilitates the industrialization, and the generated economic benefit is considerable.
Drawings
FIG. 1 is a schematic diagram of a continuous biomass carbonization system;
FIG. 2 is a schematic view of a dust free conveyor system.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments. The embodiments of the present invention have been presented for purposes of illustration and description, and are not intended to be exhaustive or limited to the invention in the form disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to best explain the principles of the invention and the practical application, and to enable others of ordinary skill in the art to understand the invention for various embodiments with various modifications as are suited to the particular use contemplated.
Example 1
A biomass continuous carbonization system, as shown in fig. 1 and 2, comprising a drying kiln 1, a gasification furnace (not shown in the figure) and a carbonization kiln 2, wherein the drying kiln 1 provides dried biomass for the carbonization kiln 2, the gasification furnace provides preheated combustible gas for the carbonization kiln 2, a combustion chamber 3 for preheating the drying kiln 1 is arranged outside the drying kiln 1, and the top of the carbonization kiln 2 is communicated with the drying kiln 1 and the combustion chamber 3 through a hot gas pipeline 4; a dust-free conveying system is arranged between the drying kiln 1 and the carbonization kiln 2.
During carbonization operation, firstly, combustible materials such as wood and the like are ignited in a combustion chamber, a drying kiln is preheated, and when the temperature of the drying kiln reaches 100 ℃, the drying kiln starts to be charged; meanwhile, dry biomass (such as rice husks and the like) is ignited in the gasification furnace, the generated combustible gas enters the carbonization kiln for combustion, when the temperature in the carbonization kiln reaches 600 ℃, the drying kiln also starts to produce biomass with the water content of below 15%, and the biomass is conveyed to a feeding hole of the carbonization kiln through a dust-free conveying system.
The top of the carbonization kiln 2 sequentially passes through a fuel gas purification system consisting of a primary coarse purification tower, a secondary coarse purification tower, a cooling tower, a gas-water separation tower, a separation tank and a purification tower, and finally flows back to the head of the carbonization kiln to be ignited, and the gasification furnace is closed after normal combustion. Here, the connection relationship between the devices of the gas purification system is common knowledge in the art, and will not be described in detail herein.
Then, opening a hot gas pipeline valve to enable heat generated by the carbonization kiln to enter the drying kiln through a hot gas pipeline; then, the combustible gas that the carbomorphism kiln produced still can have a large amount of residuals except supplying self burning, consequently, combustion chamber 3 is furnished with auxiliary combustion chamber 6, 2 tops of carbomorphism kiln are passed through gas pipeline 7 intercommunication auxiliary combustion chamber 6 opens gas pipeline valve, lets combustible gas get into the burning of auxiliary combustion chamber, treats under backward flow steam and the gas combined action, and when the temperature of drying kiln reached the stoving demand, main combustion chamber stop work.
To this end, a complete biomass continuous carbonization system is formed.
The biomass produced from the drying kiln is prepared by mixing the material and water vapor, and the water vapor needs to be discharged, and the dried material is sent into the carbonization kiln.
In this embodiment, the dust-free conveying system mainly includes a high-power fan (not shown in the figure), a pre-storage bin 501, a primary cyclone 502, a secondary cyclone 503 and an auger conveyor 504, the discharge port of the drying kiln 1 is communicated with the pre-storage bin 501, the pre-storage bin 501 is connected with the high-power fan, materials are sent into the feed port of the primary cyclone 502 by positive pressure, the discharge port of the primary cyclone 502 is connected with the feed port of the secondary cyclone 503, the discharge port of the secondary cyclone 503 is connected with the auger conveyor 504 through a discharge barrel 505, and the discharge end of the auger conveyor 504 is connected with the feed port of the carbonization kiln 2.
The high-power fan is used for sucking materials from a discharge hole of the drying kiln into a pre-storage material barrel through negative pressure and pressing the materials to a feed hole of the primary cyclone dust collector through positive pressure so as to realize primary material-steam separation; after primary material steam separation, the material enters a secondary cyclone dust collector for secondary material steam separation, and then is conveyed into a carbonization kiln through a screw conveyer.
The high-power fan is used here, and very big noise can be produced certainly, and in this embodiment, the high-power fan sets up in the amortization room, and the storage bucket discharge gate that prestores that is located the amortization outside the amortization room accesss to high-power fan, communicates to primary cyclone from the amortization roof portion. The amortization room is equipped with air intake, air outlet, supplies the door of operation personnel business turn over, the top and the lower part in amortization room all are equipped with the muffler. The wall body of the sound attenuation room is a sound insulation cotton sandwich foam brick wall.
Through the technical scheme, the problems of dust and noise pollution in material conveying from the drying kiln to the carbonization kiln are thoroughly solved.
The drying kiln, the gasification furnace and the carbonization kiln all adopt the existing equipment, and the specific structure is not the key point for protection of the invention.
It is to be understood that the described embodiments are merely a few embodiments of the invention, and not all embodiments. All other embodiments, which can be derived by one of ordinary skill in the art and related arts based on the embodiments of the present invention without any creative effort, shall fall within the protection scope of the present invention.
Claims (5)
1. The utility model provides a continuous carbomorphism system of living beings, includes drying kiln, gasifier, carbomorphism kiln, drying kiln does carbonization kiln provides the living beings after the drying, the gasifier does carbonization kiln provides preheats and uses combustible gas, a serial communication port, drying kiln outside is furnished with carries out the combustion chamber that preheats for it, the carbomorphism kiln top passes through the hot gas pipeline intercommunication drying kiln with the combustion chamber, the carbomorphism kiln top pass through gas clean system intercommunication extremely carbonization kiln furnace end, drying kiln with be equipped with dustless conveying system between the carbonization kiln.
2. The continuous biomass carbonization system as claimed in claim 1, wherein the combustion chamber is provided with an auxiliary combustion chamber, and the top of the carbonization kiln is communicated with the auxiliary combustion chamber through a gas pipeline.
3. The continuous biomass carbonization system as claimed in claim 1, wherein the gas purification system comprises a primary coarse purification tower, a secondary coarse purification tower, a cooling tower, a gas-water separation tower, a separation tank and a purification tower in sequence.
4. The continuous biomass carbonization system of claim 1, wherein the dust-free conveying system mainly comprises a high-power fan, a pre-stored material barrel, a primary cyclone dust collector, a secondary cyclone dust collector and an auger conveyor, the discharge port of the drying kiln is communicated with the pre-stored material barrel, the pre-stored material barrel is connected with the high-power fan, materials are positively conveyed into the feed port of the primary cyclone dust collector, the discharge port of the primary cyclone dust collector is connected with the feed port of the secondary cyclone dust collector, the discharge port of the secondary cyclone dust collector is connected with the auger conveyor through a discharge barrel, and the discharge end of the auger conveyor is connected with the feed port of the carbonization kiln.
5. The continuous biomass carbonization system as claimed in claim 4, wherein the high-power fan is disposed in a silencing room, the silencing room is provided with an air inlet, an air outlet and a door for workers to enter and exit, and silencers are disposed at the top and the lower part of the silencing room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811057457.0A CN110885691A (en) | 2018-09-11 | 2018-09-11 | Biomass continuous carbonization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811057457.0A CN110885691A (en) | 2018-09-11 | 2018-09-11 | Biomass continuous carbonization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110885691A true CN110885691A (en) | 2020-03-17 |
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ID=69745611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811057457.0A Pending CN110885691A (en) | 2018-09-11 | 2018-09-11 | Biomass continuous carbonization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110885691A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115574582A (en) * | 2022-10-28 | 2023-01-06 | 合肥工业大学 | Sectional type biomass continuous drying carbonization equipment |
-
2018
- 2018-09-11 CN CN201811057457.0A patent/CN110885691A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115574582A (en) * | 2022-10-28 | 2023-01-06 | 合肥工业大学 | Sectional type biomass continuous drying carbonization equipment |
| CN115574582B (en) * | 2022-10-28 | 2023-12-19 | 合肥工业大学 | Sectional biomass continuous drying and carbonizing equipment |
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| PB01 | Publication | ||
| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
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Effective date of registration: 20240612 Address after: 434406 Group 12, Zinandi Village, Dongsheng Town, Shishou City, Jingzhou City, Hubei Province (within the yard of Shishou Mingyong Storage Co., Ltd.) (self declared) Applicant after: Hubei Youjiyuan Agricultural Technology Co.,Ltd. Country or region after: China Address before: 317300 Houren Middle Street Village, Baita Town, Xianju County, Taizhou City, Zhejiang Province Applicant before: ZHEJIANG YOUJIYUAN AGRICULTURAL TECHNOLOGY Co.,Ltd. Country or region before: China |