CN105802645A - Continuous carbonizing device - Google Patents
Continuous carbonizing device Download PDFInfo
- Publication number
- CN105802645A CN105802645A CN201610279758.2A CN201610279758A CN105802645A CN 105802645 A CN105802645 A CN 105802645A CN 201610279758 A CN201610279758 A CN 201610279758A CN 105802645 A CN105802645 A CN 105802645A
- Authority
- CN
- China
- Prior art keywords
- hothouse
- drying chamber
- combustor
- carbonizing device
- conveyer belt
- 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.)
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Classifications
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- 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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- 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
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a continuous carbonizing device. The continuous carbonizing device comprises a first drying chamber, a second drying chamber and a third drying chamber which are sequentially ranged from top to bottom, wherein the lower side of the third drying chamber is connected with a carbonization furnace; the bottom of the carbonization furnace is provided with a combustion chamber; one end of each of the first drying chamber, the second drying chamber and the third drying chamber is communicated with a convergent flow chamber; a roller is arranged in the first drying chamber; one end of the roller is communicated with the convergent flow chamber, and the other end of the roller is connected with a feeding hopper; a second conveyor belt is arranged in the second drying chamber; a third conveyor belt is arranged in the third drying chamber; a plurality of combustion heads connected to a gas merging tank are arranged on the combustion chamber; the gas combining tank is also connected with the combustion chamber through a recovery pipe. The continuous carbonizing device has the advantages that raw materials can be efficiently and continuously dried and carbonized; in addition, the energy is saved; the environment is protected.
Description
Technical field
The present invention relates to a kind of carbonizing device continuously, belong to charcoal processing technical field.
Background technology
" straw and coal " is exactly the charcoal often said, refers to and utilizes carbonizing device with the corn straw in rural area, corn cob, branch, leaves, sawdust etc. for raw material, and after pulverizing, pressurization, density molding replace traditional coal, and it is a kind of emerging fuel.But current most of carbonizing devices are not cannot be carried out continuous drying, carbonization, it is simply that needing a very long streamline to carry out charcoal processing operation again after raw material is dried, under production efficiency, and energy resource consumption is bigger.
Summary of the invention
It is an object of the invention to, it is provided that a kind of carbonizing device continuously.Raw material can be carried out continuous drying, carbonization by efficiently, and energy-conserving and environment-protective more.
Technical scheme: carbonizing device continuously, is characterized in: including the first hothouse, secondary drying chamber and the 3rd hothouse that are arranged in order from top to bottom, the 3rd hothouse has been connected below retort, is provided with combustor bottom retort；Described first hothouse, secondary drying chamber and the 3rd hothouse all have one end to be communicated to room of confluxing；Being provided with cylinder in described first hothouse, cylinder one end is communicated to room of confluxing, and the other end is connected to feed hopper；It is respectively equipped with the second conveyer belt and the 3rd conveyer belt in secondary drying chamber and the 3rd hothouse；Described combustor is provided with multiple combustion head being connected to also gas tank, and described and gas tank is connected with combustor also by recovery tube.
In above-mentioned continuous carbonizing device, described 3rd hothouse is communicated to combustor near the one end of room of confluxing by discharge bucket, being provided be distributed up and down first in combustor and transmit fire grate and the second transmission fire grate, wherein the second discharge end transmitting fire grate extend out to outside combustor.
In aforesaid continuous carbonizing device, described secondary drying chamber and the 3rd hothouse be not connected with confluxing one end of room is connected to defeated warm-air pipe, and defeated warm-air pipe is connected with aid distributing pipe, and aid distributing pipe is connected with combustor by hot blast collecting pipe.
In aforesaid continuous carbonizing device, the discharge end of described cylinder is connected to the charging aperture of the second conveyer belt by the first deflector chute, and the discharging opening of the second conveyer belt is connected to the charging aperture of the 3rd conveyer belt by the second deflector chute.
In aforesaid continuous carbonizing device, described first hothouse be not connected with confluxing one end of room is provided with dehumidification tube.
Compared with prior art, the present invention utilizes multiple continuous print hothouse to coordinate different load modes, it is possible to making full use of hot blast and carry out continuous drying to raw material, dried raw material can be directly entered retort and carry out carbonization.The present invention rational deployment by total, it is possible to make full use of the energy, and the wood gas produced in carbonization process can be recycled, not only do not result in air pollution, and take full advantage of the intermediate product in carbonization process.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is further illustrated, but is not intended as the foundation to present invention restriction.
Embodiment.Continuous carbonizing device, as shown in Figure 1: including the first hothouse 1.1, secondary drying chamber 1.2 and the 3rd hothouse 1.3 that are arranged in order from top to bottom, the 3rd hothouse 1.3 has been connected below retort 12, is provided with combustor 13 bottom retort 12；Described first hothouse 1.1, secondary drying chamber 1.2 and the 3rd hothouse 1.3 all have one end to be communicated to room 2 of confluxing；Being provided with cylinder 3 in described first hothouse 1.1, cylinder 3 one end is communicated to room 2 of confluxing, and the other end is connected to feed hopper 4；The second conveyer belt 7 and the 3rd conveyer belt 8 it is respectively equipped with in secondary drying chamber 1.2 and the 3rd hothouse 1.3；Described combustor 13 is provided with multiple combustion head 17 being connected to also gas tank 16, and described and gas tank 16 is connected with combustor 13 also by recovery tube 18.Described 3rd hothouse 1.3 is communicated to combustor 13 near the one end of room 2 of confluxing by discharge bucket 11, is provided be distributed up and down first and transmits fire grate 14 and the second transmission fire grate 15 in combustor 13, and wherein the second discharge end transmitting fire grate 15 extend out to outside combustor 13.Described secondary drying chamber 1.2 and the 3rd hothouse 1.3 be not connected with confluxing one end of room 2 is connected to defeated warm-air pipe 10, and defeated warm-air pipe 10 is connected with aid distributing pipe 20, and aid distributing pipe 20 is connected with combustor 13 by hot blast collecting pipe 19.The discharge end of described cylinder 3 is connected to the charging aperture of the second conveyer belt 7 by the first deflector chute 6, and the discharging opening of the second conveyer belt 7 is connected to the charging aperture of the 3rd conveyer belt 8 by the second deflector chute 9.Described first hothouse 1.1 be not connected with confluxing one end of room 2 is provided with dehumidification tube 5.
The operation principle of the present invention: moist raw material enters cylinder from feed hopper, the second conveyer belt of secondary drying chamber is entered after drum turning is dried, the 3rd conveyer belt is entered then as conveyer belt, dried principle is transported in retort and carries out carbonization by the 3rd conveyer belt, and charcoal finished product transmits fire grate and second through first and transmits fire grate output.The high temperature of retort come from bottom combustor, combustor by and gas tank provide combustion gas burn, and in retort produce wood gas return again be recovered to and gas tank in combustion gas one combust, saved the energy.And the hot air temperature of each hothouse need not be too high, the tail gas of combustion furnace therefore can be utilized.The tail gas of combustion furnace flows to secondary drying chamber and the 3rd hothouse by gas-distribution pipe, and the steam that secondary drying chamber and the 3rd hothouse are discharged collaborates to confluxing room, and is reversely delivered to the first hothouse.
Claims (5)
1. continuous carbonizing device, it is characterized in that: include the first hothouse (1.1), secondary drying chamber (1.2) and the 3rd hothouse (1.3) that are arranged in order from top to bottom, 3rd hothouse (1.3) has been connected below retort (12), and retort (12) bottom is provided with combustor (13)；Described first hothouse (1.1), secondary drying chamber (1.2) and the 3rd hothouse (1.3) all have one end to be communicated to room of confluxing (2)；Being provided with cylinder (3) in described first hothouse (1.1), cylinder (3) one end is communicated to room of confluxing (2), and the other end is connected to feed hopper (4)；It is respectively equipped with the second conveyer belt (7) and the 3rd conveyer belt (8) in secondary drying chamber (1.2) and the 3rd hothouse (1.3)；Described combustor (13) is provided with multiple combustion head (17) being connected to also gas tank (16), and described and gas tank (16) is connected with combustor (13) also by recovery tube (18).
2. continuous carbonizing device according to claim 1, it is characterized in that: described 3rd hothouse (1.3) is communicated to combustor (13) near the one end of room (2) of confluxing by discharge bucket (11), being provided be distributed up and down first in combustor (13) and transmit fire grate (14) and the second transmission fire grate (15), wherein the second discharge end transmitting fire grate (15) extend out to combustor (13) outward.
3. continuous carbonizing device according to claim 1, it is characterized in that: described secondary drying chamber (1.2) and the 3rd hothouse (1.3) be not connected with confluxing one end of room (2) is connected to defeated warm-air pipe (10), defeated warm-air pipe (10) is connected with aid distributing pipe (20), and aid distributing pipe (20) is connected with combustor (13) by hot blast collecting pipe (19).
4. continuous carbonizing device according to claim 1, it is characterized in that: the discharge end of described cylinder (3) is connected to the charging aperture of the second conveyer belt (7) by the first deflector chute (6), the discharging opening of the second conveyer belt (7) is connected to the charging aperture of the 3rd conveyer belt (8) by the second deflector chute (9).
5. continuous carbonizing device according to claim 1, it is characterised in that: described first hothouse (1.1) be not connected with confluxing one end of room (2) is provided with dehumidification tube (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610279758.2A CN105802645B (en) | 2016-04-28 | 2016-04-28 | Continuous carbonizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610279758.2A CN105802645B (en) | 2016-04-28 | 2016-04-28 | Continuous carbonizing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105802645A true CN105802645A (en) | 2016-07-27 |
| CN105802645B CN105802645B (en) | 2018-05-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610279758.2A Active CN105802645B (en) | 2016-04-28 | 2016-04-28 | Continuous carbonizing device |
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| CN (1) | CN105802645B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108384561A (en) * | 2018-04-11 | 2018-08-10 | 上海升凯新能源开发有限公司 | A kind of biomass pyrolytic control system and method |
| CN116891754A (en) * | 2023-09-11 | 2023-10-17 | 山西大地民基生态环境股份有限公司 | High-speed carbonization device for continuously feeding straws |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2346026C2 (en) * | 2007-04-06 | 2009-02-10 | Общество с ограниченной ответственностью "Альтернативные энергетические системы" | Method of sng and coal char obtaining by pyrolysis reaction of biomass |
| CN204388533U (en) * | 2015-01-05 | 2015-06-10 | 河北旺族饲料集团有限公司 | The drying unit that a kind of pellet is special |
| CN205576023U (en) * | 2016-04-28 | 2016-09-14 | 湖州民强炭业有限公司 | Continuous system charcoal device |
-
2016
- 2016-04-28 CN CN201610279758.2A patent/CN105802645B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2346026C2 (en) * | 2007-04-06 | 2009-02-10 | Общество с ограниченной ответственностью "Альтернативные энергетические системы" | Method of sng and coal char obtaining by pyrolysis reaction of biomass |
| CN204388533U (en) * | 2015-01-05 | 2015-06-10 | 河北旺族饲料集团有限公司 | The drying unit that a kind of pellet is special |
| CN205576023U (en) * | 2016-04-28 | 2016-09-14 | 湖州民强炭业有限公司 | Continuous system charcoal device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108384561A (en) * | 2018-04-11 | 2018-08-10 | 上海升凯新能源开发有限公司 | A kind of biomass pyrolytic control system and method |
| CN116891754A (en) * | 2023-09-11 | 2023-10-17 | 山西大地民基生态环境股份有限公司 | High-speed carbonization device for continuously feeding straws |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105802645B (en) | 2018-05-18 |
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Effective date of registration: 20200730 Address after: 215500 Room 301, building 3, No. 88, Xianshi Road, Changshu high tech Industrial Development Zone, Suzhou City, Jiangsu Province Patentee after: Changshu Zijin Intellectual Property Service Co.,Ltd. Address before: 313016 Zhejiang Province, Huzhou city Nanxun District Qianjin town Simma stem Yang Village tower Patentee before: HUZHOU MINQIANG CARBON INDUSTRY Co.,Ltd. |
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