CN105802645B - Continuous carbonizing device - Google Patents
Continuous carbonizing device Download PDFInfo
- Publication number
- CN105802645B CN105802645B CN201610279758.2A CN201610279758A CN105802645B CN 105802645 B CN105802645 B CN 105802645B CN 201610279758 A CN201610279758 A CN 201610279758A CN 105802645 B CN105802645 B CN 105802645B
- Authority
- CN
- China
- Prior art keywords
- hothouse
- combustion chamber
- conveyer belt
- chamber
- roller
- 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
-
- 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
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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 kind of continuous carbonizing devices, including the first hothouse, secondary drying chamber and the 3rd hothouse being arranged in order from top to bottom, retort are connected with below the 3rd hothouse, charing furnace bottom is equipped with combustion chamber;First hothouse, secondary drying chamber and the 3rd hothouse have one end to be connected to confluence room;Roller is equipped in first hothouse, roller one end is connected to confluence room, and the other end is connected with feed hopper;The second conveyer belt and the 3rd conveyer belt are respectively equipped in secondary drying chamber and the 3rd hothouse;The combustion chamber is equipped with multiple combustion heads for being connected to simultaneously gas tank, and described and gas tank is also connected by recovery tube with combustion chamber.The present invention can efficiently carry out raw material continuous drying, charing, and more energy conservation and environmental protection.
Description
Technical field
The present invention relates to a kind of continuous carbonizing devices, belong to charcoal processing technical field.
Background technology
" straw and coal " is exactly the charcoal often said, refer to using carbonizing device with the maize straw in rural area, corncob,
Branch, leaf, sawdust etc. are raw material, after crushing pressurization, density shaping replace traditional coal, it is a kind of emerging
Fuel.But current most of carbonizing devices are not that can not carry out continuous drying, charing, exactly need a very long flowing water
Line carries out charcoal processing process again after raw material is dried, under production efficiency, and energy consumption is larger.
The content of the invention
It is an object of the present invention to provide a kind of continuous carbonizing devices.It can efficiently to raw material carry out it is continuous drying,
Charing, and more energy conservation and environmental protection.
Technical scheme:Continuous carbonizing device, its main feature is that:Including the first drying being arranged in order from top to bottom
Room, secondary drying chamber and the 3rd hothouse, the 3rd hothouse lower section are connected with retort, and charing furnace bottom is equipped with combustion chamber;Institute
Stating the first hothouse, secondary drying chamber and the 3rd hothouse has one end to be connected to confluence room;It is equipped in first hothouse
Roller, roller one end are connected to confluence room, and the other end is connected with feed hopper;It is respectively equipped in secondary drying chamber and the 3rd hothouse
Second conveyer belt and the 3rd conveyer belt;The combustion chamber is equipped with multiple combustion heads for being connected to simultaneously gas tank, and described and gas tank is also
It is connected by recovery tube with combustion chamber.
In above-mentioned continuous carbonizing device, the 3rd hothouse is connected to combustion close to one end of confluence room by discharge bucket
Room is burnt, the first transmission fire grate being distributed up and down and the second transmission fire grate are equipped in combustion chamber, wherein the discharging of the second transmission fire grate
End is extend out to outside combustion chamber.
In foregoing continuous carbonizing device, one end that the secondary drying chamber is not connected with confluence room with the 3rd hothouse connects
There is defeated hot blast pipe, defeated hot blast pipe is connected with aid distributing pipe, and aid distributing pipe is connected by hot wind collecting pipe with combustion chamber.
In foregoing continuous carbonizing device, the discharge end of the roller is connected to the second conveyer belt by the first deflector chute
Feed inlet, the discharge port of the second conveyer belt are connected to the feed inlet of the 3rd conveyer belt by the second deflector chute.
In foregoing continuous carbonizing device, one end that first hothouse is not connected with confluence room is equipped with dehumidification tube.
Compared with prior art, the present invention coordinates different transmission modes using multiple continuous hothouses, can be abundant
Continuous drying to raw material progress using hot wind, dried raw material can be directly entered retort and be carbonized.The present invention passes through whole
The rational deployment of a structure can make full use of the energy, and can recycle the wood gas generated in carbonization process, not only
Air pollution will not be caused, and takes full advantage of the intermediate product in carbonization process.
Description of the drawings
Fig. 1 is the structure diagram of the present invention.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and examples, but be not intended as to the present invention limit according to
According to.
Embodiment.Continuous carbonizing device, as shown in Figure 1:Including be arranged in order from top to bottom the first hothouse 1.1,
Two hothouses 1.2 and the 3rd hothouse 1.3,1.3 lower section of the 3rd hothouse are connected with retort 12, and 12 bottom of retort is equipped with combustion
Burn room 13;First hothouse 1.1,1.2 and the 3rd hothouse 1.3 of secondary drying chamber have one end to be connected to confluence room 2;Institute
It states and roller 3 is equipped in the first hothouse 1.1,3 one end of roller is connected to confluence room 2, and the other end is connected with feed hopper 4;Second is dry
The second conveyer belt 7 and the 3rd conveyer belt 8 are respectively equipped in dry 1.2 and the 3rd hothouse 1.3 of room;The combustion chamber 13 is equipped with more
A combustion head 17 for being connected to simultaneously gas tank 16, described and gas tank 16 are also connected by recovery tube 18 with combustion chamber 13.Described 3rd
Hothouse 1.3 is connected to combustion chamber 13 close to one end of confluence room 2 by discharge bucket 11, is equipped with what is be distributed up and down in combustion chamber 13
First transmission fire grate 14 and second transmits fire grate 15, wherein the discharge end of the second transmission fire grate 15 is extend out to outside combustion chamber 13.Institute
The one end for stating the not connected confluence room 2 of 1.2 and the 3rd hothouse 1.3 of secondary drying chamber is connected with defeated hot blast pipe 10, defeated hot blast pipe 10
It is connected with aid distributing pipe 20, aid distributing pipe 20 is connected by hot wind collecting pipe 19 with combustion chamber 13.The discharge end of the roller 3 passes through
One deflector chute 6 is connected to the feed inlet of the second conveyer belt 7, and the discharge port of the second conveyer belt 7 is connected to by the second deflector chute 9
The feed inlet of three conveyer belts 8.One end of the not connected confluence room 2 of first hothouse 1.1 is equipped with dehumidification tube 5.
The operation principle of the present invention:Moist raw material enters roller from feed hopper, dry into second after drum turning is dried
Second conveyer belt of dry room, then as conveyer belt into the 3rd conveyer belt, dried principle is transported to by the 3rd conveyer belt
It is carbonized in retort, charcoal finished product is by the first transmission fire grate and the second transmission fire grate output.The high temperature of retort comes from
The combustion chamber of bottom, combustion chamber is burnt by simultaneously gas tank offer combustion gas, and the wood gas generated in retort is returned and returned again
It receives and in gas tank with one combust of combustion gas, has saved the energy.And the hot air temperature of each hothouse need not be too high, therefore can
To utilize the tail gas of combustion furnace.The tail gas of combustion furnace is conveyed to secondary drying chamber and the 3rd hothouse by gas-distribution pipe, and second
Hothouse and the hot gas of the 3rd hothouse discharge collaborate to confluence room, and are reversely delivered to the first hothouse.
Claims (3)
1. continuous carbonizing device, it is characterised in that:Including be arranged in order from top to bottom the first hothouse (1.1), second drying
Room (1.2) and the 3rd hothouse (1.3), the 3rd hothouse (1.3) lower section are connected with retort (12), and retort (12) bottom is set
Combuster (13);First hothouse (1.1), secondary drying chamber (1.2) have one end to connect with the 3rd hothouse (1.3)
To confluence room (2);Roller (3) is equipped in first hothouse (1.1), roller (3) one end is connected to confluence room (2), another
End is connected with feed hopper (4);The second conveyer belt (7) and the are respectively equipped in secondary drying chamber (1.2) and the 3rd hothouse (1.3)
Three conveyer belts (8);The combustion chamber (13) is equipped with multiple combustion heads (17) for being connected to simultaneously gas tank (16), described and gas tank
(16) also it is connected by recovery tube (18) with combustion chamber (13);3rd hothouse (1.3) is led to close to one end of confluence room (2)
It crosses discharge bucket (11) and is connected to combustion chamber (13), the first transmission fire grate (14) and second being distributed up and down is equipped in combustion chamber (13)
Fire grate (15) is transmitted, wherein the discharge end of the second transmission fire grate (15) extend out to combustion chamber (13) outside;The secondary drying chamber
(1.2) and one end of not connected confluence room (2) of the 3rd hothouse (1.3) is connected with defeated hot blast pipe (10), defeated hot blast pipe (10) with
Aid distributing pipe (20) is connected, and aid distributing pipe (20) is connected by hot wind collecting pipe (19) with combustion chamber (13).
2. continuous carbonizing device according to claim 1, it is characterised in that:The discharge end of the roller (3) passes through first
Deflector chute (6) is connected to the feed inlet of the second conveyer belt (7), and the discharge port of the second conveyer belt (7) is connected by the second deflector chute (9)
It is connected to the feed inlet of the 3rd conveyer belt (8).
3. continuous carbonizing device according to claim 1, it is characterised in that:First hothouse (1.1) is not connected to be converged
One end of flow chamber (2) is equipped 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 |
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CN105802645A CN105802645A (en) | 2016-07-27 |
CN105802645B true CN105802645B (en) | 2018-05-18 |
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CN201610279758.2A Active CN105802645B (en) | 2016-04-28 | 2016-04-28 | Continuous carbonizing device |
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CN (1) | CN105802645B (en) |
Families Citing this family (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 |
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CN105802645A (en) | 2016-07-27 |
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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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