CN201339940Y - Organic solid waste material continuous carbonization processing device - Google Patents

Organic solid waste material continuous carbonization processing device Download PDF

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Publication number
CN201339940Y
CN201339940Y CNU2008201801308U CN200820180130U CN201339940Y CN 201339940 Y CN201339940 Y CN 201339940Y CN U2008201801308 U CNU2008201801308 U CN U2008201801308U CN 200820180130 U CN200820180130 U CN 200820180130U CN 201339940 Y CN201339940 Y CN 201339940Y
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CN
China
Prior art keywords
carbonizing
organic solid
pipe
treating apparatus
rotary valve
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.)
Expired - Fee Related
Application number
CNU2008201801308U
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Chinese (zh)
Inventor
李�浩
宁秀珍
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QINGDAO BIOMASS ENVIRONMENTAL PROTECTION TECHNOLOGY CO LTD
Original Assignee
QINGDAO BIOMASS ENVIRONMENTAL PROTECTION TECHNOLOGY CO LTD
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Priority to CNU2008201801308U priority Critical patent/CN201339940Y/en
Application granted granted Critical
Publication of CN201339940Y publication Critical patent/CN201339940Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model aims to provide an organic solid waste material continuous carbonization processing device, which comprises a bracket 1, a hopper 2, a reaction kettle 3 and a cooling pipe 4, wherein the reaction kettle 3 is provided with a ceramic heat preservation layer and an inner lining titanium plate as well as a shell with the inner wall being provided with a heating resistor 31, and the reaction kettle 3 is provided with a gas combustion pipe 5 and a carbonization pipe unit 6, and the gas combustion pipe 5 is provided with an exhausting opening 51 which is arranged outside the reaction kettle 3, and the gas combustion pipe 5 is arranged above the carbonization pipe unit 6 and is communicated with the carbonization pipe unit 6, and the cooling pipe 4 is arranged outside the reaction kettle 3 and is communicated with the tail end of the carbonization pipe unit 6 through a high-temperature rotating valve 7; a single spiral transmission mechanism 8 is respectively arranged inside the carbonization pipe unit 6 and the cooling pipe 4 and is driven by a motor 9 which is arranged on the end; and the hopper 2 is communicated with the upper side on the end of the carbonization pipe unit 6, and the middle part of the hopper 2 is provided with a uni-direction rotating valve 10. The organic solid waste material continuous carbonization processing device can prevent the secondary pollution, and can reduce the processing expense, and can improve the processing speed, and can convert the waste material into a new resource.

Description

A kind of organic solid castoff continuously carbonizing treating apparatus
Technical field
The utility model relates to refuse disposal installation, specifically is a kind of organic solid castoff continuously carbonizing treating apparatus.
Background technology
At present, known organic waste treatment technology based on domestic sludge based on compost, burn, wherein compost is because long processing period, secondary pollution are serious, the minimizing degree is low, burn and then directly discarded object one has been burnt it, not only caused the waste of resource, while energy consumption height, and produce a large amount of carbon dioxide.In existing treatment technology based on same principle (under the hypoxia carry out handled thing heating pyrolysis), general treatment temperature is lower, and adopts combustion gas or fuel oil as mainly thermal source supply, and not only energy consumption height, and Treatment Stability is not high.
The utility model content
Technical problem to be solved in the utility model is to provide a kind of organic solid castoff continuously carbonizing treating apparatus at above-mentioned prior art present situation, continuously carbonizing at organic solid castoff (comprising domestic sludge, fowl and animal excrement, changing food waste, fruits and vegetables discarded object etc.) is handled, can shorten the processing time of organic solid castoff greatly, and be translated into resource and regain utilization.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of organic solid castoff continuously carbonizing treating apparatus, comprise support (1), hopper (2), reactor (3) and cooling pipe (4), described reactor (3) is provided with the housing that ceramic heat-insulation layer and liner titanium plate and inwall are provided with heating resistor (31), reactor (3) is provided with gas combustion pipe (5), with carbonizing tube group (6), gas combustion pipe (5) has the exhaust outlet (51) that is opened in outside the reactor (3), gas combustion pipe (5) is arranged at above the carbonizing tube group (6) and in carbonizing tube group (6) UNICOM, and cooling pipe (4) is arranged at outside the reactor (3) and with carbonizing tube group (6) end and passes through high-temperature rotary valve (7) UNICOM; Be provided with single-screw transmission mechanism (8) in carbonizing tube group (6), the cooling pipe (4), drive by the motor (9) that is arranged at the termination; Hopper (2) and carbonizing tube group (6) termination upside UNICOM, the centre is provided with unidirectional rotary valve (10).
Be provided with spray cooling device in cooling pipe (4) product exit.
Be provided with carbon dioxide and replenish interface between cooling pipe (4) and high-temperature rotary valve (7), this carbon dioxide provides by dioxide bottle (12).
High-temperature rotary valve (7) is connected with drive motors (11).
The utility model use: semiarid organic solid castoff is dropped into hopper, hopper is a twoport, the below of each mouthful is equipped with a rotary valve, can play the effect of secluding air, prevent the pyrolysis gas effusion simultaneously, enter then in the carbonizing tube group in the reactor, these parts are configured to airtight spiral conveying tube, through the continuous propelling of helical blade, finish preheating and carbonization process, (can play the effect of secluding air through high-temperature rotary valve, prevent the pyrolysis gas effusion simultaneously) enter to lower the temperature and manage, the structure of cooling pipe also is that spiral transmits, and after this section flow process, handled thing discharges out of the furnace.In the carbonizing tube group, all can produce pyrolysis gas, enter the after-combustion of gas combustion pipe jointly, produce heat.Because carbonizing tube group and combustion tube all are arranged in same reactor, add the high-efficiency ceramic insulation material, the liner titanium plate.The heat that combustion tube produces is used as the needed heat of carbonization reaction on can well being radiated on the carbonizing tube group.
Need provide initial thermal energy by the heating resistor of reactor setting at initial operating stage, under the proportional situation of the organic matter of charging and water content, this equipment can be finished self-operating, provides extra heat and need not the external world when normally moving.
Single-screw transmission mechanism outside all is furnished with variable-frequency motor, and transfer rate can be regulated automatically;
The cooling tube wall is outer with water cooling plant, and the product exit is furnished with the spray water cooling system, prevents in the time of cooling that product from placing the air spontaneous combustion;
The beneficial effects of the utility model are: relative traditional treatment method, and both avoid secondary pollution, reduced disposal cost, improved processing speed, again discarded object is transformed into a kind of new resource; Energy savings reduces processing cost; Adopt electric energy as the heating supplementary energy, not only make processing procedure stable, controlled, significantly reduce floor space simultaneously, save the soil cost, and improved processing speed.
Description of drawings
Fig. 1, a kind of organic solid castoff continuously carbonizing of the utility model treating apparatus structural representation.
Below in conjunction with accompanying drawing the specific embodiment is described.
The specific embodiment
As shown in Figure 1, a kind of organic solid castoff continuously carbonizing treating apparatus, comprise support 1, hopper 2, reactor 3 and cooling pipe 4, described reactor 3 is provided with the housing that ceramic heat-insulation layer and liner titanium plate and inwall are provided with heating resistor 31, reactor 3 is provided with gas combustion pipe 5 and carbonizing tube group 6, gas combustion pipe 5 has the exhaust outlet 51 that is opened in outside the reactor 3, gas combustion pipe 5 is arranged at carbonizing tube group 6 tops and in carbonizing tube group 6 UNICOMs, cooling pipe 4 is arranged at outside the reactor 3 and with carbonizing tube group 6 ends and passes through high-temperature rotary valve 7 UNICOMs; Be provided with single-screw transmission mechanism 8 in carbonizing tube group 6, the cooling pipe 4, drive by the motor 9 that is arranged at the termination; Hopper 2 and carbonizing tube group 6 termination upside UNICOMs, the centre is provided with unidirectional rotary valve 10.
Be provided with spray cooling device in cooling pipe 4 product exits.
Be provided with carbon dioxide and replenish interface between cooling pipe 4 and high-temperature rotary valve 7, this carbon dioxide provides by dioxide bottle 12.
High-temperature rotary valve 7 is connected with drive motors 11.
The utility model is not limited to above-mentioned preferred forms; anyone can draw other various forms of products under enlightenment of the present invention; no matter but on its shape or structure, do any variation; every have identical with a utility model or akin technical scheme, all within its protection domain.

Claims (9)

1, a kind of organic solid castoff continuously carbonizing treating apparatus, comprise support (1), hopper (2), reactor (3) and cooling pipe (4), it is characterized in that: described reactor (3) is provided with the housing that ceramic heat-insulation layer and liner titanium plate and inwall are provided with heating resistor (31), reactor (3) is provided with gas combustion pipe (5), with carbonizing tube group (6), gas combustion pipe (5) has the exhaust outlet (51) that is opened in outside the reactor (3), gas combustion pipe (5) is arranged at above the carbonizing tube group (6) and in carbonizing tube group (6) UNICOM, and cooling pipe (4) is arranged at outside the reactor (3) and with carbonizing tube group (6) end and passes through high-temperature rotary valve (7) UNICOM; Be provided with single-screw transmission mechanism (8) in carbonizing tube group (6), the cooling pipe (4), drive by the motor (9) that is arranged at the termination; Hopper (2) and carbonizing tube group (6) termination upside UNICOM, the centre is provided with unidirectional rotary valve (10).
2, a kind of organic solid castoff continuously carbonizing treating apparatus according to claim 1 is characterized in that: the outer water cooling tube (41) that puts of cooling pipe (4).
3, a kind of organic solid castoff continuously carbonizing treating apparatus according to claim 1 and 2 is characterized in that: be provided with spray cooling device in cooling pipe (4) product exit.
4, a kind of organic solid castoff continuously carbonizing treating apparatus according to claim 1 is characterized in that: be provided with carbon dioxide and replenish interface between cooling pipe (4) and high-temperature rotary valve (7), this carbon dioxide provides by dioxide bottle (12).
5, a kind of organic solid castoff continuously carbonizing treating apparatus according to claim 3 is characterized in that: be provided with carbon dioxide and replenish interface between cooling pipe (4) and high-temperature rotary valve (7), this carbon dioxide provides by dioxide bottle (12).
6, a kind of organic solid castoff continuously carbonizing treating apparatus according to claim 1 and 2, it is characterized in that: high-temperature rotary valve (7) is connected with drive motors (11).
7, a kind of organic solid castoff continuously carbonizing treating apparatus of stating according to claim 3, it is characterized in that: high-temperature rotary valve (7) is connected with drive motors (11).
8, a kind of organic solid castoff continuously carbonizing treating apparatus of stating according to claim 4, it is characterized in that: high-temperature rotary valve (7) is connected with drive motors (11).
9, a kind of organic solid castoff continuously carbonizing treating apparatus of stating according to claim 5, it is characterized in that: high-temperature rotary valve (7) is connected with drive motors (11).
CNU2008201801308U 2008-11-28 2008-11-28 Organic solid waste material continuous carbonization processing device Expired - Fee Related CN201339940Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201801308U CN201339940Y (en) 2008-11-28 2008-11-28 Organic solid waste material continuous carbonization processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201801308U CN201339940Y (en) 2008-11-28 2008-11-28 Organic solid waste material continuous carbonization processing device

Publications (1)

Publication Number Publication Date
CN201339940Y true CN201339940Y (en) 2009-11-04

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CNU2008201801308U Expired - Fee Related CN201339940Y (en) 2008-11-28 2008-11-28 Organic solid waste material continuous carbonization processing device

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CN (1) CN201339940Y (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102167628A (en) * 2011-01-17 2011-08-31 青岛博迈斯环保技术有限公司 A chicken manure charcoal fertilizer and a production method thereof
CN102173931A (en) * 2011-01-17 2011-09-07 青岛博迈斯环保技术有限公司 Animal manure carbon fertilizer and production method thereof
CN102372414A (en) * 2010-08-25 2012-03-14 青岛博迈斯环保技术有限公司 Method for processing sludge by carbonization and equipment thereof
CN102372413A (en) * 2010-08-25 2012-03-14 青岛博迈斯环保技术有限公司 Equipment for carbonization treatment of sludge and its using method
CN103420553A (en) * 2013-08-31 2013-12-04 山东宏力空调设备有限公司 High-temperature hearth carbonizing furnace
CN104498063A (en) * 2014-11-25 2015-04-08 中南林业科技大学 Compound dry distiller used for manure processing
CN106678813A (en) * 2017-02-13 2017-05-17 杨红波 Device for treating medium and low level waste
CN110655055A (en) * 2018-06-29 2020-01-07 山西贝特瑞新能源科技有限公司 Continuous carbide furnace device of negative electrode material

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102372414A (en) * 2010-08-25 2012-03-14 青岛博迈斯环保技术有限公司 Method for processing sludge by carbonization and equipment thereof
CN102372413A (en) * 2010-08-25 2012-03-14 青岛博迈斯环保技术有限公司 Equipment for carbonization treatment of sludge and its using method
CN102167628A (en) * 2011-01-17 2011-08-31 青岛博迈斯环保技术有限公司 A chicken manure charcoal fertilizer and a production method thereof
CN102173931A (en) * 2011-01-17 2011-09-07 青岛博迈斯环保技术有限公司 Animal manure carbon fertilizer and production method thereof
CN102173931B (en) * 2011-01-17 2014-01-01 青岛博迈斯环保技术有限公司 Animal manure carbon fertilizer and production method thereof
CN102167628B (en) * 2011-01-17 2014-07-23 青岛博迈斯环保技术有限公司 A chicken manure charcoal fertilizer and a production method thereof
CN103420553A (en) * 2013-08-31 2013-12-04 山东宏力空调设备有限公司 High-temperature hearth carbonizing furnace
CN104498063A (en) * 2014-11-25 2015-04-08 中南林业科技大学 Compound dry distiller used for manure processing
CN106678813A (en) * 2017-02-13 2017-05-17 杨红波 Device for treating medium and low level waste
CN110655055A (en) * 2018-06-29 2020-01-07 山西贝特瑞新能源科技有限公司 Continuous carbide furnace device of negative electrode material

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Addressee: Qingdao Biomass Environmental Protection Technology Co.,Ltd.

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091104

Termination date: 20151128