CN207452043U - A kind of refuse gasification desulfurization deacidifying device - Google Patents
A kind of refuse gasification desulfurization deacidifying device Download PDFInfo
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- CN207452043U CN207452043U CN201721532626.2U CN201721532626U CN207452043U CN 207452043 U CN207452043 U CN 207452043U CN 201721532626 U CN201721532626 U CN 201721532626U CN 207452043 U CN207452043 U CN 207452043U
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- desulfurization
- case
- depickling
- water pump
- refuse gasification
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Abstract
The utility model discloses a kind of refuse gasification desulfurization deacidifying device, including reduction sagger, desulfurization deacidification agent case, air inlet pipe, the first driving water pump, desulfurization depickling case, stirring wheel, driving motor, the second driving water pump, the first feed pipe, the second feed pipe；The air inlet pipe passes through the upper roof of desulfurization depickling case, wherein the lower nozzle of air inlet pipe is located at the middle and lower part of desulfurization depickling case reaction chamber, stirring wheel is installed in the middle part of the bottom surface of desulfurization depickling case reaction chamber, wherein stirring wheel is connected by agitating shaft with driving motor, and wherein agitating shaft passes through the lower roof plate of desulfurization depickling case；Reduction sagger, desulfurization deacidification agent case, the first driving water pump are from left to right installed successively on the upper top surface of the desulfurization depickling case.The utility model is for the device handled in the gas after refuse gasification containing sulphur, acid.
Description
Technical field
The utility model is related to a kind of desulfurization deacidifying devices, and in particular to a kind of refuse gasification desulfurization deacidifying device.
Background technology
Refuse gasification is divided into common gasification and plasma gasification.
Refuse gasification refers in closed container, rubbish is carried out anoxycausis, using air and steam as mixing
Gasifying agent, Control for Kiln Temperature make rubbish release the flammable gas such as substantial amounts of carbon monoxide, hydrogen, methane at 800 DEG C,
After filtering and cleaning, can the gas be converted into electric energy or thermal energy to utilize.Due to entire gasification temperature compared with
It is low, it will not largely generate nitrogen oxides；Bioxin is generated in gasification chilling facility to be utilized to coordinate activated carbon adsorption
Tower and bag-type dust collector remove completely, and the fuel gas that gasification generates may finally be made to become real pure green energy
Source.
Plasma gasification（plasma gasification）It needs to heat high temperature garbage in the combustion chamber of closing.This
In the case that kind process is happened at almost anaerobic, the organic principle in rubbish will not burn, but be changed into carbon monoxide and hydrogen
The synthesis gas of gas（syngas）.The gas is filtered, and chemical composition can be fallen by " cleaning ", gentle so as to remove toxic molecule
Then body through burned for energy or is converted into the fuel of biogas, ethyl alcohol or combined diesel oil etc..After this process, most
It is left the chemical substance that dust, filter and cleaning leave afterwards, it is treated to send to burial or be discharged into sewer.Plasma
Gasification is that rubbish is evaporated in the case of at higher temperature, and more debirs is made to gasify, and temperature is and common up to 10,000 degrees Celsius
Gasification temperature is only 800 degrees Celsius.Another advantage of plasma gasification technology is that high temperature will not make rubbish become fine ash, but
Vitreous solid may be used as the filler material in building trade in this theory of solids.But plasma refuse gasification consumes in itself
It can be huge, it is difficult to realize commercialization.
The method of past processing rubbish is to burn to generate steam by incinerator, drives turbine, drives electrical power generators.
In comparison, gasification when burning a certain amount of rubbish than generating more energy, and discharges poisonous and harmful substance and understand less.
At present gasification rubbish technology pilot factory in states such as the U.S., Canada, France, Britain and Portugal it has been established that
Wherein most uses plasma gasification technology.Japan has two commercialization plasma refuse gasification power plants.China
Also there is domestic garbage gasification center, have been carried out stable electric generation.
Gas in after refuse gasification can contain ingredients, such gases such as substantial amounts of sulphur, acid and be discharged into meeting in air
Air is polluted, acid rain can be formed when serious, is badly in need of now for the dress handled in the gas after refuse gasification containing sulphur, acid
It puts.
The content of the invention
The purpose of this utility model is to provide a kind of refuse gasification desulfurization deacidifying devices, are for the gas after refuse gasification
The device handled in body containing sulphur, acid.
A kind of refuse gasification desulfurization deacidifying device, including reduction sagger, desulfurization deacidification agent case, air inlet pipe, first driving water pump,
Desulfurization depickling case, stirring wheel, driving motor, the second driving water pump, the first feed pipe, the second feed pipe；It is characterized in that：It is described
Air inlet pipe passes through the upper roof of desulfurization depickling case, and the wherein lower nozzle of air inlet pipe is located at the middle and lower part of desulfurization depickling case reaction chamber,
Stirring wheel is installed in the middle part of the bottom surface of desulfurization depickling case reaction chamber, wherein stirring wheel is connected by agitating shaft with driving motor
It connects, wherein agitating shaft passes through the lower roof plate of desulfurization depickling case；It is from left to right installed successively on the upper top surface of the desulfurization depickling case
Reduction sagger, desulfurization deacidification agent case, the first driving water pump.
Further, the reduction sagger is connected with desulfurization deacidification agent case by pipeline, and wherein reduction sagger is by desulfurization deacidification agent
It restores, reaches recycling.
Further, the reduction sagger is equipped with the first feed pipe, wherein the first feed pipe makes reducing agent be passed through in reduction sagger,
Reducing agent is made to carry out reduction reaction with the waste liquid in desulfurization depickling case out.
Further, the desulfurization deacidification agent case be equipped with the second feed pipe, wherein the second feed pipe make desulfurization deacidification agent into
Enter in desulfurization deacidification agent case.
Further, the desulfurization deacidification agent case is connected by pipeline with the first driving water pump, wherein the first driving water pump makes
Desulfurization deacidification agent enters desulfurization depickling case.
Further, the first driving water pump is connected by pipeline with the feed inlet of desulfurization depickling case, wherein first drives
Dynamic water pump makes desulfurization deacidification agent enter desulfurization depickling case.
Further, the reduction sagger is connected by pipeline with the second driving water pump, wherein the second driving water pump takes off desulfurization
Waste liquid in sour case is transported in reduction sagger.
Further, the second driving water pump is connected by pipeline with the discharge port of desulfurization depickling case, wherein the second driving
Water pump makes the waste liquid in desulfurization depickling case be transported in reduction sagger.
In use, starting the first driving water pump, desulfurization deacidification agent is made to enter desulfurization depickling case, then by the gas after refuse gasification
Body is passed through desulfurization depickling case by air inlet pipe, while starts driving motor, stirring wheel is driven to rotate, wherein stirring wheel stirring desulphurization
Gas after deacidification agent and refuse gasification, makes the two sufficiently be mixed, while also makes the gas sweetening after refuse gasification
Depickling is more abundant, when completing desulfurization depickling, starts the second driving water pump, the waste liquid in desulfurization depickling case is quickly extracted out,
In reduction sagger is transported to, waste liquid is made to be reduced into desulfurization deacidification agent, is recycled, is economized on resources.
The beneficial effects of the utility model are：The present apparatus is simple in structure, and design is reasonable, after the present apparatus removes refuse gasification
Gas in containing substantial amounts of sulphur, acid；The present apparatus utilize stirring wheel, make both gas after desulfurization deacidification agent and refuse gasification into
Row sufficiently mixing, make the present apparatus except desulfuration, acid it is efficient；Meanwhile the present apparatus makes the present apparatus form Xun Huan also using pipeline
System can not only economize on resources, moreover it is possible to accelerate the efficiency of the present apparatus；The present apparatus also using reduction sagger, obtains desulfurization deacidification agent
It recycles.
Description of the drawings
Fig. 1 is the structure diagram of the utility model；
Fig. 2 is the structure diagram of the utility model；
Fig. 3 is the utility model desulfurization depickling case sectional view.
In figure, reduction sagger 1, desulfurization deacidification agent case 2, air inlet pipe 3, first drive water pump 4, desulfurization depickling case 5, stirring wheel 6,
Driving motor 7, second drives water pump 8, the first feed pipe 9, the second feed pipe 10.
Specific embodiment
It is the better embodiment of the utility model below, but does not therefore limit the scope of protection of the utility model.
As shown in the figure, a kind of refuse gasification desulfurization deacidifying device, including reduction sagger 1, desulfurization deacidification agent case 2, air inlet pipe 3,
First driving water pump 4, desulfurization depickling case 5, stirring wheel 6, driving motor 7, second drive water pump 8, the first feed pipe 9, second into
Expects pipe 10；It is characterized in that：The air inlet pipe 3 passes through the upper roof of desulfurization depickling case 5, and the lower nozzle of wherein air inlet pipe 3 is located at
The middle and lower part of 5 reaction chamber of desulfurization depickling case, is installed with stirring wheel 6, wherein stirring in the middle part of the bottom surface of 5 reaction chamber of desulfurization depickling case
It mixes wheel 6 by agitating shaft with driving motor 7 to be connected, wherein agitating shaft passes through the lower roof plate of desulfurization depickling case 5；The desulfurization takes off
Reduction sagger 1 is from left to right installed successively, desulfurization deacidification agent case 2, first drives water pump 4 on the upper top surface of sour case 5.
Further, the reduction sagger 1 is connected with desulfurization deacidification agent case 2 by pipeline, and wherein reduction sagger 1 is by desulfurization depickling
Agent restores, and reaches recycling, and wherein reduction sagger 1 is equipped with the first feed pipe 9, wherein the first feed pipe 9 makes reducing agent
It is passed through in reduction sagger 1, reducing agent is made to carry out reduction reaction, wherein desulfurization deacidification agent case 2 with the waste liquid in desulfurization depickling case 5 out
The second feed pipe 10 is equipped with, wherein the second feed pipe 10 makes desulfurization deacidification agent enter in desulfurization deacidification agent case 2, wherein desulfurization takes off
Sour agent case 2 is connected by pipeline with the first driving water pump 4, wherein the first driving water pump 4 by pipeline and desulfurization depickling case 5 into
Material mouth is connected, wherein the first driving water pump 4 makes desulfurization deacidification agent enter desulfurization depickling case 5；The reduction sagger 1 by pipeline with
Second driving water pump 8 connects, wherein the second driving water pump 8 is connected by pipeline with the discharge port of desulfurization depickling case 5, wherein second
Driving water pump 8 makes the waste liquid in desulfurization depickling case 5 be transported in reduction sagger 1.
In use, starting the first driving water pump 4, desulfurization deacidification agent is made to enter desulfurization depickling case 5, then will be after refuse gasification
Gas is passed through desulfurization depickling case 5 by air inlet pipe 3, while starts driving motor 7, stirring wheel 6 is driven to rotate, wherein stirring wheel 6
Gas after stirring desulphurization deacidification agent and refuse gasification, makes the two sufficiently be mixed, while after also making refuse gasification
Gas sweetening depickling is more abundant, when completing desulfurization depickling, starts the second driving water pump 8, and the waste liquid in desulfurization depickling case 5 is fast
The extraction of speed, in reduction sagger 1 is transported to, makes waste liquid be reduced into desulfurization deacidification agent, recycles, economize on resources.
The utility model devises a kind of refuse gasification desulfurization deacidifying device：The present apparatus is simple in structure, and design is reasonable, this dress
It puts in the gas after removing refuse gasification containing substantial amounts of sulphur, acid；The present apparatus utilizes stirring wheel, makes desulfurization deacidification agent and rubbish gas
Both gas after change is sufficiently mixed, make the present apparatus except desulfuration, acid it is efficient；Meanwhile the present apparatus also utilizes pipeline,
The present apparatus is made to form the circulatory system, can not only be economized on resources, moreover it is possible to accelerate the efficiency of the present apparatus；The present apparatus also utilizes reduction sagger,
Recycled desulfurization deacidification agent.
It the above is only the preferred embodiment of the utility model, it is noted that for the ordinary skill people of the art
Member for, on the premise of the utility model technical principle is not departed from, several improvements and modifications can also be made, these improve and
Retouching also should be regarded as the scope of protection of the utility model.
Claims (8)
1. a kind of refuse gasification desulfurization deacidifying device drives water pump including reduction sagger, desulfurization deacidification agent case, air inlet pipe, first, takes off
Sulphur depickling case, stirring wheel, driving motor, the second driving water pump, the first feed pipe, the second feed pipe；It is characterized in that：It is described into
Tracheae passes through the upper roof of desulfurization depickling case, and the wherein lower nozzle of air inlet pipe is located at the middle and lower part of desulfurization depickling case reaction chamber,
Stirring wheel is installed in the middle part of the bottom surface of desulfurization depickling case reaction chamber, wherein stirring wheel is connected by agitating shaft with driving motor
It connects, wherein agitating shaft passes through the lower roof plate of desulfurization depickling case；It is from left to right installed successively on the upper top surface of the desulfurization depickling case
Reduction sagger, desulfurization deacidification agent case, the first driving water pump.
2. a kind of refuse gasification desulfurization deacidifying device according to claim 1, it is characterized in that：The reduction sagger takes off with desulfurization
Sour agent case is connected by pipeline.
3. a kind of refuse gasification desulfurization deacidifying device according to claim 1, it is characterized in that：The reduction sagger is equipped with the
One feed pipe.
4. a kind of refuse gasification desulfurization deacidifying device according to claim 1, it is characterized in that：On the desulfurization deacidification agent case
Equipped with the second feed pipe.
5. a kind of refuse gasification desulfurization deacidifying device according to claim 1, it is characterized in that：The desulfurization deacidification agent case leads to
Piping is connected with the first driving water pump.
6. a kind of refuse gasification desulfurization deacidifying device according to claim 5, it is characterized in that：The first driving water pump leads to
Piping is connected with the feed inlet of desulfurization depickling case.
7. a kind of refuse gasification desulfurization deacidifying device according to claim 2, it is characterized in that：The reduction sagger passes through pipeline
It is connected with the second driving water pump.
8. a kind of refuse gasification desulfurization deacidifying device according to claim 7, it is characterized in that：The second driving water pump leads to
Piping is connected with the discharge port of desulfurization depickling case.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721532626.2U CN207452043U (en) | 2017-11-16 | 2017-11-16 | A kind of refuse gasification desulfurization deacidifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721532626.2U CN207452043U (en) | 2017-11-16 | 2017-11-16 | A kind of refuse gasification desulfurization deacidifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207452043U true CN207452043U (en) | 2018-06-05 |
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ID=62280200
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|---|---|---|---|
| CN201721532626.2U Active CN207452043U (en) | 2017-11-16 | 2017-11-16 | A kind of refuse gasification desulfurization deacidifying device |
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| CN (1) | CN207452043U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116970413A (en) * | 2023-09-22 | 2023-10-31 | 山东东方宏业化工有限公司 | Waste organic matter cracking treatment system and process |
-
2017
- 2017-11-16 CN CN201721532626.2U patent/CN207452043U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116970413A (en) * | 2023-09-22 | 2023-10-31 | 山东东方宏业化工有限公司 | Waste organic matter cracking treatment system and process |
| CN116970413B (en) * | 2023-09-22 | 2023-12-19 | 山东东方宏业化工有限公司 | Waste organic matter cracking treatment system and process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191216 Address after: 311201 Fenghuang mountain village, Xiaoshan District, Hangzhou, Zhejiang Patentee after: Zhejiang Jiuan Boiler & Pressure Container Manufacturing Co., Ltd. Address before: 311201 Fenghuang mountain village, Xiaoshan District, Hangzhou, Zhejiang Patentee before: Tang Chunfeng |