CN202682924U - Tail gas collecting device of high-temperature sintering furnace - Google Patents
Tail gas collecting device of high-temperature sintering furnace Download PDFInfo
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- CN202682924U CN202682924U CN 201220388276 CN201220388276U CN202682924U CN 202682924 U CN202682924 U CN 202682924U CN 201220388276 CN201220388276 CN 201220388276 CN 201220388276 U CN201220388276 U CN 201220388276U CN 202682924 U CN202682924 U CN 202682924U
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- pump
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- rotary pump
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Abstract
The utility model provides a tail gas collecting device of a high-temperature sintering furnace. The tail gas collecting device comprises a liquid ring pump and a postpositional filter unit which is connected with the liquid ring pump through a pipeline. The postpositional filter unit is composed of more than two liquid containers which are communicated with each other in series. Filter screens are arranged at the connector between two adjacent liquid containers. A first-level container of the postpositional filter unit is directly connected with an exhaust port of the liquid ring pump through the pipeline. A final-level container along the liquid flow direction is connected with a water suction pump through the pipeline. The other end of the water suction pump is connected with a feed liquid inlet of the liquid ring pump through the pipeline. Volatile matters in a furnace chamber of the high-temperature sintering furnace enter the liquid ring pump, suspend in the water, and then are brought out along with exhaust air of the liquid ring pump and a portion of water. Next, the volatile matters enter the first-level container and then filtered through filtering and precipitating of the filter screens. Purified water does not contain impurities and can be supplied to the liquid ring pump through the water suction pump to be used as a working medium. Water resources are saved.
Description
Technical field
The utility model relates to a kind of high temperature sintering furnace, particularly a kind of tail gas collecting device of high temperature sintering furnace.
Background technology
It is H that Granted publication number is used for air inlet for the Chinese patent file CVI/CVD process tail gas processing method of CN 1072458C discloses
2, the processing method of Ar and metal organosilan CVI/CVD process tail gas.The method mainly adopts three grades of composite treatment process, by preposition filtration, mechanical pump pump drainage, water filtration tail gas is processed, and makes the discharging of tail gas reach environmental protection standard.Preposition filtration mainly adopts oil strainer and solid filter to remove sedimentation products solids, catabolite tar, and part is removed HCl gas and removed residu tar; The water filter that water ring pump, circulation NaOH solution and moisture trap form is removed HCl gas.In this patent document, adopt mechanical pump to vacuumize, by preposition exhaust gas processing device, only have the HCl that does not remove fully to enter in the water ring pump, along with the water ring pump exhaust enters into moisture trap, the H of separation
2Enter atmosphere with Ar by discharge duct, and HCl gas and NaOH solution fully react the saline solution of generation and enters water tank, when the acid-base value of NaOH solution when being neutral, prove that NaOH has been exhausted, should in time change the NaOH aqueous solution.
Because water ring pump constantly has water at work along with the exhaust of water ring pump is taken out of water ring pump, therefore need constantly to replenish working media---water to water ring pump, and can find out from the above-mentioned course of work, the technical scheme of this patent document is not considered the supply to water ring pump, therefore in this patent document water ring pump is replenished working media and can only rely on constantly and carry out supply from extraneous suction water, thereby can cause the waste of resource.
The utility model content
The purpose of this utility model is to provide a kind of exhaust collection equipment of high temperature sintering furnace, can realize the water circuit utilization, economizes on resources.
For solving above-mentioned purpose, the utility model adopts following technical scheme: a kind of exhaust collection equipment of high temperature sintering furnace, comprise liquid rotary pump and the rearmounted filter that links to each other by pipeline with liquid rotary pump, described rearmounted filter is composed in series by the liquid container that is connected more than two, interface at adjacent liquid container is provided with filter screen, the first order container of described rearmounted filter directly links to each other with the liquid rotary pump exhaust outlet by pipeline, afterbody container along liquid flow direction is connected with suction pump by pipeline, and the described suction pump other end is connected by pipeline with the supply opening of described liquid rotary pump.
Described rearmounted filter is for to be separated into two-part container by filter screen, and the described first order is the filtering ponds that link to each other by pipeline with the liquid rotary pump exhaust outlet, and described afterbody is the clarifier-tank that links to each other with the liquid rotary pump supply opening by suction pump.
The exhaust collection equipment of high temperature sintering furnace of the present utility model, with the volatile matter that produces in the high temperature sintering furnace furnace chamber by after the filtration of pre-filtering device, under the pump drainage of vacuum unit, the unfiltered volatile matter of part, enter liquid rotary pump, volatile matter is suspended in the working media of liquid rotary pump---in the water, the liquid rotary pump next stage is provided with the filter that links to each other by pipeline with described liquid rotary pump, this filter is for to be composed in series by the liquid container that is connected more than two, be provided with filter screen at the adjacent container interface, described first order container is connected by pipeline with the liquid rotary pump exhaust outlet, when liquid rotary pump is worked, enter this from the water that the liquid rotary pump exhaust outlet is taken out of by pipeline along with the liquid rotary pump exhaust, by filtration from level to level, the volatile matter that suspends in water is filtered out, enter at last in the described afterbody container, water in this container has not contained impurity at this moment, by the suction pump that is attached thereto, the water suction that will not have impurity is supplied with liquid rotary pump by the supply opening of liquid rotary pump and is recycled as working media, thereby realize the recycling of resource, saving water resource.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment.
The specific embodiment
As shown in Figure 1, a kind of embodiment of exhaust collection equipment of high temperature sintering furnace comprises pre-filtering device, vacuum unit and rearmounted filter.
The pre-filtering device of present embodiment is the dewaxing tank 3 for the higher boiling volatile matter of collecting furnace chamber 1 generation.The flue of furnace chamber 1 is by vacuum valve 2 access dewaxing tanks 3 entrances.
The vacuum unit is comprised of lobe pump 4, gauge valve 5, atmosphere injection valve 6 and liquid rotary pump 7.Lobe pump 4 air inlets are connected by pipeline with 3 outlets of dewaxing tank, the air inlet of the exhaust outlet of lobe pump 4, gauge valve 5, atmosphere injection valve 6 and liquid rotary pump 7 is successively by pipeline series connection, and the exhaust outlet of liquid rotary pump 7 passes into rearmounted filter outside the workshop by pipeline---in the settling tank 8.Adopt lobe pump series connection atmosphere injection valve and liquid rotary pump to form the vacuum unit, improve the final vacuum of vacuum unit, more thoroughly the volatile matter in the pump drainage furnace chamber 1.
Described rearmounted filter is for to be separated into two-part settling tank 8 by filter screen 9.The described first order is filtering ponds 81, described afterbody is another part clarifier-tank 82 of settling tank 8, the exhaust outlet of liquid rotary pump 7 directly passes in the filtering ponds 81 by pipeline, filtration by filter screen 9, water after the filtration flows in the clarifier-tank 82, therefore the water in the clarifier-tank 82 does not contain the volatile matter that pumps out in the furnace chamber 1, can continue to recycle as working media for liquid rotary pump 7.
Adopting suction pump 11 constantly the water in the clarifier-tank 82 to be supplied with liquid rotary pump 7 in the present embodiment recycles as working media.Suction pump 11 1 ends are provided with valve 10, and by in the pipeline access clarifier-tank 82, the other end is connected by the supply opening of pipeline with liquid rotary pump 7.
During work, open vacuum valve 2, starting 7 pairs of furnace chambers 1 of liquid rotary pump vacuumizes, volatile matter in the furnace chamber 1 is rotated voluntarily by lobe pump 4(gas push roots pump rotor) enter liquid rotary pump 7 through gauge valve 5 and atmosphere injection valve 6, when the suction pressure of atmosphere injection valve 6 reaches the permission pressure at expulsion of lobe pump 4, lobe pump 4 begins to start, and the vacuum unit starting vacuumizes furnace chamber 1.Pump drainage along with liquid rotary pump 7, volatile matter in the furnace chamber 1 enters dewaxing tank 3 by pipeline, dewaxing tank 3 is collected after the higher boiling volatile matter, residual volatile matter is along with liquid rotary pump 7 bleeds, enter the air inlet of lobe pump 4, discharge from the exhaust outlet of lobe pump 4 again, by the guiding of gauge valve 5, flow to liquid rotary pump 7 through atmosphere injection valve 6, volatile matter is suspended in the water, exhaust along with liquid rotary pump 7, part water and the volatile matter that suspends in water are taken out of liquid rotary pump 7 thereupon, by discharge of pipes in filtering ponds 81, by the filtration of filter screen 9, volatile matter is left in the filtering ponds 81, and the water after filtering flows directly in the clarifier-tank 82.Water after the purification does not contain other impurity, opens valve 10, it is pumped into the liquid rotary pump 7 from the liquid rotary pump supply opening by the suction pump 11 that is connected with clarifier-tank 82, supplies with liquid rotary pump 7 and recycles as working media.
In other embodiment of the present utility model, the settling tank described in above-described embodiment can also for being composed in series by other the independent containers that are connected more than 3 or 3, be composed in series such as a plurality of water tanks, and be provided with filter screen at the interface of each adjacent container.
Claims (2)
1. the exhaust collection equipment of a high temperature sintering furnace, comprise liquid rotary pump and the rearmounted filter that links to each other by pipeline with liquid rotary pump, it is characterized in that: described rearmounted filter is composed in series by the liquid container that is connected more than two, be provided with filter screen at adjacent liquid container interface, the first order container of described rearmounted filter directly links to each other with the liquid rotary pump exhaust outlet by pipeline, afterbody container along liquid flow direction is connected with suction pump by pipeline, and the described suction pump other end is connected by pipeline with the supply opening of described liquid rotary pump.
2. the exhaust collection equipment of high temperature sintering furnace according to claim 1, it is characterized in that: described rearmounted filter is for to be separated into two-part container by filter screen, the described first order is the filtering ponds that link to each other by pipeline with the liquid rotary pump exhaust outlet, and described afterbody is the clarifier-tank that links to each other with the liquid rotary pump supply opening by suction pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220388276 CN202682924U (en) | 2012-08-07 | 2012-08-07 | Tail gas collecting device of high-temperature sintering furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220388276 CN202682924U (en) | 2012-08-07 | 2012-08-07 | Tail gas collecting device of high-temperature sintering furnace |
Publications (1)
Publication Number | Publication Date |
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CN202682924U true CN202682924U (en) | 2013-01-23 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220388276 Expired - Fee Related CN202682924U (en) | 2012-08-07 | 2012-08-07 | Tail gas collecting device of high-temperature sintering furnace |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115253645A (en) * | 2022-08-26 | 2022-11-01 | 湖南顶立科技有限公司 | Vacuum guarantee and tail gas treatment integrated system and using method thereof |
-
2012
- 2012-08-07 CN CN 201220388276 patent/CN202682924U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115253645A (en) * | 2022-08-26 | 2022-11-01 | 湖南顶立科技有限公司 | Vacuum guarantee and tail gas treatment integrated system and using method thereof |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: 450199 Jinzhai, Henan City, Xingyang Jin Zhai village, Zhengzhou Patentee after: Henan Aryan New Material Co., Ltd. Address before: 450199 Jinzhai, Henan City, Xingyang Jin Zhai village, Zhengzhou Patentee before: Henan Aryan Speical Ceramics Co., Ltd. |
|
CP01 | Change in the name or title of a patent holder | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130123 Termination date: 20200807 |
|
CF01 | Termination of patent right due to non-payment of annual fee |