CN205699624U - A kind of continuous way chemical industry subsider - Google Patents
A kind of continuous way chemical industry subsider Download PDFInfo
- Publication number
- CN205699624U CN205699624U CN201620414310.2U CN201620414310U CN205699624U CN 205699624 U CN205699624 U CN 205699624U CN 201620414310 U CN201620414310 U CN 201620414310U CN 205699624 U CN205699624 U CN 205699624U
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- cell body
- hollow axle
- subsider
- collecting chamber
- overflow
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Abstract
The utility model discloses a kind of continuous way chemical industry subsider, including cell body and collecting chamber；Centre position, described cell body side is equipped with feed pipe；Cell body opposite side top is equipped with overflow pipe；The described overflow pipe other end is connected with overflow cylinder；It is connected with feed pipe by conveyance conduit bottom described overflow cylinder；Cell body top is equipped with cover plate；Described cover plate central position is equipped with hollow axle；Described hollow axle top is equipped with swivel joint；The described swivel joint other end is connected with discharging tube；Hollow axle centre position is provided with pump orifice；Equipped with scraper plate bottom hollow axle；Second row outlet it is provided with bottom cell body；The outlet of described second row is connected with collecting chamber；Described collecting chamber side is equipped with helical blade obliquely；This utility model continual can carry out solid-liquid separation with continuous sedimentation；Through rotating centrifugal effect, the impurity being difficult to precipitation converges at cell body inwall；Aspirate by arranging pump orifice on hollow axle, effectively reduce the content of solid particle in liquid.
Description
Technical field
This utility model relates to a kind of chemical industry equipment, specifically a kind of continuous way chemical industry subsider.
Background technology
At chemical field, use subsider to be separated with liquid by the solid particle in feed liquid, but existing subsider is difficult to work continuously, for realizing continuous work, it is most important that realize discharging the subsider supernatant and the solid of bottom sedimentation continuously；The solid discharge device of general subsider easily causes Upgrade Problem because the viscosity of solid is different so that solid discharge has some setbacks；Meanwhile, the discharge of overflow clear liquid may be formed because of in clear liquid scab containing a small amount of solid particle, and ultimately resulting in subsider cannot work continuously.
Utility model content
The purpose of this utility model is to provide a kind of continuous way chemical industry subsider, with the problem solving to propose in above-mentioned background technology.
For achieving the above object, the following technical scheme of this utility model offer:
A kind of continuous way chemical industry subsider, including cell body and collecting chamber；Centre position, described cell body side is equipped with feed pipe；Equipped with the second check valve on described feed pipe；Cell body opposite side top is equipped with overflow pipe；The described overflow pipe other end is connected with overflow cylinder；It is connected with feed pipe by conveyance conduit bottom described overflow cylinder；Cell body top is equipped with cover plate；Described cover plate central position is equipped with hollow axle；Described hollow axle top is equipped with swivel joint；The described swivel joint other end is connected with discharging tube；Equipped with suction pump on described discharging tube；Hollow axle top is connected by transmission band and the first motor；Hollow axle centre position is provided with pump orifice；Equipped with scraper plate bottom hollow axle；Second row outlet it is provided with bottom cell body；The outlet of described second row is connected with collecting chamber；Described collecting chamber side is equipped with helical blade obliquely；Described helical blade top is connected with the second motor；First row outlet it is provided with below helical blade top.
As further program of the utility model: on described conveyance conduit, near one end of overflow cylinder equipped with stop valve；Near one end of feed pipe equipped with the first check valve；Equipped with gear pump between described stop valve and the first check valve.
As this utility model further scheme: the level height of described pump orifice is lower than the level height of overflow pipe 10 centimetres.
Compared with prior art, the beneficial effects of the utility model are:
This utility model simple in construction, easy to operate, continual can carry out solid-liquid separation with continuous sedimentation；Through rotating centrifugal effect, the impurity being difficult to precipitation converges at cell body inwall；Aspirate by arranging pump orifice on hollow axle, effectively reduce the content of solid particle in liquid；By bottom scraper plate, the precipitate of bottom is scraped in collecting chamber, then is discharged by helix transporting device；Effectively reduce the content liquid in precipitate.
Accompanying drawing explanation
Fig. 1 is the structural representation of continuous way chemical industry subsider.
Fig. 2 is the structural representation of continuous way chemical industry subsider middle scraper.
In figure: 1-the first motor, 2-transmission band, 3-cover plate, 4-overflow pipe, 5-overflow cylinder, 6-stop valve, 7-conveyance conduit, 8-the second motor, 9-first row exports, 10-helical blade, 11-collecting chamber, and 12-second row exports, 13-hollow axle, 14-scraper plate, 15-gear pump, 16-the first check valve, 17-feed pipe, 18-the second check valve, 19-cell body, 20-pump orifice, 21-swivel joint, 22-suction pump, 23-discharging tube.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the technical scheme of this patent is described in more detail.
Referring to Fig. 1-2, a kind of continuous way chemical industry subsider, including cell body 19 and collecting chamber 11；Centre position, described cell body 19 side is equipped with feed pipe 17；Equipped with the second check valve 18 on described feed pipe 17；Cell body 19 opposite side top is equipped with overflow pipe 4；Described overflow pipe 4 other end is connected with overflow cylinder 5；It is connected with feed pipe 17 by conveyance conduit 7 bottom described overflow cylinder 5；On conveyance conduit 7, near one end of overflow cylinder 5 equipped with stop valve 6；On conveyance conduit 7, near one end of feed pipe 17 equipped with the first check valve 16；Equipped with gear pump 15 between described stop valve 6 and the first check valve 16；Cell body 19 top is equipped with cover plate 3；Described cover plate 3 center is equipped with hollow axle 13；Described hollow axle 13 top is equipped with swivel joint 21；Described swivel joint 21 other end is connected with discharging tube 23；Equipped with suction pump 22 on described discharging tube 23；Hollow axle 13 top is connected with the first motor 1 by transmission band 2；Hollow axle 13 centre position is provided with pump orifice 20；The level height of described pump orifice 20 is lower than the level height of overflow pipe 4 10 centimetres；Equipped with scraper plate 14 bottom hollow axle 13；Second row outlet 12 it is provided with bottom cell body 19；Described second row outlet 12 is connected with collecting chamber 11；Described collecting chamber 11 side is equipped with helical blade 10 obliquely；Described helical blade 10 top is connected with the second motor 8；First row outlet 9 it is provided with below helical blade 10 top.
Operation principle of the present utility model is:
Material enters in cell body 19 from charging aperture 17 and settles；First motor 1 drives hollow axle 13 to rotate, and is stirred material so that the precipitate bottom cell body 19, from second row outlet 12 entrance collecting chamber 11, is being discharged via helical blade 10；Supernatant liquid passes through pump orifice 20, flows to swivel joint 21, suction pump 22 and discharging tube 23 from hollow axle 13 inside；Discharge from discharging tube 23；When in cell body 19, page height is too high, will flow in overflow cylinder 5 from overflow pipe 4；It is back in feed pipe 17 by the effect of conveyance conduit 7 and gear pump 15 again.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art is possessed, it is also possible to make a variety of changes on the premise of without departing from this patent objective.
Claims (3)
1. a continuous way chemical industry subsider, including cell body and collecting chamber；It is characterized in that, centre position, described cell body side is equipped with feed pipe；Equipped with the second check valve on described feed pipe；Cell body opposite side top is equipped with overflow pipe；The described overflow pipe other end is connected with overflow cylinder；It is connected with feed pipe by conveyance conduit bottom described overflow cylinder；Cell body top is equipped with cover plate；Described cover plate central position is equipped with hollow axle；Described hollow axle top is equipped with swivel joint；The described swivel joint other end is connected with discharging tube；Equipped with suction pump on described discharging tube；Hollow axle top is connected by transmission band and the first motor；Hollow axle centre position is provided with pump orifice；Equipped with scraper plate bottom hollow axle；Second row outlet it is provided with bottom cell body；The outlet of described second row is connected with collecting chamber；Described collecting chamber side is equipped with helical blade obliquely；Described helical blade top is connected with the second motor；First row outlet it is provided with below helical blade top.
Continuous way chemical industry subsider the most according to claim 1, it is characterised in that on described conveyance conduit, near one end of overflow cylinder equipped with stop valve；Near one end of feed pipe equipped with the first check valve；Equipped with gear pump between described stop valve and the first check valve.
Continuous way chemical industry subsider the most according to claim 1, it is characterised in that the level height of described pump orifice is lower than the level height of overflow pipe 10 centimetres.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620414310.2U CN205699624U (en) | 2016-05-10 | 2016-05-10 | A kind of continuous way chemical industry subsider |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620414310.2U CN205699624U (en) | 2016-05-10 | 2016-05-10 | A kind of continuous way chemical industry subsider |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205699624U true CN205699624U (en) | 2016-11-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620414310.2U Active CN205699624U (en) | 2016-05-10 | 2016-05-10 | A kind of continuous way chemical industry subsider |
Country Status (1)
| Country | Link |
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| CN (1) | CN205699624U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055847A (en) * | 2017-06-27 | 2017-08-18 | 陈金辉 | Efficient colliery water purification installation |
| CN107082201A (en) * | 2017-05-05 | 2017-08-22 | 杭州金知科技有限公司 | It is easy to the good antiscale property thickener and method of discharging in a kind of Salt production |
| CN108126375A (en) * | 2018-01-23 | 2018-06-08 | 北京澳柯清洁煤气工程技术有限公司 | Slag-liquid separation device and method |
| CN109107269A (en) * | 2018-09-27 | 2019-01-01 | 南京金陵化工厂有限责任公司 | A kind of compound stabilizer production spun down slot |
| CN111375231A (en) * | 2020-04-11 | 2020-07-07 | 长兴和泽环保科技有限公司 | Sludge scraping device of treatment tank for sewage treatment of environmental protection equipment |
-
2016
- 2016-05-10 CN CN201620414310.2U patent/CN205699624U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107082201A (en) * | 2017-05-05 | 2017-08-22 | 杭州金知科技有限公司 | It is easy to the good antiscale property thickener and method of discharging in a kind of Salt production |
| CN107055847A (en) * | 2017-06-27 | 2017-08-18 | 陈金辉 | Efficient colliery water purification installation |
| CN108126375A (en) * | 2018-01-23 | 2018-06-08 | 北京澳柯清洁煤气工程技术有限公司 | Slag-liquid separation device and method |
| CN109107269A (en) * | 2018-09-27 | 2019-01-01 | 南京金陵化工厂有限责任公司 | A kind of compound stabilizer production spun down slot |
| CN111375231A (en) * | 2020-04-11 | 2020-07-07 | 长兴和泽环保科技有限公司 | Sludge scraping device of treatment tank for sewage treatment of environmental protection equipment |
| CN111375231B (en) * | 2020-04-11 | 2022-05-17 | 淮北联诚网络科技有限公司 | Sludge scraping device of treatment tank for sewage treatment of environmental protection equipment |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |