CN201261729Y - Rotary tower separator - Google Patents
Rotary tower separator Download PDFInfo
- Publication number
- CN201261729Y CN201261729Y CNU2008200238645U CN200820023864U CN201261729Y CN 201261729 Y CN201261729 Y CN 201261729Y CN U2008200238645 U CNU2008200238645 U CN U2008200238645U CN 200820023864 U CN200820023864 U CN 200820023864U CN 201261729 Y CN201261729 Y CN 201261729Y
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- CN
- China
- Prior art keywords
- liquid storage
- storage cylinder
- water
- cylinder
- cone
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 73
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000004744 fabric Substances 0.000 claims abstract description 29
- 239000000463 material Substances 0.000 claims abstract description 19
- 238000005086 pumping Methods 0.000 claims abstract description 11
- 230000000740 bleeding effect Effects 0.000 claims description 10
- 238000000605 extraction Methods 0.000 claims description 4
- 238000011001 backwashing Methods 0.000 abstract 3
- 239000010865 sewage Substances 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
A rotary tower separator comprises a support and a liquid storage cylinder with an upper cover on the support, the liquid storage cylinder is a cylinder with a cone-shaped bottom, a discharge port is arranged at the lower part of the liquid storage cylinder, the liquid storage cylinder and the upper cover form a closed pressure container, a filter cylinder which is fixedly connected with the upper cover and has a conical bottom is arranged in the liquid storage cylinder, the side wall of the filter cylinder is provided with filter cloth, the inner cavity of the filter cylinder is provided with at least one cavity, an air exhaust pipe and a filter cloth backwashing pipe are arranged in the cavity and are correspondingly connected with an air exhaust port and a filter cloth backwashing port which are arranged on the upper cover and correspond to the air exhaust pipe and the filter cloth backwashing pipe of each cavity, the side wall of the liquid storage cylinder is provided with a feed inlet which enters tangentially, a water outlet which enters tangentially and a water outlet which enters vertically, a material distributing cone which has the diameter smaller than that of the liquid storage cylinder and is reverse to the cone at the bottom of the liquid storage cylinder is arranged above the inner cone of the liquid storage cylinder, and a water pumping cylinder which is connected with the water outlet through a connecting pipe is arranged below the material distributing cone.
Description
Technical field:
The utility model relates to a kind of waste disposal plant, relate in particular to a kind of rotary column separator.
Background technology:
Along with the continuous quickening of process of industrialization and improving constantly of standard of living, industrial sewage and sanitary sewage be treated as a problem demanding prompt solution, a kind of slag liquid separate vacuum filtration unit is disclosed in application number is 92210671.1 application, this device middle filtrator lower end is connected by communicating vessels and vacuum water tank, sieve plate in the strainer is provided with filter cloth, during work, feed liquid is input in the strainer, not vacuum environment in the strainer, clear water after the filtration is inhaled in the vacuum water tank, takes out when full when the vacuum water tank, opens another vacuum water tank again, two vacuum water tank cycle operatioies, this structure operation complexity, and sewage streamlined flow in strainer, the glide path of sewage is short, filtration efficiency is not high, and this is the existing in prior technology weak point.
Summary of the invention:
The purpose of this utility model, be exactly at the existing in prior technology deficiency, a kind of technical scheme of rotary column separator is provided, this scheme utilizes negative pressure of vacuum principle and cyclone technique to realize the full-automation of sewage disposal, and is applied widely, is specially adapted to the filtration of ultra-fine suspended substance, energy consumption is low, simple in structure, long service life, filtration efficiency height.
This programme is realized by following technical measures: this rotary column separator, comprise support and on support, have the liquid storage cylinder of loam cake, on the sidewall of liquid storage cylinder, opening for feed is arranged, discharge outlet is arranged at the bottom at liquid storage cylinder, be characterized in that described liquid storage cylinder is the right cylinder that taper is arranged at the bottom, this liquid storage cylinder and loam cake constitute airtight pressurized vessel, described opening for feed is the opening for feed that tangentially enters on the sidewall of liquid storage cylinder, the water-in that on the sidewall of liquid storage cylinder, tangentially enters in addition, water outlet that tangentially enters and the vertical water port that enters, above described liquid storage cylinder inner cone, the sub-material cone is arranged, there is water pumping cylinder sub-material cone below, and described water port is connected with water pumping cylinder by pipe connecting; The cartridge filter of fixedlying connected with loam cake is arranged in liquid storage cylinder, on the sidewall of cartridge filter, filter cloth is arranged, the inner chamber of described cartridge filter has a chamber at least, in chamber, there are extraction pipe and filter cloth backwash pipe correspondence to be connected and cover bleeding point corresponding and filter cloth backwash mouth with each chamber evacuation pipe and filter cloth backwash pipe, the bottom of described cartridge filter is taper, the diameter of described sub-material cone is less than liquid storage cylinder diameter and reverse with liquid storage cylinder bottom taper, described water-in and opening for feed position in cartridge filter cone and liquid storage cylinder between the sub-material cone, water-in that tangentially enters in addition in the middle and upper part of described liquid storage cylinder sidewall and the water outlet that tangentially enters.
The beneficial effect of this programme can be learnt according to the narration to such scheme, because in this scheme, the inner chamber of cartridge filter has a chamber at least, in chamber, there are extraction pipe and filter cloth backwash pipe correspondence to be connected and cover bleeding point corresponding and filter cloth backwash mouth with each chamber evacuation pipe and filter cloth backwash pipe, bleeding point connects vacuum pump, guarantee to be always vacuum environment in the cartridge filter, filter cloth backwash mouth water pump or air compressor pump, when filter cloth need clean, can clean the filter cloth of one of them chamber earlier, other chamber works better can guarantee the continuity of operation and stable aquifer yield like this; Liquid storage cylinder is the right cylinder that taper is arranged at the bottom, this liquid storage cylinder and loam cake constitute airtight pressurized vessel, the cartridge filter that is positioned at liquid storage cylinder is always vacuum environment, the great like this filtration efficiency that improved, the bottom of cartridge filter is taper, liquid storage cylinder inner cone top have diameter less than the liquid storage cylinder diameter and with the reverse sub-material cone of liquid storage cylinder bottom taper, there is water pumping cylinder sub-material cone below, on described liquid storage cylinder sidewall, the water port that vertically enters is arranged, water port is connected with water pumping cylinder by pipe connecting, water-in that tangentially enters and the opening for feed that tangentially enters are arranged on the liquid storage cylinder sidewall in cartridge filter cone and liquid storage cylinder between the sub-material cone, above-mentioned water-in is connected with the recirculated water pump outlet, water port is connected with the inlet of water circulating pump, this structure can increase the rotational flow of liquid in the liquid storage cylinder, realized that the suspended substance in the sewage moves down in the tapered bottom rotation of the drive lower edge of eddy flow liquid storage cylinder, finally drop on the discharge outlet end of liquid storage cylinder conical lower portion, reach when setting concentration requirement, by automatic control device control discharging automatically, there are tangential water inlet and tangential water outlet in liquid storage cylinder sidewall middle and upper part, tangential water inlet and tangential water outlet connect recirculated water pump outlet and inlet respectively, can wash away the suspended substance on the filter cloth of cartridge filter sidewall like this, guarantee the ventilation property of filter cloth, this shows, the utility model compared with prior art, have outstanding substantive distinguishing features and obvious improvement, the beneficial effect of its enforcement also is conspicuous.
Description of drawings:
Fig. 1 is the structural representation of the utility model embodiment.
Fig. 2 be among Fig. 1 A-A to sectional view.
Fig. 3 be among Fig. 1 B-B to sectional view.
Among the figure, 1 is hanger, and 2 is bleeding point, 3 is filter cloth backwash mouth, and 4 is loam cake, and 5 is liquid storage cylinder, 6 is water-in, and 7 is water port, and 8 is pipe connecting, 9 is support, and 10 is discharge outlet, and 11 is water pumping cylinder, 12 is the sub-material cone, and 13 is cartridge filter, and 14 is water outlet, 15 is dividing plate, and 16 is supporting plate, and 17 is opening for feed.
Embodiment:
For clearly demonstrating the technical characterstic of this programme,, and, this programme is set forth in conjunction with its accompanying drawing below by an embodiment.
A kind of rotary column separator, comprise support 9 and on support 9, have the liquid storage cylinder 5 of loam cake 4, opening for feed 17 is arranged on the sidewall of liquid storage cylinder 5, in the bottom of liquid storage cylinder 5 discharge outlet 10 is arranged, liquid storage cylinder 5 described in this programme is right cylinders that taper is arranged at the bottom, this liquid storage cylinder 5 constitutes airtight pressurized vessel with loam cake 4, described opening for feed 17 is the opening for feeds 17 that tangentially enter on the sidewall of liquid storage cylinder 5, the water-in 6 that on the sidewall of liquid storage cylinder 5, tangentially enters in addition, water outlet 14 that tangentially enters and the vertical water port that enters 7, above described liquid storage cylinder 5 inner cones, sub-material cone 12 is arranged, there is water pumping cylinder 11 sub-material cone 12 belows, and described water port 7 is connected with water pumping cylinder 11 by pipe connecting 8; The cartridge filter 13 of fixedlying connected with loam cake 4 is arranged in liquid storage cylinder 5, on the sidewall of cartridge filter 13, filter cloth is arranged, the inner chamber of described cartridge filter 13 has a chamber at least, in chamber, there are extraction pipe and filter cloth backwash pipe correspondence to be connected bleeding point 2 corresponding on the loam cake 4 and filter cloth backwash mouth 3 with each chamber evacuation pipe and filter cloth backwash pipe, the bottom of described cartridge filter 13 is taper, the diameter of described sub-material cone 12 is less than liquid storage cylinder 5 diameters and reverse with liquid storage cylinder 5 bottom tapers, described water-in 6 and opening for feed 17 positions in cartridge filter 13 cones and liquid storage cylinder 5 between the sub-material cone 12, water-in 6 that tangentially enters in addition in the middle and upper part of described liquid storage cylinder 5 sidewalls and the water outlet 14 that tangentially enters.
During work, the vacuum pump that startup links to each other with bleeding point 2, make in the cartridge filter 13 and remain vacuum environment, opening for feed 17 tangentially enters liquid storage cylinder 5 from liquid storage cylinder 5 sidewalls, the water-in 6 tangent with liquid storage cylinder 5 sidewalls is connected with the recirculated water pump outlet, water port 7 one ends are communicated with the water pumping cylinder 11 that is positioned at sub-material cone 12 belows by pipe connecting 8, the other end of water port 7 is connected with the inlet of water circulating pump, this structure has been strengthened the rotational flow of liquid in the liquid storage cylinder 5, suspended substance in the sewage moves down in the bottom cone rotation of the drive lower edge of eddy flow liquid storage cylinder 5, last concentrated solution is pooled to cone base, reach when setting concentration requirement, by automatic control device control discharging automatically, the clarified liq after the filtration is discharged cartridge filter 13 by bleeding point 2.
After work for some time, if the liquid outlet quantity of bleeding point 2 ends reduces, the filter cloth that shows cartridge filter 13 sidewalls is blocked, needing to open the water pump or the air compressor pump that join with filter cloth backwash mouth 3 cleans, the water pump or the air compressor pump startup of joining with filter cloth backwash mouth 3 in one of them chamber are begun to clean, all the other chamber works better, after finishing, this chamber clean cleans the another one chamber again, wash cycles like this, so both can guarantee the continuity of operation, can keep the stable aquifer yield of bleeding point 2 ends again.
Claims (7)
1. rotary column separator, comprise support and on support, have the liquid storage cylinder of loam cake, on the sidewall of liquid storage cylinder, opening for feed is arranged, discharge outlet is arranged at the bottom at liquid storage cylinder, it is characterized in that: described liquid storage cylinder is the right cylinder that taper is arranged at the bottom, this liquid storage cylinder and loam cake constitute airtight pressurized vessel, on the sidewall of liquid storage cylinder, also have water-in, water outlet and water port, above described liquid storage cylinder inner cone, the sub-material cone is arranged, there is water pumping cylinder sub-material cone below, and described water port is connected with water pumping cylinder by pipe connecting; The cartridge filter of fixedlying connected with loam cake is arranged in liquid storage cylinder, on the sidewall of cartridge filter, filter cloth is arranged, the inner chamber of described cartridge filter has a chamber at least, has extraction pipe and filter cloth backwash pipe correspondence to be connected in chamber and covers bleeding point corresponding with each chamber evacuation pipe and filter cloth backwash pipe and filter cloth backwash mouth.
2. rotary column separator according to claim 1 is characterized in that: the bottom of described cartridge filter is taper.
3. rotary column separator according to claim 1 and 2 is characterized in that: the diameter of described sub-material cone is less than liquid storage cylinder diameter and reverse with liquid storage cylinder bottom taper.
4. rotary column separator according to claim 1 is characterized in that: the opening for feed on the described liquid storage cylinder sidewall, water-in are for tangentially entering.
5. rotary column separator according to claim 4 is characterized in that: described water-in and opening for feed position are in cartridge filter cone and liquid storage cylinder between the sub-material cone.
6. rotary column separator according to claim 5 is characterized in that: water-in that tangentially enters in addition in the middle and upper part of described liquid storage cylinder sidewall and the water outlet that tangentially enters.
7. rotary column separator according to claim 1 is characterized in that: the water port on the described liquid storage cylinder sidewall is that vertical direction enters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200238645U CN201261729Y (en) | 2008-06-13 | 2008-06-13 | Rotary tower separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200238645U CN201261729Y (en) | 2008-06-13 | 2008-06-13 | Rotary tower separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201261729Y true CN201261729Y (en) | 2009-06-24 |
Family
ID=40808200
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200238645U Expired - Fee Related CN201261729Y (en) | 2008-06-13 | 2008-06-13 | Rotary tower separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201261729Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101314489A (en) * | 2008-06-13 | 2008-12-03 | 孙成义 | Rotary tower separator |
| CN102728120A (en) * | 2012-07-14 | 2012-10-17 | 通化市五一环保科技股份有限公司 | Self-flushing and self-blowing water-gas two-purpose rotational flow filter |
| CN115300970A (en) * | 2022-07-25 | 2022-11-08 | 北京加隆工程机械有限公司 | Zero-discharge treatment device for waste water of asphalt mixing plant |
-
2008
- 2008-06-13 CN CNU2008200238645U patent/CN201261729Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101314489A (en) * | 2008-06-13 | 2008-12-03 | 孙成义 | Rotary tower separator |
| CN101314489B (en) * | 2008-06-13 | 2014-04-30 | 孙成义 | Rotary column separator |
| CN102728120A (en) * | 2012-07-14 | 2012-10-17 | 通化市五一环保科技股份有限公司 | Self-flushing and self-blowing water-gas two-purpose rotational flow filter |
| CN102728120B (en) * | 2012-07-14 | 2015-08-05 | 北京五一环保科技股份有限公司 | From punching, boast, water and gas dual-purpose spiral-flow filter |
| CN115300970A (en) * | 2022-07-25 | 2022-11-08 | 北京加隆工程机械有限公司 | Zero-discharge treatment device for waste water of asphalt mixing plant |
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| C14 | Grant of patent or utility model | ||
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Effective date of registration: 20090805 Pledge (preservation): Preservation |
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| PD01 | Discharge of preservation of patent |
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| PP01 | Preservation of patent right |
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| PP01 | Preservation of patent right |
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| RINS | Preservation of patent right or utility model and its discharge | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090624 Termination date: 20110613 |