CN203355404U - Clear filtrate and turbid filtrate separating device - Google Patents
Clear filtrate and turbid filtrate separating device Download PDFInfo
- Publication number
- CN203355404U CN203355404U CN 201320377563 CN201320377563U CN203355404U CN 203355404 U CN203355404 U CN 203355404U CN 201320377563 CN201320377563 CN 201320377563 CN 201320377563 U CN201320377563 U CN 201320377563U CN 203355404 U CN203355404 U CN 203355404U
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- filtrate
- turbid
- clear
- drainpipe
- press filter
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Abstract
The utility model relates to a clear filtrate and turbid filtrate separating device which comprises press filter plates, wherein free flow discharge pipes are arranged in front of the press filter plates in positions close to the bottom ends of the press filter plates and connected with a filtrate receiving tank below the free flow discharge pipes; subterranean flow discharge pipes are arranged on the left side of the press filter plates and connected with a filtrate collecting tank below the subterranean flow discharge pipes; the filtrate collecting tank is communicated with the filtrate receiving tank; a filtrate discharge pipe I and a filtrate discharge pipe II are respectively arranged at the bottom end of one side surface of the filtrate collecting tank; the filtrate collecting tank is connected with the clean filtrate tank through the filtrate discharge pipe I and connected with a filtrate tank through the filtrate discharge pipe II; a filtrate turbidity detector is connected into the filtrate collecting tank and connected with a software control system. The clear filtrate and turbid filtrate separating device has the benefits of realizing clear filtrate and turbid filtrate separation, staged discharge and recycle of clear filtrate and turbid filtrate, saving resources, lowering cost, realizing closed cycle, avoiding sewage discharge, achieving automation in system operation and simplicity in operation, and saving time and labor.
Description
Technical field
The utility model relates to the solid-liquid separating equipment technical field, relates in particular to a kind of pure and impure separator.
Background technology
Filter press the earliest only has the free flow drainage structure or only has the undercurrent drainage structure, and present most filter press has free flow drainage structure and undercurrent drainage structure, but these two kinds of fluid-discharge methods are all simply filtrate to be collected, then filtrate discharge.Filter press does not in the market also have to realize the clear, turbid separating treatment of filtrate, filtrate directly is discharged, clear liquid is polluted by turbid liquid, most of filtrate is also quite muddy when discharge, both contaminated environment, waste again resource, and its discharge filtrate subsequent treatment work not only measure greatly, difficulty is also large.
The utility model content
The purpose of this utility model is to provide a kind of pure and impure separator, to overcome currently available technology, exists pure and impure solution separating difficulty large, causes environmental pollution, the deficiencies such as the wasting of resources.
The purpose of this utility model is to be achieved through the following technical solutions:
A kind of pure and impure separator, comprise filter press filter board, described filter press filter board front is provided with the free flow discharging tube by positon of near bottom, free flow discharging tube below is connected with water receiving tank, the filter press filter board left side is provided with the undercurrent discharging tube, undercurrent discharging tube below is connected with the filtrate collection and deposits case, the filtrate collection is deposited case and is communicated with water receiving tank, described filtrate collection is deposited bottom, case side and is respectively equipped with filtrate drainpipe one and filtrate drainpipe two, described filtrate collection is deposited case and is connected with clear water reserviors by filtrate drainpipe one, described filtrate collection is deposited case and is connected with the filtrate pond by filtrate drainpipe two, described filtrate collection is deposited in case and is connected with filtrate turbidity detector, filtrate turbidity detector is connected with software control system.
Further, described filtrate drainpipe one is provided with Clean water valve; Described filtrate drainpipe two is provided with the muddy water valve.
Further, described Clean water valve all is connected with software control system with the muddy water valve.
The beneficial effects of the utility model are: the utility model has been realized the pure and impure separation of filtrate, classified emission; Clear filtrate can realize that clear filtrate utilizes again for cleaning the processes such as filter cloth, equipment surface dust, factory building, economizes on resources, and reduces costs; Turbid filtrate is returned to filtration system, is again filtered, and has realized closed cycle, has avoided wastewater disposition, strengthens corporate environment and social benefit; Automated system operation, simple to operate, saving of work and time.
The accompanying drawing explanation
Below with reference to the accompanying drawings the utility model is described in further detail.
Fig. 1 is the structural representation of the described a kind of pure and impure separator of the utility model embodiment.
In figure:
1, free flow discharging tube; 2, undercurrent discharging tube; 3, water receiving tank; 4, the filtrate collection is deposited case; 5, the filtrate drainpipe two; 6, Clean water valve; 7, muddy water valve; 8, filtrate turbidity detector; 9, software control system; 10, clear water reserviors; 11, filtrate pond; 12, the filtrate drainpipe one; 13, filter press filter board.
The specific embodiment
As shown in Figure 1, the described a kind of pure and impure separator of the utility model embodiment, comprise filter press filter board 13, described filter press filter board 13 fronts are provided with free flow discharging tube 1 by positon of near bottom, free flow discharging tube 1 below is connected with water receiving tank 3, described filter press filter board 13 left sides are provided with undercurrent discharging tube 2, undercurrent discharging tube 2 belows are connected with the filtrate collection and deposit case 4, the filtrate collection is deposited case 4 and is communicated with water receiving tank 3, described filtrate collection is deposited case 4 bottoms, side and is respectively equipped with filtrate drainpipe 1 and filtrate drainpipe 25, described filtrate collection is deposited case 4 and is connected with clear water reserviors 10 by filtrate drainpipe 1, described filtrate collection is deposited case 4 and is connected with filtrate pond 11 by filtrate drainpipe 25, described filtrate collection is deposited in case 4 and is connected with filtrate turbidity detector 8, filtrate turbidity detector 8 is connected with software control system 9, described filtrate drainpipe 1 is provided with Clean water valve 6, described filtrate drainpipe 25 is provided with muddy water valve 7, described Clean water valve 6 all is connected 9 with software control system with muddy water valve 7.
During concrete the use, filtrate is flowed out from free flow discharging tube 1 and undercurrent discharging tube 2, and wherein the filtrate in free flow discharging tube 1 is discharged in water receiving tank 3, then flows into the filtrate collection and deposits in case 4; Filtrate in undercurrent discharging tube 2 directly is discharged to the filtrate collection and deposits in case 4.Now filtrate turbidity detector 8 is monitored the concentration that the filtrate collection is deposited filtrate in case 4 always, and testing result is sent to software control system 9 carries out the signal processing.The filter liquor concentration value detected when filtrate turbidity detector 8 is higher, and during higher than the artificial filter liquor concentration value of setting, software control system 9 judges that now filtrate is turbid filtrate, and sends command signal, and 7 unlatchings of muddy water valve, Clean water valve 6 are closed.The filtrate that now the filtrate collection is deposited in case 4 is expelled to filtrate pond 11 along the filtrate drainpipe 25 that muddy water valve 7 is housed, and continues to enter impulse stroke next time.Turbid filtrate forms closed cycle thus, free from environmental pollution.The filter liquor concentration value detected when filter liquor concentration detector 8 is lower, and during lower than the artificial filter liquor concentration value of setting, software control system 9 judges that now filtrate is clear filtrate, and sends command signal, and Clean water valve 6 unlatchings, muddy water valve 7 are closed.The filtrate that now the filtrate collection is deposited in case 4 is expelled to clear water reserviors 10 along the filtrate drainpipe 1 that Clean water valve 6 is housed.Clear water in clear water reserviors 10 can be for rinsing the processes such as filter cloth, equipment surface dust, factory building and hydraulic pressure press for extracting juice, and historical facts or anecdotes has showed the utilization again of clear filtrate, economizes on resources, reduce costs, and automated system operation, simple to operate, saving of work and time.
The utility model is not limited to above-mentioned preferred forms; anyone can draw other various forms of products under enlightenment of the present utility model; no matter but do any variation on its shape or structure; every have identical with a application or akin technical scheme, within all dropping on protection domain of the present utility model.
Claims (4)
1. a pure and impure separator, comprise filter press filter board (13), it is characterized in that: described filter press filter board (13) front is provided with free flow discharging tube (1) by positon of near bottom, free flow discharging tube (1) below is connected with water receiving tank (3), described filter press filter board (13) left side is provided with undercurrent discharging tube (2), undercurrent discharging tube (2) below is connected with the filtrate collection and deposits case (4), the filtrate collection is deposited case (4) and is communicated with water receiving tank (3), described filtrate collection is deposited case (4) bottom, side and is respectively equipped with filtrate drainpipe one (12) and filtrate drainpipe two (5), described filtrate collection is deposited case (4) and is connected with clear water reserviors (10) by filtrate drainpipe one (12), described filtrate collection is deposited case (4) and is connected with filtrate pond (11) by filtrate drainpipe two (5), described filtrate collection is deposited in case (4) and is connected with filtrate turbidity detector (8), filtrate turbidity detector (8) is connected with software control system (9).
2. pure and impure separator according to claim 1, it is characterized in that: described filtrate drainpipe one (12) is provided with Clean water valve (6).
3. pure and impure separator according to claim 2, it is characterized in that: described filtrate drainpipe two (5) is provided with muddy water valve (7).
4. pure and impure separator according to claim 3, it is characterized in that: described Clean water valve (6) all is connected (9) with muddy water valve (7) with software control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320377563 CN203355404U (en) | 2013-06-28 | 2013-06-28 | Clear filtrate and turbid filtrate separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320377563 CN203355404U (en) | 2013-06-28 | 2013-06-28 | Clear filtrate and turbid filtrate separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203355404U true CN203355404U (en) | 2013-12-25 |
Family
ID=49803230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320377563 Expired - Fee Related CN203355404U (en) | 2013-06-28 | 2013-06-28 | Clear filtrate and turbid filtrate separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203355404U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649404A (en) * | 2015-03-03 | 2015-05-27 | 上海城投污水处理有限公司石洞口污水处理厂 | System and method for accurately controlling discharge of treated sewage |
| CN113735310A (en) * | 2021-08-29 | 2021-12-03 | 南京宝地梅山产城发展有限公司 | Clean water and turbid water separation process |
| CN114432753A (en) * | 2022-03-22 | 2022-05-06 | 景津装备股份有限公司 | Device for dynamically shunting clear and turbid filtrate and open-flow filter press liquid collection and separation mechanism |
-
2013
- 2013-06-28 CN CN 201320377563 patent/CN203355404U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649404A (en) * | 2015-03-03 | 2015-05-27 | 上海城投污水处理有限公司石洞口污水处理厂 | System and method for accurately controlling discharge of treated sewage |
| CN113735310A (en) * | 2021-08-29 | 2021-12-03 | 南京宝地梅山产城发展有限公司 | Clean water and turbid water separation process |
| CN113735310B (en) * | 2021-08-29 | 2024-01-09 | 南京宝地梅山产城发展有限公司 | Clear water and turbid water separation process |
| CN114432753A (en) * | 2022-03-22 | 2022-05-06 | 景津装备股份有限公司 | Device for dynamically shunting clear and turbid filtrate and open-flow filter press liquid collection and separation mechanism |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Beijing ZSC Filter Co., Ltd. Assignor: China wins (Beijing) Electromechanical Equipment Co., Ltd. Contract record no.: 2014990000459 Denomination of utility model: Clear filtrate and turbid filtrate separating device Granted publication date: 20131225 License type: Exclusive License Record date: 20140626 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131225 Termination date: 20160628 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |