CN201578998U - Double ultrafiltration membrane series connected mounting system - Google Patents
Double ultrafiltration membrane series connected mounting system Download PDFInfo
- Publication number
- CN201578998U CN201578998U CN2009202854608U CN200920285460U CN201578998U CN 201578998 U CN201578998 U CN 201578998U CN 2009202854608 U CN2009202854608 U CN 2009202854608U CN 200920285460 U CN200920285460 U CN 200920285460U CN 201578998 U CN201578998 U CN 201578998U
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- milipore filter
- ultrafiltration membrane
- series
- milipore
- filter
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Abstract
The utility model relates to a double ultrafiltration membrane series connected mounting system, comprising a first ultrafiltration membrane, a second ultrafiltration membrane, a third ultrafiltration membrane and a fourth ultrafiltration membrane. The double ultrafiltration membrane series connected mounting system is characterized in that the second end of the first ultrafiltration membrane and the first end of the second ultrafiltraion membrane are connected in series by using pipelines, the second end of the third ultrafiltraion membrane and the first end of the fourth ultrafiltration membrane are connected in series by using the pipelines, the first end of the first ultrafiltration membrane is connected in parallel with the first end of the third ultrafiltration membrane by using the pipelines, and the second end of the second ultrafiltration membrane is connected in parallel with the second end of the fourth ultrafiltration membrane by using the pipelines. The double ultrafiltration membrane series connected mounting system can achieve the purpose of energy-saving running by adopting double ultrafiltraiton membrane series connected mounting and operation technique, the water supply amount of a raw material water supply pump is only 1/2 of the prior art, so that the capacity of the water pump is reduced, the energy consumption is accordingly reduced, and simultaneously, the investment of equipment is reduced.
Description
Technical field
The utility model relates to the energy-conservation installation and operation method of a kind of milipore filter, specifically a kind of two systems that are installed in series of milipore filter.
Background technology
Milipore filter is a kind of film material, and when the pressure-driven material liquid tangentially flowed on face, solvent in the material liquid and little solute particle saw through film.The liquid that sees through film is called through liquid, and the material that can not see through film discharges with material liquid, and this part liquid is called concentrate.Overall process is the isolation technics of film.
It is lower that milipore filter is withstand voltage, and the former capital adopts single film to be installed in parallel, as shown in Figure 1, when the film number increased, the material liquid flow also increased thereupon, and the infusion pump of material liquid is dilatation thereupon also, so not only the water pump price increases, and operation energy consumption is surge thereupon also, has improved enterprise investment and production cost simultaneously.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of equipment investment few, two operation methods that are installed in series of energy-conservation milipore filter.
The technical scheme that provides according to the utility model, a kind of two systems that are installed in series of milipore filter, comprise first milipore filter, second milipore filter, the 3rd milipore filter, the 4th milipore filter, it is characterized in that: second end of first milipore filter and first end of second milipore filter utilize pipeline to be connected in series, first end of the 3rd milipore filter second end and the 4th milipore filter utilizes pipeline to be connected in series, first end of described first milipore filter utilizes pipeline to be connected in parallel with first end of described the 3rd milipore filter to be in the same place, and second end of described second milipore filter utilizes pipeline to be connected in parallel with second end of described the 4th milipore filter to be in the same place.
After first end of described first milipore filter and first end of described the 3rd milipore filter were connected in parallel together, first end of first milipore filter was connected with total flow meter, material liquid inlet gage, source water pump respectively successively with first end of the 3rd milipore filter; Second end of described second milipore filter links together with second end of described the 4th milipore filter and then is connected with the concentrated solution discharge meter.
Between first end of second end of described first milipore filter and described second milipore filter, be connected with dense water pressure table.
Respectively have two to see through the liquid outlet at the sidewall of described first milipore filter, second milipore filter, the 3rd milipore filter, the 4th milipore filter, described see through the liquid outlet and utilize pipeline to link together after, and see through the flow quantity meter and be connected.
The utility model adopts two of milipore filters to be installed in series and running technology, can reach the purpose of energy-saving run, and the output of raw water transfer pump only is 1/2 of a prior art, and the water pump capacity reduces, and energy consumption decreases, and has reduced the investment of equipment simultaneously.
Description of drawings
Fig. 1 is installed in parallel system schematic for the list of prior art props up film.
Fig. 2 is a structural representation of the present utility model.
The specific embodiment
As shown in Figure 2: two the systems of being installed in series of milipore filter comprise first milipore filter 1, second milipore filter 2, the 3rd milipore filter 3, the 4th milipore filter 4, material liquid inlet gage 5, dense water pressure table 6, total flow meter 7, see through flow quantity meter 8, concentrated solution discharge meter 9, source water pump 10 etc.
Wherein, first end of second end of first milipore filter 1 and second milipore filter 2 utilizes pipeline to be connected in series, first end of second end of the 3rd milipore filter 3 and the 4th milipore filter 4 utilizes pipeline to be connected in series, first end of first end of described first milipore filter 1 and described the 3rd milipore filter 3 utilizes pipeline to be connected in parallel to be in the same place, and second end of second end of described second milipore filter 2 and described the 4th milipore filter 4 utilizes pipeline to be connected in parallel to be in the same place.
After first end of first end of described first milipore filter 1 and described the 3rd milipore filter 3 was connected in parallel together, first end of first end of first milipore filter 1 and the 3rd milipore filter 3 was connected with total flow meter 7, material liquid inlet gage 5, source water pump 10 respectively successively; After linking together, second end of second end of described second milipore filter 2 and described the 4th milipore filter 4 is connected with concentrated solution discharge meter 9.
Between first end of second end of described first milipore filter 1 and described second milipore filter 2, be connected with dense water pressure table 6.
Respectively have two to see through the liquid outlet at the sidewall of described first milipore filter 1, second milipore filter 2, the 3rd milipore filter 3, the 4th milipore filter 4, described see through the liquid outlet and utilize pipeline to link together after, and see through flow quantity meter 8 and be connected.
Behind the utility model installation and operation, the water inlet of the raw material of second milipore filter 2 utilizes the dense water of water outlet of first milipore filter 1, and the raw material water inlet of the 4th milipore filter 4 utilizes the dense water of water outlet of the 3rd milipore filter 3, has changed the technology that raw water is advanced in existing milipore filter parallel connection respectively.
Because the raw water that enters second milipore filter 2 has utilized the dense water of first milipore filter 1, the raw water of the 4th milipore filter 4 has utilized the dense water of the 3rd milipore filter 3, so the output of the utility model source water pump 10 only is 1/2 of a present technology, water pump 10 capacity in source reduce, energy consumption decreases, and the price of source water pump 10 is also low simultaneously.
Claims (4)
1. two systems that are installed in series of a milipore filter, comprise first milipore filter (1), second milipore filter (2), the 3rd milipore filter (3), the 4th milipore filter (4), it is characterized in that: first end of second end of first milipore filter (1) and second milipore filter (2) utilizes pipeline to be connected in series, first end of the 3rd milipore filter (3) second ends and the 4th milipore filter (4) utilizes pipeline to be connected in series, first end of first end of described first milipore filter (1) and described the 3rd milipore filter (3) utilizes pipeline to be connected in parallel to be in the same place, and second end of second end of described second milipore filter (2) and described the 4th milipore filter (4) utilizes pipeline to be connected in parallel to be in the same place.
3. two systems that are installed in series of milipore filter as claimed in claim 1, it is characterized in that: after first end of first end of described first milipore filter (1) and described the 3rd milipore filter (3) was connected in parallel together, first end of first end of first milipore filter (1) and the 3rd milipore filter (3) was connected with total flow meter (7), material liquid inlet gage (5), source water pump (10) respectively successively; After linking together, second end of second end of described second milipore filter (2) and described the 4th milipore filter (4) is connected with concentrated solution discharge meter (9).
4. two systems that are installed in series of milipore filter as claimed in claim 1 is characterized in that: be connected with dense water pressure table (6) between first end of second end of described first milipore filter (1) and described second milipore filter (2).
5. two systems that are installed in series of milipore filter as claimed in claim 1, it is characterized in that: the sidewall at described first milipore filter (1), second milipore filter (2), the 3rd milipore filter (3), the 4th milipore filter (4) respectively has two to see through the liquid outlet, described see through the liquid outlet and utilize pipeline to link together after, and see through flow quantity meter (8) and be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202854608U CN201578998U (en) | 2009-12-29 | 2009-12-29 | Double ultrafiltration membrane series connected mounting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202854608U CN201578998U (en) | 2009-12-29 | 2009-12-29 | Double ultrafiltration membrane series connected mounting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201578998U true CN201578998U (en) | 2010-09-15 |
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ID=42720990
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202854608U Expired - Fee Related CN201578998U (en) | 2009-12-29 | 2009-12-29 | Double ultrafiltration membrane series connected mounting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201578998U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109562964A (en) * | 2016-08-24 | 2019-04-02 | 奥加诺株式会社 | Ultrapure water production device |
-
2009
- 2009-12-29 CN CN2009202854608U patent/CN201578998U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109562964A (en) * | 2016-08-24 | 2019-04-02 | 奥加诺株式会社 | Ultrapure water production device |
| CN109562964B (en) * | 2016-08-24 | 2021-11-05 | 奥加诺株式会社 | Ultrapure water production equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: JIANGSU SHUANGJING CLEANSING TECHNOLOGY CO., LTD. Free format text: FORMER NAME: WUXI SHUANGJING CLEANSING EQUIPMENT CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 214123 women's street, Binhu District, Jiangsu, Wuxi, 6 Patentee after: Jiangsu Shuangjing Purification Technology Co., Ltd. Address before: 214123 women's street, Binhu District, Jiangsu, Wuxi, 6 Patentee before: Wuxi Shuangjing Purification Equipment Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100915 Termination date: 20141229 |
|
| EXPY | Termination of patent right or utility model |