CN2477641Y - Refrigerant filter - Google Patents
Refrigerant filter Download PDFInfo
- Publication number
- CN2477641Y CN2477641Y CN 00252378 CN00252378U CN2477641Y CN 2477641 Y CN2477641 Y CN 2477641Y CN 00252378 CN00252378 CN 00252378 CN 00252378 U CN00252378 U CN 00252378U CN 2477641 Y CN2477641 Y CN 2477641Y
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- Prior art keywords
- contact
- pipeline valve
- heat exchanger
- road
- filter
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- Expired - Fee Related
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Abstract
The utility model discloses a cooling medium filter. An original solution container YY connects a pipe valve, a primary filter, a filter, a heat exchanger, an evaporator, a beverage pump, a filter aid container, a transparent sight drum, a refrigerator and a filtrate container in certain order by pipeline into a system. Due to the adding of the heating exchanger, the system can precool the stock solution completely with cooled and filtered solution and reduce the energy consumption. Since the heat exchanger, the evaporator, the filter and the refrigerator are assembled to form a system, the operation is simpler and more convenient.
Description
The utility model relates to a kind of Refrigerant filter, particularly a kind of Refrigerant filter that is used for low alcohol and beverage depth type filtration.
At present, the freezing and filtering that is used for low class wine is that separately to adopt large-scale refrigerating apparatus to carry out freezing, adopts filter to filter again, exists energy consumption big, and pre-cool time is long, and inconvenient operation does not have incorporate Refrigerant filter temporarily.
The purpose of this utility model is to provide a kind of energy-efficient Refrigerant filter that low class wine carries out depth type filtration that is used for.
The purpose of this utility model is to realize by the Refrigerant filter of following structure, it comprises pipeline valve F, former liquid container YY, initial filtrator CL, compressor Y, condenser L, cryogen vessel C, vaporizer SF, refrigeration agent strainer T, expansion valve B, tensimeter MP, a transparent SJ that looks, beverage pump B, heat exchanger GH, flocculating aids container C G, filtrate container LY, its former liquid container YY by intermediate conduit through pipeline valve F1 to contact J1 punishment two-way, a road of contact J1 connects the stoste entrance end of the inner coil pipe of heat exchanger GH through beverage pump BA, the stoste exit end of the inner coil pipe of heat exchanger GH connects the stoste entrance end of vaporizer SF through pipeline valve F4 by intermediate conduit, the stoste exit end of vaporizer SF by intermediate conduit through pipeline valve F7 to contact J3 punishment two-way, a road of contact J3 meets cleaning liquid inlet end Z through pipeline valve F6, another road of contact J3 is to contact J4 punishment two-way, the intermediate conduit of leading up to of contact J4 connects the exit end of flocculating aids container C G through pipeline valve F16, another road of contact J4 is through a transparent SJ2 that looks, beverage pump BB punishes three the tunnel to contact J5, a road of contact J5 connects the entrance end of flocculating aids container C G through pipeline valve F11 to contact J7, the second tunnel of contact J5 divides two-way through pipeline valve F10 to contact J6, a road of contact J6 takes over entrance end at the bottom of the stoste of filter GL, another road of contact J6 meets sewage draining exit Q through pipeline valve F12, and the Third Road of contact J5 is taken over the stoste side-entrance end of filter GL through pipeline valve F9; Another road of contact J1 by intermediate conduit through pipeline valve F2 contact J2, a road of contact J2 connects the inner vessels filtrate entrance end of heat exchanger GH through pipeline valve F3, the inner vessels filtrate outlet end of heat exchanger CH meets filtrate container LY by intermediate conduit through pipeline valve F17, another road of contact J2 is divided two-way through pipeline valve F14 to contact J8 by intermediate conduit, a road of contact J8 looks the filtrate outlet end that a SJ3 takes over filter GL through transparent, and another road of contact J8 connects the entrance end of flocculating aids container C G through contact J7 through pipeline valve F15; By refrigeration agent, compressor Y, condenser L, cryogen vessel C, refrigeration agent strainer T, expansion valve B, the refrigeration equipment that tensimeter MP4, tensimeter MP5 and pipeline are formed by intermediate conduit respectively with vaporizer SF in the entrance end and the exit end of generating tube join, form cooling cycle system and give liquid refrigerating in the vaporizer SF.Described contact J1-J8 is the pipeline position that is interconnected.Tensimeter MP1 and pipeline valve F5 are installed on the described heat exchanger GH, or tensimeter MP2 and pipeline valve F8 are installed on the vaporizer SF, or tensimeter MP3 and pipeline valve F13 are installed on the strainer GL, or its arbitrary combination is installed.Described transparent looking installed contact arbitrarily or directly connect filtrate test port by intermediate conduit through pipeline valve F19 from contact J8 between a SJ3 and the pipeline valve F14.The inner vessels of described heat exchanger GH is that the inwall of heat exchanger GH is with the vessel space beyond the inner coil pipe of interior, heat exchanger GH.Described intermediate conduit be metal tube or for non-metallic pipe or for multiple-unit tube or section of tubing be non-metallic pipe or multiple-unit tube for metal tube another part.A transparent SJ1, beverage pump BA, the initial filtrator CL of looking is installed between the stoste entrance end of the inner coil pipe of described contact J1 and heat exchanger GH, and its order can be adjusted arbitrarily.
In sum, characteristics of the present utility model are: by adding heat exchanger GH, utilize the liquid behind the freezing and filtering that stoste is carried out precooling, reduced energy consumption, become a system by heat exchanger, vaporizer, strainer and refrigeration equipment are fitted together simultaneously, make operation more easy, after all kinds of low alcohol are filtered by the native system cryogenic freezing, make its under low-temperature condition, do not have muddy, do not have precipitation, loss of gloss not, extend the shelf life.
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is a structure principle chart of the present utility model.
By Fig. 1 to Fig. 3 as can be known, former liquid container YY of the present utility model is connected with beverage pump BA, initial filtrator CL, strainer GL, heat exchanger GH, vaporizer SF, beverage pump BA, beverage pump BB, flocculating aids container C G, beverage pump BB, a transparent SJ1, SJ2, SJ3 and the filtrate container LY of looking with pipeline valve by intermediate conduit; Its workflow mainly comprises following step: promptly system's liquid feeding, system's precooling, system's internal recycle, filter working process, system's cleaning process.At first give system's liquid feeding, before liquid feeding, close pipeline valve F2, pipeline valve F6, pipeline valve F12, pipeline valve F14, pipeline valve F15, pipeline valve F16, opening conduits valve F1, pipeline valve F4, pipeline valve F7, pipeline valve F8, pipeline valve F10, pipeline valve F11, pipeline valve F13, pipeline valve F18, stoste flows out through pipeline valve F1 from former liquid container YY, beverage pump BA, strainer GL, the inner coil pipe of heat exchanger GH, pipeline valve F4, vaporizer SF, pipeline valve F7, a transparent SJ2 that looks, beverage pump BB, wherein one the tunnel through pipeline valve F11 to flocculating aids container C G, another road is through pipeline valve F10, strainer GL.Behind system's liquid feeding, system is carried out precooling, close pipeline valve F5, pipeline valve F8, pipeline valve F13, pipeline valve F18 this moment, start compressor Y, give the liquid refrigerating in the vaporizer SF; In refrigeration after specified temperature, open pipeline valve F10, pipeline valve F15, pipeline valve F16, starting beverage pump BB circulates the stoste in the filtering system, liquid stream flows out to pipeline valve F16 from flocculating aids container C G and enters strainer GL through beverage pump BB through pipeline valve F10 through a transparent SJ2 that looks, flow out to a transparent SJ3 that looks, enter flocculating aids container C G through pipeline valve F15, treat that transparent to look stoste in the SJ3 limpid or carry out cold liquid circulation in the system after pipeline valve F19 sampling stoste is up to standard, close pipeline valve F3, pipeline valve F9, pipeline valve F13, opening conduits valve F2, pipeline valve F14, liquid stream flows into a transparent SJ3 that looks from strainer GL, through pipeline valve F14, pipeline valve F2, a transparent SJ1 that looks, beverage pump BA, strainer GL enters vaporizer SF inner coil pipe, outflow is through vaporizer SF, pipeline valve F7, a transparent SJ2 that looks, beverage pump BB, pipeline valve F10 is to strainer GL, when the stoste of vaporizer SF is identical or close with former liquid temp in the strainer GL, close pipeline valve F2, opening conduits valve F3, pipeline valve F17, make system enter the filtration working process, stoste from former liquid container YY through pipeline valve pipeline valve F1, a transparent SJ1 that looks, beverage pump BA, the coil pipe of initial filtrator CL to the interchanger heat exchanger GH through pipeline valve F4 to vaporizer SF to pipeline valve F7, a transparent SJ2 that looks, beverage pump BB, pipeline valve F10, strainer GL, a transparent SJ3 that looks, pipeline valve F14, pipeline valve F3, the inner vessels of heat exchanger GH is interior through pipeline valve F17, filtrate container LY.
In the system filtration process, some impurity stick on the filter disc of strainer GL inevitably, to influence filtering benefit and effect, at this moment, must clean system, close beverage pump BA, pipeline valve F7, pipeline valve F14, pipeline valve F16, opening conduits valve F12, pipeline valve F11, pipeline valve F9, pipeline valve F6, pipeline valve F15, scavenging solution is from pipeline valve F6, a transparent SJ2 that looks, beverage pump BB, pipeline valve F9, filter disc in the washing nozzle spraywashing strainer GL in the strainer GL, pipeline valve F11, pipeline valve F15, a transparent SJ3 that looks, the interior axle back flushing filter disc of strainer GL, the impurity in the strainer GL is discharged by the bottom outlet K of strainer GL bottom and through pipeline valve F12 with scavenging solution.The workflow of filtering capable of circulation again after cleaning.
Claims (7)
1, a kind of Refrigerant filter, comprise pipeline valve F, former liquid container YY, initial filtrator CL, compressor Y, condenser L, cryogen vessel C, vaporizer SF, refrigeration agent strainer T, expansion valve B, tensimeter MP, a transparent SJ that looks, beverage pump B, heat exchanger GH, flocculating aids container C G, filtrate container LY, it is characterized in that: former liquid container YY by intermediate conduit through pipeline valve F1 to contact J1 punishment two-way, a road of contact J1 connects the stoste entrance end of the inner coil pipe of heat exchanger GH through beverage pump BA, the stoste exit end of the inner coil pipe of heat exchanger GH connects the stoste entrance end of vaporizer SF through pipeline valve F4 by intermediate conduit, the stoste exit end of vaporizer SF by intermediate conduit through pipeline valve F7 to contact J3 punishment two-way, a road of contact J3 meets cleaning liquid inlet end Z through pipeline valve F6, another road of contact J3 is to contact J4 punishment two-way, the intermediate conduit of leading up to of contact J4 connects the exit end of flocculating aids container C G through pipeline valve F16, another road of contact J4 is through a transparent SJ2 that looks, beverage pump BB punishes three the tunnel to contact J5, a road of contact J5 connects the entrance end of flocculating aids container C G through pipeline valve F11 to contact J7, the second tunnel of contact J5 divides two-way through pipeline valve F10 to contact J6, a road of contact J6 takes over entrance end at the bottom of the stoste of filter GL, another road of contact J6 meets sewage draining exit Q through pipeline valve F12, and the Third Road of contact J5 is taken over the stoste side-entrance end of filter GL through pipeline valve F9; Another road of contact J1 by intermediate conduit through pipeline valve F2 contact J2, a road of contact J2 connects the inner vessels filtrate entrance end of heat exchanger GH through pipeline valve F3, the inner vessels filtrate outlet end of heat exchanger GH meets filtrate container LY by intermediate conduit through pipeline valve F17, another road of contact J2 is divided two-way through pipeline valve F14 to contact J8 by intermediate conduit, a road of contact J8 looks the filtrate outlet end that a SJ3 takes over filter GL through transparent, and another road of contact J8 connects the entrance end of flocculating aids container C G through contact J7 through pipeline valve F15; By refrigeration agent, compressor Y, condenser L, cryogen vessel C, refrigeration agent strainer T, expansion valve B, the refrigeration equipment that tensimeter MP4, tensimeter MP5 and pipeline are formed by intermediate conduit respectively with vaporizer SF in the entrance end and the exit end of generating tube join, form cooling cycle system and give liquid refrigerating in the vaporizer SF.
2, according to the described Refrigerant filter of claim 1, it is characterized in that: described contact J1-J8 is the pipeline position that is interconnected, and contact J3 and contact J4 are merged into a contact.
3, according to the described Refrigerant filter of claim 1, it is characterized in that: tensimeter MP1 and pipeline valve F5 are installed on the described heat exchanger GH, or tensimeter MP2 and pipeline valve F8 are installed on the vaporizer SF, or tensimeter MP3 and pipeline valve F13 are installed on the strainer GL, or its arbitrary combination is installed.
4, according to the described Refrigerant filter of claim 1, it is characterized in that: described transparent looking installed contact arbitrarily or directly connect filtrate test port by intermediate conduit through pipeline valve F19 from contact J8 between a SJ3 and the pipeline valve F14.
5, according to the described Refrigerant filter of claim 1, it is characterized in that: the inner vessels of described heat exchanger GH is that the inwall of heat exchanger GH is with the vessel space beyond the inner coil pipe of interior, heat exchanger GH.
6, according to the described Refrigerant filter of claim 1, it is characterized in that: described intermediate conduit be metal tube or for non-metallic pipe or for multiple-unit tube or section of tubing be non-metallic pipe or multiple-unit tube for metal tube another part.
7, according to the described Refrigerant filter of claim 1, it is characterized in that: a transparent SJ1, beverage pump BA, the initial filtrator CL of looking is installed between the stoste entrance end of the inner coil pipe of described contact J1 and heat exchanger GH, and its order can be adjusted arbitrarily.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00252378 CN2477641Y (en) | 2000-12-27 | 2000-12-27 | Refrigerant filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00252378 CN2477641Y (en) | 2000-12-27 | 2000-12-27 | Refrigerant filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2477641Y true CN2477641Y (en) | 2002-02-20 |
Family
ID=33610047
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00252378 Expired - Fee Related CN2477641Y (en) | 2000-12-27 | 2000-12-27 | Refrigerant filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2477641Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109876519A (en) * | 2019-02-22 | 2019-06-14 | 高云芝 | A kind of freezing and filtering unit of helpless filter medium |
| CN115678731A (en) * | 2022-11-09 | 2023-02-03 | 湘潭林海机械制造有限公司 | Double-mode large-temperature-difference freezing filter unit |
-
2000
- 2000-12-27 CN CN 00252378 patent/CN2477641Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109876519A (en) * | 2019-02-22 | 2019-06-14 | 高云芝 | A kind of freezing and filtering unit of helpless filter medium |
| CN109876519B (en) * | 2019-02-22 | 2021-11-30 | 高云芝 | Freezing filter unit without filter aid medium |
| CN115678731A (en) * | 2022-11-09 | 2023-02-03 | 湘潭林海机械制造有限公司 | Double-mode large-temperature-difference freezing filter unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |