CN203778390U - CIP in-place cleaning system - Google Patents
CIP in-place cleaning system Download PDFInfo
- Publication number
- CN203778390U CN203778390U CN201420165777.9U CN201420165777U CN203778390U CN 203778390 U CN203778390 U CN 203778390U CN 201420165777 U CN201420165777 U CN 201420165777U CN 203778390 U CN203778390 U CN 203778390U
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- Prior art keywords
- tank
- concentrated
- thinning tank
- concentrated acid
- pipeline
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- Expired - Fee Related
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Abstract
The utility model relates to an equipment cleaning device, in particular to a CIP in-place cleaning system, which comprises a concentrated acid tank, a concentrated alkaline tank, a concentrated acid thinning tank and a concentrated alkaline thinning tank, wherein the concentrated acid tank is connected with the concentrated acid thinning tank through a pipeline, and the concentrated alkaline tank is connected with the concentrated alkaline thinning tank through a pipeline. The CIP in-place cleaning system is characterized in that the concentrated acid thinning tank and the concentrated alkaline thinning tank are respectively connected with a plate type heat exchanger through pipelines, the plate type heat exchanger is connected with a to-be-cleaned device through a pipeline, and the to-be-cleaned device is connected with the concentrated acid thinning tank and the concentrated alkaline thinning tank through pipelines respectively. The CIP in-place cleaning system has the advantages that 1, cleaning liquid can be reused; 2, the plate type heat exchanger is high in heating speed and good in heat exchange effect; 3, a sprinkling device is connected with a water tank, and the cleaning is convenient; 4, a pneumatic diaphragm pump is suitable for being applied to concentrated acid and concentrated alkaline.
Description
Technical field
The utility model relates to a kind of equipment cleaning device, specifically a kind of CIP purging system in place.
Background technology
CIP purging system in place is at decomposition production equipment not, again the clean device that equipment is cleaned of available shirtsleeve operation method safety.
Publication number is CN203343113U, within open day, be on December 18th, 2013 name be called the Chinese utility model patent of novel C IP purging system, it is low that a kind of solution CIP purging system cleaning efficiency is disclosed, the problem that cleaning performance is poor, the problem that this patent exists is: 1) with steam, sour tank, alkali tank are heated, heat time is long, and efficiency is low; 2) cannot effectively clean sour tank, alkali tank; 3) cleaning fluid cannot recycle, and causes waste.
Utility model content
The utility model provides a kind of CIP addressing the above problem purging system in place.
The concrete technical scheme adopting of the utility model is:
CIP purging system in place, comprise concentrated acid tank, concentrated base tank, concentrated acid thinning tank, concentrated base thinning tank, concentrated acid tank is connected with concentrated acid thinning tank pipeline, being connected with concentrated base thinning tank pipeline of concentrated base tank, it is characterized in that, concentrated acid thinning tank, concentrated base thinning tank are connected with plate type heat exchanger by pipeline respectively, and plate type heat exchanger is connected with device to be cleaned by pipeline, and device to be cleaned is connected with concentrated acid thinning tank, concentrated base thinning tank by pipeline.Cleaning fluid in concentrated acid thinning tank, concentrated base thinning tank can reach rapidly temperature requirement by plate type heat exchanger heat exchange, cleaning fluid after cleaning can be got back in concentrated acid thinning tank, concentrated base thinning tank, realizing cleaning fluid recycles, concentrated acid tank, concentrated base pot liquid constantly can be added to concentrated acid thinning tank, concentrated base thinning tank for maintaining concentration, underproof cleaning fluid after testing, can be from concentrated acid thinning tank, concentrated base thinning tank safety dumping.
Wherein, also comprise water pot, water pot is connected with the spray equipment at concentrated acid tank, concentrated base tank, concentrated acid thinning tank, concentrated base thinning tank top respectively, and water pot is also connected with heat exchanger.After cleaning at cleaning fluid, facilitate water to clean and be also provided with water pot cleaning equipment, water in water pot can also clean it by the spray equipment at concentrated acid tank, concentrated base tank, concentrated acid thinning tank, concentrated base thinning tank top, solved prior art and cleaned difficult problem, spray equipment can be devices spraying head type or other applicable spray structures.
Wherein, between described concentrated acid tank and concentrated acid thinning tank and between concentrated base tank and concentrated base thinning tank, be respectively equipped with pneumatic diaphragm pump.
Wherein, described pipeline is provided with tubing pump, also has flowmeter, temperature sensor on pipeline, between each parts of described pipeline, is provided with hand-operated valve, pneumatic operated valve.
Native system is controlled by control system, control system comprises host computer, slave computer, host computer has adopted touch-screen as man-machine control interface, capable of dynamic shows the parameters such as temperature in workflow and the course of work, liquid level, time, make operation more directly perceived, convenient, user also can carry out as required special configuration and carry out easily manual operation.In good time data automatically show on touch-screen display, and can store at any time, and are furnished with mini-printer and print parameters of operation process record in order to inquiry; Slave computer has adopted Modern New control device-Siemens programmable controller to carry out programme-control, has function strong, and reliability is high, uses the features such as flexible.Pneumatic operated valve between each parts of tubing pump, flowmeter, temperature sensor, described pipeline all has control system control.
Concentrated acid tank in native system, concentrated base tank adopt 022Cr17Ni12Mo2 material, adopt 316L all steel material, compared with original water treatment system tank body, and nitric acid and NaOH corrosion that can resisting high-concentration.
Concentrated acid thinning tank, concentrated base thinning tank adopt the design of 06Cr19Ni10 stainless steel, with liquid level gauge and temperature detection mouth.
All pipelines are welding procedure, guarantee without leaking.
Compared with prior art, the utility model has the advantages that:
1) cleaning fluid can be recycled, and reduces waste liquid; 2) plate type heat exchanger firing rate is fast, good effect of heat exchange; 3) spray equipment is connected with water pot, easy to clean; 4) pneumatic diaphragm pump is applicable to concentrated acid, concentrated base uses.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
In figure, 1, concentrated acid tank, 2, concentrated base tank, 3, concentrated acid thinning tank, 4, concentrated base thinning tank, 5, pneumatic diaphragm pump, 6, plate type heat exchanger, 7, device to be cleaned, 8, water pot, 9, tubing pump.
Detailed description of the invention
CIP purging system in place, concentrated acid tank 1 is connected by the pneumatic diaphragm pump 5 being located on pipeline with concentrated acid thinning tank 3, concentrated base tank 2 is connected by the pneumatic diaphragm pump 5 being located on pipeline with concentrated base thinning tank 4, concentrated acid thinning tank 3, concentrated base thinning tank 4 are connected with plate type heat exchanger 6 by pipeline respectively, plate type heat exchanger 6 is connected with device 7 to be cleaned by pipeline, and device 7 to be cleaned is connected with concentrated acid thinning tank 3, concentrated base thinning tank 4 by pipeline; Also be provided with the water pot 8 being connected with the spray equipment at concentrated acid tank 1, concentrated base tank 2, concentrated acid thinning tank 3, concentrated base thinning tank 4 tops respectively, water pot 8 is also connected with plate type heat exchanger 6, on the pipeline of plate type heat exchanger 6 front ends, be provided with tubing pump 9, the pipeline of plate type heat exchanger 6 rear ends is provided with conductivity gauge, flowmeter, temperature sensor, between all parts, be provided with hand-operated valve, pneumatic operated valve, pneumatic operated valve is connected with control system.
The course of work
Concentrated acid, concentrated base enter concentrated acid tank, concentrated base tank through pump, then entering concentrated acid thinning tank, concentrated base thinning tank by pneumatic diaphragm pump, water in water pot is input to concentrated acid thinning tank, concentrated base thinning tank and carries out concentrated acid, concentrated base dilution, then heat by plate type heat exchanger, treating cleaning device cleans again, cleaning fluid after cleaning, getting back in concentrated acid thinning tank, concentrated base thinning tank, carries out next one circulation.After cleaning finishes, if purging system needs to rinse, open water pot switch, the concentrated acid tank, concentrated base tank, concentrated acid thinning tank, the concentrated base thinning tank that complete cleaning are cleaned by spray equipment, cleaning fluid is drained, enter holding state, wait for next cleaning process automatically.In cleaning process, system carries conductivity gauge and temperature sensor, regulates normal-temperature water and the proportioning of concentrated acid concentrated base and the circulation of acid & alkali liquid to heat up by signal feedback.Treat that acid-base value and temperature reach system requirements, enter the equipment that needs cleaning, complete automatic cleaning process.
Claims (4)
1.CIP purging system in place, comprise concentrated acid tank, concentrated base tank, concentrated acid thinning tank, concentrated base thinning tank, concentrated acid tank is connected with concentrated acid thinning tank pipeline, concentrated base tank is connected with concentrated base thinning tank pipeline, it is characterized in that, concentrated acid thinning tank, concentrated base thinning tank are connected with plate type heat exchanger by pipeline respectively, and plate type heat exchanger is connected with device to be cleaned by pipeline, and device to be cleaned is connected with concentrated acid thinning tank, concentrated base thinning tank by pipeline.
2. CIP according to claim 1 purging system in place, is characterized in that, also comprises water pot, and water pot is connected with the spray equipment at concentrated acid tank, concentrated base tank, concentrated acid thinning tank, concentrated base thinning tank top respectively, and water pot is also connected with plate type heat exchanger.
3. CIP according to claim 1 purging system in place, is characterized in that, between described concentrated acid tank and concentrated acid thinning tank and between concentrated base tank and concentrated base thinning tank, is respectively equipped with pneumatic diaphragm pump.
4. CIP according to claim 1 purging system in place, is characterized in that, described pipeline is provided with tubing pump, also has conductivity gauge, flowmeter, temperature sensor on pipeline, between each parts of described pipeline, is provided with hand-operated valve, pneumatic operated valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420165777.9U CN203778390U (en) | 2014-04-04 | 2014-04-04 | CIP in-place cleaning system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420165777.9U CN203778390U (en) | 2014-04-04 | 2014-04-04 | CIP in-place cleaning system |
Publications (1)
Publication Number | Publication Date |
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CN203778390U true CN203778390U (en) | 2014-08-20 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420165777.9U Expired - Fee Related CN203778390U (en) | 2014-04-04 | 2014-04-04 | CIP in-place cleaning system |
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CN (1) | CN203778390U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105363237A (en) * | 2015-11-27 | 2016-03-02 | 北京首钢朗泽新能源科技有限公司 | Clean-in-place system for distillation device, preparation for cleaning liquid, and cleaning method |
CN114350442A (en) * | 2021-12-13 | 2022-04-15 | 山东省科学院菏泽分院 | Production device for producing ground sesame seed oil by water substitution method |
-
2014
- 2014-04-04 CN CN201420165777.9U patent/CN203778390U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105363237A (en) * | 2015-11-27 | 2016-03-02 | 北京首钢朗泽新能源科技有限公司 | Clean-in-place system for distillation device, preparation for cleaning liquid, and cleaning method |
CN114350442A (en) * | 2021-12-13 | 2022-04-15 | 山东省科学院菏泽分院 | Production device for producing ground sesame seed oil by water substitution method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140820 Termination date: 20190404 |