CN217941166U - CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter - Google Patents
CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter Download PDFInfo
- Publication number
- CN217941166U CN217941166U CN202222090268.1U CN202222090268U CN217941166U CN 217941166 U CN217941166 U CN 217941166U CN 202222090268 U CN202222090268 U CN 202222090268U CN 217941166 U CN217941166 U CN 217941166U
- Authority
- CN
- China
- Prior art keywords
- cip
- water
- cleaning
- water recovery
- recovery
- 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.)
- Active
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The patent of the utility model relates to a CIP washs water recovery system, retrieves shelter, cleaning system and washs the shelter. The CIP cleaning water recovery system comprises a coarse filtering device, a membrane group filtering device, a material recovery tank and a pure water recovery device; the coarse filtering device is connected with the water outlet end of the CIP cleaning water and is used for filtering coarse-grained impurities in the cleaning water; the membrane group filtering device is connected with the coarse filtering device in series; the material recovery tank is connected with a material discharge end of the membrane group filtering device, the pure water recovery device is connected with a pure water discharge end of the membrane group filtering device, and the pure water recovery device is connected with the CIP cleaning water system. A CIP cleaning water recovery system is movably arranged in the recovery shelter; the cleaning system comprises a CIP cleaning water recovery system; the cleaning shelter is movably provided with a CIP cleaning system. CIP washs water recovery system, retrieves shelter, cleaning system and washs the shelter and has realized the material recovery function, has reached the effect of practicing thrift the washing water.
Description
Technical Field
The patent of the utility model relates to a water treatment technology field especially relates to a CIP washs water recovery system, retrieves shelter, cleaning system and washs the shelter.
Background
In dairy plants, the pipes after processing need to be cleaned, the cleaning method usually used is CIP cleaning, and the cleaning system needs to perform a five-pass flushing procedure. The first time, the pipeline is cleaned by hot water to ensure the cleanness and the sterility of the cleaned pipeline, but in the early period, more residual materials in the pipeline need to be recovered, in the later period, the discharged water is not recovered due to the dilution of the materials, the unrecovered cleaning water contains a large amount of organic matters, and the cleaning water containing the organic matters is treated in a sewage treatment area to form a large amount of waste water, so that the great waste of water sources is caused; cleaning with alkali liquor for the second time, wherein the concentration of the used alkali liquor is 3-5%, the purpose is to clean fatty oil substances in the pipeline, the alkali liquor with the concentration of 3-5% in the early cleaning stage can be recycled, and when the concentration of the alkali liquor is lower than 1%, the alkali liquor is not recycled and is discharged to a sewage treatment plant for treatment, so that certain water source waste is caused; the third time of cleaning by hot water, which aims to wash away the residual alkali liquor in the pipeline until clear water flows out, and in the process, a large amount of waste water is discharged to be treated in a sewage treatment area, so that a certain amount of water source waste is also caused; and fourthly, cleaning with acid liquor, namely cleaning the residual protein in the pipeline with 3-5% acid-containing nitric acid and hydrochloric acid, and then cleaning with clear water after washing. And the fifth time is the washing with the sterilized water, the washing is carried out by adopting hot water at about 85 degrees, and a part of energy is taken away while waste water is generated in the washing.
However, through the cleaning procedures of the above five flows, although the processing production pipeline is cleaned, a large amount of material wastewater, acidic wastewater and alkaline wastewater are generated in the process, which causes great waste of resources. Although some improvement means are provided for the method in the prior art, the method is limited to the partial recovery of the residual liquid of the dairy product, and the recovery treatment is not performed on acid and alkali by adopting related technical means, so that the waste of water resources in the cleaning procedure of the dairy product is large; in addition, in the process, a large amount of waste water is generated due to large water consumption, so that great water resource waste is caused.
Disclosure of Invention
Therefore, the CIP cleaning water recovery system, the recovery square cabin, the cleaning system and the cleaning square cabin are needed to solve the problems of low wastewater utilization rate and large acid and alkali waste in the CIP cleaning process of a dairy production factory in the prior art, so that the material recovery function is realized, and the cleaning water saving effect is achieved.
A CIP cleaning water recovery system comprises a coarse filtering device, a membrane group filtering device, a material recovery tank and a pure water recovery device; the coarse filtering device is connected with the water outlet end of the CIP cleaning water and is used for filtering coarse grain impurities in the cleaning water; the membrane group filtering device is connected with the coarse filtering device in series; the material recovery tank is connected with a material discharge end of the membrane group filtering device, the pure water recovery device is connected with a pure water discharge end of the membrane group filtering device, and the pure water recovery device is connected with the CIP cleaning water system.
In one embodiment, the membrane group filtration device comprises at least one of a dairy permeable membrane, an acid wash permeable membrane, a caustic wash permeable membrane, and a pure water permeable membrane.
In one embodiment, the material recovery tank comprises a dairy tank, an acid tank and a base tank, wherein the dairy tank is connected with the material discharge end of the dairy permeable membrane, the acid tank is connected with the material discharge end of the acid washing permeable membrane, and the base tank is connected with the material discharge end of the alkali washing permeable membrane.
In one embodiment, the CIP cleaning water recovery system further comprises a wastewater tank connecting the wastewater port of the pure water permeable membrane and the wastewater port of the coarse filtration device.
In one embodiment, the coarse filtering device comprises a filter screen, an outlet pipe network and a wastewater recovery pipe, wherein the filter screen is used for coarsely filtering CIP cleaning water, the outlet pipe network is connected with a filtered water outlet of the filter screen, and the wastewater recovery pipe is connected with a wastewater outlet of the filter screen.
In one embodiment, the outlet pipe network comprises a plurality of automatic control valves, and the automatic control valves are interlocked.
In one embodiment, the mesh of the filter screen is 200-300 meshes.
A CIP wash water recovery shelter comprising a wash water recovery shelter body and the CIP wash water recovery system of any of the embodiments described above removably installed in the wash water recovery shelter body.
A CIP wash water system comprising the CIP wash water recovery system described in any of the above embodiments.
A CIP wash water module comprises a wash water module body and the CIP wash water system movably mounted in the wash water module body.
Above-mentioned CIP washs water recovery system, retrieve the shelter, cleaning system and washing shelter, can filter the coarse impurity that CIP washs water through setting up coarse filter equipment, the membrane group filter equipment that sets up through the series connection carries out the membrane group to CIP washs water and filters to effectively carry out effective separation with material and drainage, wherein the material retrieves the storage through material recovery jar, filterable clear water enters into pure water recovery unit simultaneously and retrieves, will retrieve through closed loop connection's pure water recovery unit when CIP washs and wash water and use in the washing link once more. Therefore, through the design of the permeable membrane, more materials can be recovered, so that a sewage treatment station is not needed, and a large amount of fixed asset investment and operation cost are saved; meanwhile, the pure water recovery device is arranged to repeatedly return the recovered clean water to the CIP cleaning system for cleaning so as to contribute to environmental protection, avoid waste water and river pollution.
Drawings
FIG. 1 is a schematic diagram of a CIP wash water recovery system according to an embodiment;
FIG. 2 is a schematic diagram of an embodiment of a CIP wash water recovery shelter.
Detailed Description
To facilitate an understanding of the present application, the present application will now be described more fully with reference to the accompanying drawings. Preferred embodiments of the present application are given in the accompanying drawings. This application may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
It will be understood that when an element is referred to as being "disposed on" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. As used herein, the terms "vertical," "horizontal," "left," "right," "top," "bottom," "top," and the like are for purposes of illustration only and do not represent the only embodiment.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used herein in the description of the present application is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
In one embodiment, a CIP cleaning water recovery system comprises a coarse filtering device, a membrane group filtering device, a material recovery tank and a pure water recovery device; the coarse filtering device is connected with the water outlet end of the CIP cleaning water and is used for filtering coarse-grained impurities in the cleaning water; the membrane group filtering device is connected with the coarse filtering device in series; the material recovery tank is connected with a material discharge end of the membrane group filtering device, the pure water recovery device is connected with a pure water discharge end of the membrane group filtering device, and the pure water recovery device is connected with the CIP cleaning water system.
In one embodiment, a CIP wash water recovery module includes a wash water recovery module body and the CIP wash water recovery system movably mounted within the wash water recovery module body.
In an embodiment, a CIP wash water system includes the CIP wash water recovery system.
In one embodiment, a CIP wash water module includes a wash water module body and the CIP wash water system movably mounted within the wash water module body.
Above-mentioned CIP washs water recovery system, recovery shelter, cleaning system and washing shelter can filter the coarse impurity that CIP washs water through setting up coarse filtration device, and the membrane group filter equipment that sets up through the series connection carries out the membrane group to CIP washs water and filters to effectively carry out effective separation with material and drainage, wherein the material retrieves the storage through material recovery jar, and filterable clear water enters into pure water recovery unit simultaneously and retrieves, uses once more when CIP washs. Through the design of the permeable membrane, more materials can be recovered, so that a sewage treatment station is not needed, and a large amount of fixed asset investment and operation cost are saved; meanwhile, the pure water recovery device is arranged to repeatedly return the recovered clean water to the CIP cleaning system for cleaning so as to contribute to environmental protection, avoid waste water and river pollution.
Referring to fig. 1, in one embodiment, a CIP cleaning water recovery system 10 includes a coarse filtering apparatus 100, a membrane module filtering apparatus 200, a material recovery tank 300, and a pure water recovery apparatus 400; the coarse filtering device 200 is connected with the water outlet end of the CIP cleaning water and is used for filtering coarse impurities in the cleaning water; the membrane group filtering device 200 is connected with the coarse filtering device 100 in series; the material recovery tank 300 is connected to the material discharge end of the membrane module filtering device 200, the pure water recovery device 400 is connected to the pure water discharge end of the membrane module filtering device 200, and the pure water recovery device 200 is connected to the CIP cleaning water system.
In particular, coarse filtration device 100 is an industrial coarse filter that can protect the proper operation of compressors, pumps, meters, and other equipment. In one embodiment, the rough filtering apparatus 100 includes a filter screen 110, a water outlet pipe network 120, and a wastewater recycling pipe 130, wherein the filter screen 110 is used for roughly filtering CIP washing water, the water outlet pipe network 120 is connected to a filtered water outlet of the filter screen 110, and the wastewater recycling pipe 120 is connected to a wastewater outlet of the filter screen. In one embodiment, the mesh of the filter screen is 200-300 meshes. That is, the filter screen 110 is a filter cylinder with 200-300 mesh specification, when fluid flows into the filter screen, impurities are blocked, clean filtrate is discharged from a filtered water outlet of the filter screen 110, when the filter screen needs to be cleaned, the detachable filter cylinder is only required to be taken out and installed again after being treated, and therefore, the filter screen is very convenient to use and maintain.
In one embodiment, the membrane module filtration device 200 includes at least one of a dairy permeable membrane 210, an acid wash permeable membrane 220, a base wash permeable membrane 230, and a pure water permeable membrane 240. That is, the membrane module filtering apparatus 200 may selectively set only the dairy permeable membrane 210, the acid washing permeable membrane 220, the alkali washing permeable membrane 230, or the pure water permeable membrane 240 according to the filtering recovery requirement; the selective placement of both the dairy permeable membrane 210 and the acid washed permeable membrane 220 is also possible; a dairy permeable membrane 210 and a caustic wash permeable membrane 230; a pure water permeable membrane 240 and an acid washed permeable membrane 220; a pure water permeable membrane 240 and an alkaline cleaning permeable membrane 230; acid wash permeable membrane 220 and base wash permeable membrane 230; a dairy permeable membrane 210 and a pure water permeable membrane 240; a dairy permeable membrane 210, an acid wash permeable membrane 220, a base wash permeable membrane 230, and a pure water permeable membrane 240. The permeable membrane is an organic membrane, and the reverse osmosis membrane may be a forward permeable membrane, which is not limited in this embodiment. The water is recovered and separated into pure water and materials through the cleaning of the permeable membrane.
In one embodiment, the material recovery tank 300 comprises a dairy tank 310, an acid tank 320, and a base tank 330, the dairy tank 310 being connected to the material discharge end of the dairy permeable membrane 210, the acid tank 320 being connected to the material discharge end of the acid wash permeable membrane 220, and the base tank 330 being connected to the material discharge end of the base wash permeable membrane 230. Specifically, the dairy permeable membrane 210 has a dairy product port and a plain water port, wherein the dairy product port is connected to the dairy tank 310 and the plain water port is connected to the plain water recovery unit 400. In a specific embodiment, the dairy product material port is provided with a material concentration meter, and when the material concentration meter detects that the material concentration is 1% -4%, the dairy product material port is started to recover the material. The acid-washing permeable membrane 220 is provided with an acid material port and a pure water port, wherein the acid material port is connected with the acid tank 320, and the pure water port is connected with the pure water recovery device 400; in one embodiment, the acid material port is provided with an acid concentration meter, and the acid is recovered when the acid concentration meter detects that the material concentration is 1% -5%. The alkali washing permeable membrane 230 has an alkali material opening and a pure water opening, wherein the alkali material opening is connected to the alkali tank 330, the pure water opening is connected to the pure water recovery unit 400, the pure water recovery unit 400 has a waste material opening and a pure water opening, and the pure water opening is connected to the pure water recovery unit 400.
In one embodiment, the CIP cleaning water recovery system further comprises a wastewater tank 500 connecting the wastewater port of the pure water permeable membrane 240 and the wastewater port of the coarse filtration device 100. In an embodiment, the wastewater basin 500 is provided with a wastewater treatment system, which may be a freeze-drying type system or a drying type system. And (3) adopting a wastewater treatment system to obtain solid feed by adopting a freeze-drying technology or a drying technology on the wastewater discharged into the wastewater tank.
In one embodiment, the outlet network 120 includes a plurality of automatic control valves, and each of the automatic control valves is interlocked. That is, the automatic control valves arranged in the water outlet pipe network 120 are controlled by a program control system, the automatic control valves are interlocked and arranged according to a program control logic, the program control adopts electric signal communication, and when one or more of the automatic control valves are opened, other automatic control valves are automatically closed. Therefore, the automatic control valve arranged in an interlocking manner ensures that the corresponding control valve is selectively opened according to the recovered materials in the CIP cleaning water recovery process, and the materials are synchronously or step-by-step recovered.
In one embodiment, the CIP wash water recovery system operates as follows:
the first step is as follows: starting the coarse filtering device, and synchronously starting the water outlet pipe network and the wastewater recovery pipe;
the second step is that: selectively opening at least one of a material permeable membrane, an acid cleaning permeable membrane, an alkali cleaning permeable membrane and a pure water permeable membrane according to the cleaning requirement for carrying out permeation filtration;
the third step: opening material outlets of the permeable membranes according to a material recovery set index, and respectively conveying recovered materials to a corresponding material tank, an acid tank, an alkali tank and a pure water recovery device;
the fourth step: and (3) obtaining the solid feed by adopting a freeze-drying technology or a drying technology for the wastewater discharged into the wastewater tank.
Referring to fig. 2, in one embodiment, a CIP wash water recovery module 20 includes a wash water recovery module body 600 and the CIP wash water recovery system 10 removably installed within the wash water recovery module body. The cleaning water recovery shelter body is of a container type closed box body structure and can be moved, movable installation and arrangement can be carried out at any time and any place according to installation requirements, and equipment and pipelines related to the CIP cleaning water recovery system are arranged in the container type closed box body.
In an embodiment, a CIP wash water system includes the CIP wash water recovery system. The CIP cleaning water system is a system for cleaning the equipment and the pipeline of the dairy production system, the CIP cleaning water recovery system is connected at the tail end of the CIP cleaning water system, and the outlet of the CIP cleaning water system is connected to the water inlet of the coarse filtering device of the CIP cleaning water recovery system. That is, the CIP wash water system includes a reclamation system, forming a larger system CIP wash water system.
In one embodiment, a CIP wash water module includes a wash water module body and the CIP wash water system movably mounted within the wash water module body. Wherein, wash water shelter body is container formula closed box structure, and can remove, can carry out movable mounting setting according to the installation needs anytime and anywhere, and equipment and the pipeline setting that CIP washing water system relates to are in container formula closed box.
Above-mentioned CIP washs water recovery system, retrieve the shelter, cleaning system and washing shelter, can filter the coarse impurity that CIP washs water through setting up coarse filter equipment, the membrane group filter equipment that sets up through the series connection carries out the membrane group to CIP washs water and filters, thereby effectively carry out effective separation with material and drainage, wherein the material passes through material recovery jar recovery storage, filterable clear water enters into pure water recovery unit and retrieves simultaneously, will retrieve through closed loop connection's pure water recovery unit when CIP washs and wash water and use in the cleaning link once more. Through the design of the permeable membrane, more materials can be recovered, so that a sewage treatment station is not needed, and a large amount of fixed asset investment and operation cost are saved; meanwhile, the pure water recovery device is arranged to repeatedly return the recovered clean water to the CIP cleaning system for cleaning so as to contribute to environmental protection, avoid waste water and river pollution.
The technical features of the embodiments described above may be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the embodiments described above are not described, but should be considered as being within the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
The above-mentioned embodiments only express several embodiments of the present application, and the description thereof is more specific and detailed, but not construed as limiting the claims. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the concept of the present application, which falls within the scope of protection of the present application. Therefore, the protection scope of the present patent application shall be subject to the appended claims.
Claims (10)
1. A CIP cleaning water recovery system is characterized by comprising a coarse filtration device, a membrane group filtration device, a material recovery tank and a pure water recovery device;
the coarse filtering device is connected with the water outlet end of the CIP cleaning water and is used for filtering coarse grain impurities in the cleaning water;
the membrane group filtering device is connected with the coarse filtering device in series;
the material recovery tank is connected with a material discharge end of the membrane group filtering device, the pure water recovery device is connected with a pure water discharge end of the membrane group filtering device, and the pure water recovery device is connected with the CIP cleaning water system.
2. The CIP wash water recovery system of claim 1, wherein the membrane module filtration unit includes at least one of a dairy osmosis membrane, an acid wash osmosis membrane, a base wash osmosis membrane, and a pure water osmosis membrane.
3. The CIP wash water recovery system of claim 2, wherein the material recovery tank comprises a dairy tank connected to the material discharge end of the dairy permeable membrane, an acid tank connected to the material discharge end of the acid wash permeable membrane, and a base tank connected to the material discharge end of the base wash permeable membrane.
4. The CIP wash water recovery system according to claim 2, further comprising a wastewater tank connecting the wastewater port of the pure water permeable membrane and the wastewater port of the coarse filtration device.
5. The CIP wash water recovery system according to claim 4, wherein the coarse filtration device includes a filter screen for coarse filtering the CIP wash water, an outlet pipe network connected to a filtered water outlet of the filter screen, and a waste water recovery pipe connected to a waste water outlet of the filter screen.
6. The CIP wash water recovery system of claim 5, wherein the outlet piping network includes a plurality of automatic control valves, each of the automatic control valves being interlockingly disposed.
7. The CIP cleaning water recovery system according to claim 5, wherein the mesh of the filter screen is 200-300 mesh.
8. A CIP wash water recovery module comprising a wash water recovery module body and a CIP wash water recovery system according to any one of claims 1 to 7 movably mounted in the wash water recovery module body.
9. A CIP wash water system comprising the CIP wash water recovery system of any one of claims 1 to 7.
10. A CIP wash water shelter comprising a wash water shelter body and the CIP wash water system of claim 9 movably mounted in the wash water shelter body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222090268.1U CN217941166U (en) | 2022-08-09 | 2022-08-09 | CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222090268.1U CN217941166U (en) | 2022-08-09 | 2022-08-09 | CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217941166U true CN217941166U (en) | 2022-12-02 |
Family
ID=84227247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222090268.1U Active CN217941166U (en) | 2022-08-09 | 2022-08-09 | CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217941166U (en) |
-
2022
- 2022-08-09 CN CN202222090268.1U patent/CN217941166U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202358976U (en) | Glass wastewater treatment equipment | |
| CN103030237B (en) | Treatment device and treatment method for recycling coal slurry sewage | |
| KR20170031996A (en) | System for filtering waste water and recovering heat of waste water | |
| CN102688694B (en) | On-line back washing process system of porous ceramic film | |
| CN205461190U (en) | Water advanced treatment integrated device | |
| CN205710136U (en) | A kind of plating cupric poaching wastewater processing system | |
| CN2677366Y (en) | Medium and small size integrated reverse asmosis sea water desalination device | |
| CN217941166U (en) | CIP cleaning water recovery system, recovery shelter, cleaning system and cleaning shelter | |
| CN210528597U (en) | Intelligent wastewater recycling water purifier | |
| CN202449889U (en) | Distributed water treatment device based on dynamic membrane | |
| CN110947219A (en) | Device and method for recycling materials in ternary precursor washing wastewater and recycling wastewater | |
| CN208648833U (en) | A kind of double film combination sewage-treatment plants | |
| CN203269626U (en) | Membrane treatment device for industrial wastewater treatment | |
| CN216260055U (en) | Online monitoring and cleaning system for ultrafiltration membrane for treating landfill leachate | |
| CN205035121U (en) | Reverse osmosis membrane water processing system | |
| CN213707828U (en) | Magnesium hydroxide washing water treatment device | |
| CN209442762U (en) | A kind of circulation water recycling device | |
| CN112875804A (en) | Process for reducing ultrafiltration self-water utilization rate and improving water yield recovery rate | |
| CN209652000U (en) | A kind of processing system of nickel-containing waste water | |
| KR101973736B1 (en) | Method for production of sludge dewatering cake in ceramic membrane filtration process using submerged membrane and pressurized membrane | |
| CN113385036A (en) | Classified recovery device and method for ultrafiltration drainage | |
| CN207405158U (en) | A kind of enzyme purification system using UF membrane | |
| CN114573076A (en) | Drinking water ultrafiltration system without chemical adding and unpowered backwashing and operation method | |
| CN219290705U (en) | Vinegar beverage production technology water saving system | |
| CN210521872U (en) | Sand carbon filter backwash economizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |