CN207512154U - It is pure to eat vinegar composite membrane aseptic filtration machine raw - Google Patents
It is pure to eat vinegar composite membrane aseptic filtration machine raw Download PDFInfo
- Publication number
- CN207512154U CN207512154U CN201720528986.9U CN201720528986U CN207512154U CN 207512154 U CN207512154 U CN 207512154U CN 201720528986 U CN201720528986 U CN 201720528986U CN 207512154 U CN207512154 U CN 207512154U
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- CN
- China
- Prior art keywords
- composite membrane
- vinegar
- main circulation
- pure
- aseptic filtration
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- 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.)
- Expired - Fee Related
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model is related to it is a kind of it is pure eat vinegar aseptic filtration machine raw, main circulation loop is formed by main circulation pump, composite membrane component, liquid collecting cavity and valve pipe etc., fill cycles circuit is formed by charging pump, major cycle pipeline and corresponding valve pipe etc..Wherein composite membrane shares 4 components, and the membrane area of every component is 9m2Two and two series connections, the aperture of composite membrane is only 0.2 μm, this equipment can effectively remove suspended matter in vinegar, sediment, miscellaneous bacteria, vinegar, which needs not move through heat sterilization, can reach the requirement of 2719 vinegar sanitary standards of GB, equipment operation is simple, reduces pollution, can be with industrialized production.
Description
Technical field
The utility model is related to a kind of filter more particularly to a kind of equipment for edible vinegar sterilizing filtering.
Background technology
At present, in the practical application of vinegar brewing industry, removal of impurities goes turbid method mainly to have diatomite filtering and activity
Charcoal adsorption filtration.These method equipment are complicated, operating cost is high, and energy consumption is big, and bacteria-eliminating efficacy is bad, must also after leading to filtering
The sanitary standard of product must be can be only achieved by high temperature sterilization again.
Invention content
To solve the above-mentioned problems, the utility model provides a kind of superfine filter easy to operate, pollution is few, it
Not only removal of impurities is gone turbid clean, and is avoided that because of the nutritional ingredient of high temperature product, so as to keep the original flavor of product.
To achieve the above object, the utility model takes following designing scheme：This pure vinegar aseptic filtration machine of eating raw is by leading
Circulating pump, composite membrane component, liquid collecting cavity and valve pipe etc. form main circulation loop, by charging pump, major cycle pipeline and
The composition fill cycles such as corresponding valve pipe circuit.Wherein composite membrane shares 4 components, and the membrane area of every component is 9m2 ,
Two and two series connections.Main circulation loop main function is to provide power to ceramic membrane filter, makes material complete when flowing through membrane module
Into filtering and separation, fill cycles circuit main function one is to main circulation loop supplement feed and trapped substance concentration is higher
Major cycle liquid sends head tank back to, second is that properly increasing the system pressure of main circulation loop.
Pure vinegar aseptic filtration machine of eating raw adds in preprocessed processed vinegar in head tank, by charging pump sucking and
Enter major circulatory system after improving pressure, recycled through main circulation pump and be sent into membrane module, the permeate flowed out from membrane module is through flow
Enter subsequent processing after meter；Dope is flowed out from major circulatory system, and dope flows back into head tank, and so constantly cycle realizes material
Filtering.
Since the compound membrane aperture that the utility model uses is 0.2 μm, so as to obtain following advantageous effect：Degerming removes
Turbid effect is good, vinegar after filtering, can not only ensure the clarity of vinegar, but also can reach effective degerming, microorganism
Index can reach the requirement of 2719 vinegar sanitary standards of GB, and product is not needed to using high-temperature sterilization, so as to also maintain production
The original flavor of product.
Description of the drawings
Attached drawing 1 is the process flow chart of the utility model.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
In attached drawing 1,1 is head tank, and 2 be charging pump, and 3 be circulating pump, and 4 be sub-material tank, and 5 be membrane module, and 6 be purge tank.
The course of work of filter is as follows：
First material liquid is added in head tank during membrane filtration, can opening bottom outlet valve, suitably opens it at charging pump inlet valve
Outlet valve, system outlet valve start charging pump（Start front exhaust）, it is fed to system, while drain air in system, low frequency opens
Dynamic main circulation pump, slowly promotes frequency, pressure, flow are suitably adjusted according to needed for membrane filtration after operating steadily.Open film
Component per-meate side valve opens corresponding valve according to pipeloop, first starts charging pump（Pump exhaust is first given before unlatching）, treat
After main circulation loop is full of material, start main circulation pump, open 4 membrane modules and penetrate fluid valve, penetrating fluid is conveyed to Clear liquid tank,
Part dope flows back to head tank.
After membrane flux gradually declines due to film surface pollutes, therefore equipment has often filtered a batch quantity, composite membrane is coped with
It is cleaned.First by slag emptying dense in system, past purge tank adds pure water to be floated to emptying after cycle rinses 2-3 times completely, is carried out
Wash water then with 1.0% sodium hydroxide solution, under the conditions of 45 DEG C -55 DEG C, is cleaned 30-40 minutes, is emptied.2- is rinsed with pure water
It 3 times, empties.Then the liquor natrii hypochloritis of available chlorine content 300-400PPM, the circular flow under the conditions of 20 DEG C -25 DEG C are used again
It shuts down and impregnates 30 minutes after ten minutes, empty, rinsed 2-3 times with pure water until pH value is in neutrality.
Claims (3)
1. one kind is pure to eat vinegar composite membrane aseptic filtration machine raw, by by main circulation pump, Ceramic Composite membrane module, liquid collecting cavity and valve
Pipeline etc. forms main circulation loop, and fill cycles circuit is formed by charging pump, major cycle pipeline and corresponding valve pipe etc.,
It is characterized in that：It is made of two circuits, main circulation loop main function is to provide power to ceramic membrane filter, is flowing material
Through completing to filter during membrane module and detach, fill cycles circuit main function one is to supplement feed to main circulation loop and will retain
The higher major cycle liquid of object concentration sends head tank back to, second is that properly increasing the system pressure of main circulation loop.
2. pure vinegar composite membrane aseptic filtration machine is eaten raw according to claim 1, it is characterised in that：The material of composite membrane is pottery
Porcelain shares 4 components, and the membrane area of every component is 9m2 , two and two series connections, the aperture of ceramic composite membrane is 0.2 μm.
3. pure vinegar composite membrane aseptic filtration machine is eaten raw according to claim 1, it is characterised in that：Equipped with feed temperature, film
Component inlet pressure number is shown and overtemperature alarm function detects seepage discharge function with infiltration flow measurement gauge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720528986.9U CN207512154U (en) | 2017-05-13 | 2017-05-13 | It is pure to eat vinegar composite membrane aseptic filtration machine raw |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720528986.9U CN207512154U (en) | 2017-05-13 | 2017-05-13 | It is pure to eat vinegar composite membrane aseptic filtration machine raw |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207512154U true CN207512154U (en) | 2018-06-19 |
Family
ID=62530729
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720528986.9U Expired - Fee Related CN207512154U (en) | 2017-05-13 | 2017-05-13 | It is pure to eat vinegar composite membrane aseptic filtration machine raw |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207512154U (en) |
-
2017
- 2017-05-13 CN CN201720528986.9U patent/CN207512154U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180619 |