CN205925182U - Refined system of fish sauce fermentation stoste - Google Patents
Refined system of fish sauce fermentation stoste Download PDFInfo
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- CN205925182U CN205925182U CN201620929265.4U CN201620929265U CN205925182U CN 205925182 U CN205925182 U CN 205925182U CN 201620929265 U CN201620929265 U CN 201620929265U CN 205925182 U CN205925182 U CN 205925182U
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- storage tank
- desalination
- liquid storage
- ceramic membrane
- electrodialysis plant
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Abstract
The utility model discloses a refined system of fish sauce fermentation stoste, including primary filter, storage tank, ceramic membrane filter equipment, electrodialysis device, the storage tank includes just filtrate storage tank, desalination liquid storage tank and concentrate storage tank, and primary filter is connected with the storage tank of just filtrating, and the storage tank of just filtrating is connected with ceramic membrane filter equipment through feedstock pump, and ceramic membrane filter equipment is connected with desalination liquid storage tank, be provided with including positive pole, amberplex and negative pole in the electrodialysis device, desalination liquid storage tank is connected with the electrodialysis device through desalination liquid delivery pump, and the concentrate storage tank is connected with the electrodialysis device through the concentrate delivery pump, and the electrodialysis device is connected with desalination liquid storage tank, and the electrodialysis device is connected with the concentrate storage tank. The utility model discloses fish sauce fermentation stoste through straining with desalination after, realized the refining treatment of fish sauce fermentation stoste when obtaining the bright fish sauce of the defecation, not changing its nutrition, flavor and taste.
Description
Technical field
This utility model belongs to technical field of seasoning processing, more particularly to a kind of fish juice fermenation raw liquid refining system.
Background technology
Fish juice, also known as petis, pancreas oil, northern Shandong is referred to as fish soup, is a kind of Aquatic product flavoring agent of unique flavor, main inclusion
Delicate flavour and saline taste.Fish juice with low value fish and shrimp or disposal from fishery product processing as raw material, using the protease contained by fish body and other
Enzyme, and in the common presence of multiple-microorganism, to the protein in raw material fish, the composition such as fat carries out fermentation and decomposes, and brews
Form.Its salty in the mouth, extremely delicious, nutritious, contain all of necessary aminoacid and taurine, also contain multiple ore deposit such as calcium, iodine
Material and vitamin.Fish juice as flavoring agent, uses more, nowadays Europe also has and gradually flows at present in southeastern coast, Southeast Asia
OK, there is larger market prospect.
General fish juice adopts natural filtration in process of production, that is, with filter cloth by fermenation raw liquid natural filtration thereon, obtains
To the fish juice of clarification, this filter method efficiency is very low and the more difficult health demand meeting now；And traditional fish juice life
During product, its sodium chloride content is in saturation, and probably 28% about, so high salinity has a strong impact on it one
Application in a little food is it is difficult to adapt to demand for exports.
Content of the invention
The purpose of this utility model is that and overcomes the deficiencies in the prior art, there is provided a kind of fish juice fermenation raw liquid refines system
System, fish juice fermenation raw liquid of the present utility model through filter and desalting processing after it is achieved that the refinement treatment of fish juice fermenation raw liquid,
While obtaining clarifying bright fish juice, do not change its nutrition, local flavor and mouthfeel, and good filtration effect, substantially increase life
Produce efficiency, desalination amount can be adjusted according to different clients demand, to adapt to different crowd.
To achieve these goals, this utility model provides a kind of fish juice fermenation raw liquid refining system, including primary mistake
Filter, storage tank, ceramic membrane filter device, electrodialysis plant, described storage tank includes just filtrate tanks, desalination liquid storage tank and concentrated solution
Storage tank, described primary filter is connected with described just filtrate tanks, and described just filtrate tanks pass through raw material pump and described pottery
Film filter is connected, and described ceramic membrane filter device is connected with described desalination liquid storage tank；Set in described electrodialysis plant
It is equipped with including anode, ion exchange membrane and negative electrode, described electrodialysis plant is separated into diluting compartment and dense by described ion exchange membrane
Contracting room, described anode is connected with the positive and negative polarities of DC source respectively with negative electrode；It is defeated that described desalination liquid storage tank passes through desalination solution
Pump is sent to be connected with the desalination chamber inlet of described electrodialysis plant, described concentration liquid storage tank passes through concentrated solution delivery pump and described electricity
The concentration chamber inlet of electrodialysis apparatus is connected, and the diluting compartment outlet of described electrodialysis plant is connected with described desalination liquid storage tank,
Enriched chamber's outlet of described electrodialysis plant is connected with described concentration liquid storage tank.
Further, described fish juice fermenation raw liquid desalting refinement includes head tank, described head tank and described primary filter
Device is connected, and described ceramic membrane filter device is connected with described head tank.
Further, described ion exchange membrane is homogeneous electrodialytic membraness.
Further, in described ceramic membrane filter device, the membrane aperture of ceramic membrane is 0.1 μm.
The beneficial effects of the utility model：
Fish juice fermenation raw liquid of the present utility model obtains clear after primary filter and ceramic membrane filter device double-filtration
Clear liquid, then clear liquor is delivered to electrodialysis plant carries out desalting processing it is achieved that the refinement treatment of fish juice fermenation raw liquid,
To while clarifying bright fish juice, do not change its nutrition, local flavor and mouthfeel.Wherein ceramic membrane filter device filter compared to
Existing natural filtration method, its good filtration effect, substantially increase production efficiency.Electrodialysis plant can be according to difference simultaneously
The demand of client is adjusted to the desalination amount of clear liquor, and to adapt to different crowd, its salt rejection rate can reach more than 90%, this reality
It is particularly conducive to manufacturing of high-end fish juice with new, competitive advantage can be had more when exploiting the overseas market.
Brief description
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or in description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of this utility model embodiment.
Above-mentioned reference：
1 head tank, 2 primary filters, 3 first filtrate tanks, 4 raw material pumps, 5 ceramic membrane filter devices, 6 desalination liquid storage tanks, 7
Desalination solution delivery pump, 8 electrodialysis plants, 9 concentrated solution delivery pumps, 10 concentration liquid storage tanks.
Specific embodiment
Below in conjunction with the accompanying drawings utility model is further illustrated, but be not limited to scope of the present utility model.
Embodiment
As shown in figure 1, a kind of fish juice fermenation raw liquid refining system that this utility model provides, including primary filter 1, storage
Tank, ceramic membrane filter device 5, electrodialysis plant 8, described storage tank includes just filtrate tanks 3, desalination liquid storage tank 6 and concentrated solution storage
Tank 10, described primary filter 2 is connected with described just filtrate tanks 3, described just filtrate tanks 3 pass through raw material pump 4 with described
Ceramic membrane filter device 5 is connected, and described ceramic membrane filter device 5 is connected with described desalination liquid storage tank 6.
It is provided with including anode, ion exchange membrane and negative electrode in described electrodialysis plant 8, described electrodialysis plant 8 is divided
It is divided into diluting compartment and enriched chamber, described anode is connected with the positive and negative polarities of DC source respectively with negative electrode；Described desalination solution storage
Tank 6 is connected with the desalination chamber inlet of described electrodialysis plant 8 by desalination solution delivery pump 7, and described concentration liquid storage tank 10 passes through
Concentrated solution delivery pump 9 is connected with the concentration chamber inlet of described electrodialysis plant 8, the diluting compartment outlet of described electrodialysis plant 8
It is connected with described desalination liquid storage tank 6, enriched chamber's outlet of described electrodialysis plant 8 is connected with described concentration liquid storage tank 10.
Preferably, described ion exchange membrane is homogeneous electrodialytic membraness.
Described fish juice fermenation raw liquid refining system of the present utility model includes head tank 1, described head tank 1 and described primary
Filter 2 is connected, and fish juice fermenation raw liquid is stored in head tank 1.Wherein ceramic membrane filter device 5 is connected with head tank 1,
It is back in head tank 1 with realizing float that ceramic membrane filter device 5 filters out and insoluble impuritiess.
Preferably, in described ceramic membrane filter device 5, the membrane aperture of ceramic membrane is 0.1 μm to this utility model, i.e. ceramic membrane
The filtering accuracy of defecator 5 is 100 nanometers, and filtering accuracy is high, can be effectively by the float in first filtrate and insoluble impuritiess
Filter out completely.
Workflow of the present utility model：
1st, fish juice fermenation raw liquid obtain after primary filter 2 primary filter just filtrate (containing a lot of float and insoluble
Property impurity), and be delivered to just filtrate tanks 3；
2nd, pass through raw material pump 4 and will contain the first filtrate of a lot of float and insoluble impuritiess in first filtrate tanks 3, be pumped to
Ceramic membrane filter device 5 filters further, obtains clear liquor to filter out the float in first filtrate and insoluble impuritiess, obtains
Clear liquor be delivered to desalination liquid storage tank 6, the float wherein filtering out and insoluble impuritiess are back in head tank 1；
3rd, in electrodialysis plant 8, the initial concentration of concentrated solution is the sodium chloride solution of electrical conductivity 30ms/cm, electrodialysis plant
Anode in 8 and negative electrode are connected with the both positive and negative polarity of DC source respectively, and electrodialysis plant 8 is separated into diluting compartment by ion exchange membrane
And enriched chamber, the cation of the free state in the desalination solution respectively conveying of desalination solution delivery pump being come by electric field action and the moon
Ion is migrated；
4th, desalination solution is delivered in electrodialysis plant 8 by desalination solution delivery pump 7 and carries out desalting processing, at electrodialysis
After reason, the inorganic ion such as sodium chloride passes through ion exchange membrane, enters in the middle of concentrated solution.Concentrated solution migrates for inorganic ion
Reception liquid, inorganic ion by desalination solution pass through ion exchange membrane enter concentrated solution so that the inorganic salt content in concentrated solution not
Disconnected rising, and it is finally reached the concentration of 15%-20%, after concentrated solution concentration reaches terminal, by most concentration liquid storage tank 10
In concentrated solution discharge, stay part high concentration concentrated solution and fresh water be diluted to again electrical conductivity 30ms/cm about concentrated solution, continue
The inorganic ion that continuous circulation, enrichment are passed through by desalination solution；
5th, desalination solution constantly circulates desalination in the diluting compartment of desalination liquid storage tank 6 and electrodialysis plant 8, wherein can basis
Different quality requirements control the terminal of desalination.
6th, after desalination terminates, pole is carried out down to the anode and negative electrode of electrodialysis plant 8, sun will be changed into by original negative electrode
Pole, original anode is changed into negative electrode, then carries out Membrane cleaning, in case next batch uses.
7th, wherein in electrodialysis plant 8 electric current density controlled in 550-600A/m2.
Fish juice fermenation raw liquid of the present utility model obtains after primary filter 2 and ceramic membrane filter device 5 double-filtration
Clear liquor, then clear liquor is delivered to electrodialysis plant 8 carries out desalting processing it is achieved that the refinement treatment of fish juice fermenation raw liquid,
While obtaining clarifying bright fish juice, do not change its nutrition, local flavor and mouthfeel.Wherein ceramic membrane filter device 5 filters
Compared to existing natural filtration method, its good filtration effect, substantially increase production efficiency.Electrodialysis plant 8 can simultaneously
Demand according to different clients is adjusted to the desalination amount of clear liquor, and to adapt to different crowd, wherein salt rejection rate can reach
More than 90%, competitive advantage can be had more when this utility model is particularly conducive to exploit the overseas market.
Of the present utility model ultimate principle, principal character and of the present utility model advantage have been shown and described above.One's own profession
The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description
Principle of the present utility model is simply described, on the premise of without departing from this utility model spirit and scope, this utility model also can
There are various changes and modifications, these changes and improvements both fall within the range of claimed this utility model.This utility model will
Protection domain is asked to be defined by appending claims and its equivalent.
Claims (4)
1. a kind of fish juice fermenation raw liquid refining system it is characterised in that：Including primary filter, storage tank, ceramic membrane filter device,
Electrodialysis plant, described storage tank includes just filtrate tanks, desalination liquid storage tank and concentrate liquid storage tank, described primary filter with described
Just filtrate tanks are connected, and described just filtrate tanks are connected with described ceramic membrane filter device by raw material pump, described pottery
Film filter is connected with described desalination liquid storage tank；
It is provided with including anode, ion exchange membrane and negative electrode in described electrodialysis plant, described ion exchange membrane is by described electric osmose
Analysis apparatus are separated into diluting compartment and enriched chamber, and described anode is connected with the positive and negative polarities of DC source respectively with negative electrode；
Described desalination liquid storage tank is connected with the desalination chamber inlet of described electrodialysis plant by desalination solution delivery pump, described concentration
Liquid storage tank is connected with the concentration chamber inlet of described electrodialysis plant by concentrated solution delivery pump, the desalination of described electrodialysis plant
Room outlet is connected with described desalination liquid storage tank, and enriched chamber's outlet of described electrodialysis plant is connected with described concentration liquid storage tank
Connect.
2. a kind of fish juice fermenation raw liquid refining system according to claim 1 is it is characterised in that described fish juice fermenation raw liquid
Refining system also includes head tank, and described head tank is connected with described primary filter, described ceramic membrane filter device and institute
State head tank to be connected.
3. a kind of fish juice fermenation raw liquid refining system according to claim 1 is it is characterised in that described ion exchange membrane is
Homogeneous electrodialytic membraness.
4. a kind of fish juice fermenation raw liquid refining system according to claim 1 is it is characterised in that described ceramic membrane filter fills
The membrane aperture putting middle ceramic membrane is 0.1 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620929265.4U CN205925182U (en) | 2016-08-24 | 2016-08-24 | Refined system of fish sauce fermentation stoste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620929265.4U CN205925182U (en) | 2016-08-24 | 2016-08-24 | Refined system of fish sauce fermentation stoste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205925182U true CN205925182U (en) | 2017-02-08 |
Family
ID=57952718
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620929265.4U Active CN205925182U (en) | 2016-08-24 | 2016-08-24 | Refined system of fish sauce fermentation stoste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205925182U (en) |
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2016
- 2016-08-24 CN CN201620929265.4U patent/CN205925182U/en active Active
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: Room 802, No. 30, Jiayuanli, Huli District, Xiamen City, Fujian Province Patentee after: Huasheng Fluid Separation Technology (Xiamen) Co., Ltd. Address before: Room 802, No. 30, Jiayuanli, Huli District, Xiamen City, Fujian Province Patentee before: Huasheng fluid separation technology (Xiamen) Co., Ltd. |
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| CP03 | Change of name, title or address |