CN204952454U - Be used for refine membrane filtration system of syrup - Google Patents
Be used for refine membrane filtration system of syrup Download PDFInfo
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- CN204952454U CN204952454U CN201520712313.XU CN201520712313U CN204952454U CN 204952454 U CN204952454 U CN 204952454U CN 201520712313 U CN201520712313 U CN 201520712313U CN 204952454 U CN204952454 U CN 204952454U
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Abstract
The utility model relates to a be used for refine membrane filtration system of syrup, including the board -like colating device of syrup liquid tank, multilayer that loops through pipeline intercommunication, intermediate storage tanks no. 1, ceramic micro -filtration device, intermediate storage tanks no. 2 and ceramic ultrafiltration device, impurity filtrating in the pottery micro -filtration device is gone into through the pipeline backward flow syrup liquid tank, pottery ultrafiltration device's impurity filtrating is gone into through the pipeline backward flow intermediate storage tanks one. The beneficial effects of the utility model are that, before the syrup carries out the ultrafiltration processing, colating and micro -filtration device has set gradually, can guarantee that the filtration pore of milipore filter is not blockked up, milipore filter long service life, be provided with intermediate storage tanks no. 1 and intermediate storage tanks no. 2, when the sponge that needs to be changed, filter cloth or micro -filtration membrane, do not need whole production facility to park in the production process, improve production efficiency.
Description
Technical field
The utility model belongs to syrup manufacture field, is specifically related to a kind of membrane filtration system refining for syrup.
Background technology
Containing the impurity substances that the particle diameters such as a certain amount of protein, non-degraded cellulose, colloid, particulate (as fine sand) are larger in syrup stoste, need these impurity filterings in syrup finishing passes.The refining multiple tracks milipore filter that often directly adopts of the prior art carries out refining processing, or again through milipore filter processing and refining after a coarse filtration, its weak point existed is, because not doing deep process to syrup stoste before ultrafiltration, it is comparatively large that it includes the more and particle diameter of impurity of impurity level, very easily blocks the aperture of milipore filter in ultra-filtration process, and then surpass into milipore filter and break, production efficiency is low, and cost is high.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of membrane filtration system refining for syrup, this filtration system before ultrafiltration is carried out to syrup through coarse filtration and micro-filtration process, and suitably control the pressure of each filtration step, milipore filter not easily breaks, can not often change, production efficiency is higher.
The technical scheme that the utility model solves the problems of the technologies described above is, a kind of membrane filtration system refining for syrup, comprise successively by the syrup original fluid container of pipeline communication, multi-layer plate-type rough filtering device, intermediate storage tank one, ceramic micro filter device, intermediate storage tank two and Ceramic excessive filtration device, pipeline between described syrup original fluid container and multi-layer plate-type rough filtering device is provided with dehvery pump one, pipeline between described intermediate storage tank one and ceramic micro filter device is provided with dehvery pump two, pipeline between described intermediate storage tank two and described Ceramic excessive filtration device is provided with dehvery pump three, impurity filtrate in described ceramic micro filter device flows into described syrup original fluid container by back of pipeline, the impurity filtrate of described Ceramic excessive filtration device flows into described intermediate storage tank one by back of pipeline, described multi-layer plate-type rough filtering device is provided with pressure controller one, described ceramic micro filter device is provided with pressure controller two, described Ceramic excessive filtration device is provided with pressure controller three.Described syrup original fluid container is communicated with the syrup stoste workshop of preceding working procedure by carrying out pipe material, and the syrup refined liquid that described Ceramic excessive filtration device leaches enters next process through charging line, continues deep processing as added batching or enters packing shop etc.
On the basis of technique scheme, the utility model also can do following technological improvement:
Further, every laminate of described multi-layer plate-type rough filtering device is by the sponge of food-grade stainless (steel) wire and upper laying thereof or fiber filter cloth composition.Stainless (steel) wire and sponge or fiber filter cloth carry out preliminary treatment to syrup stoste, can make the whole filtering of the impurity of particle diameter more than 50 μm.
Further, the sponge on described stainless (steel) wire or fiber filter cloth replaceable.This device is when designing, and stainless (steel) wire can the support body level of this device relatively skid off, and drawer-like structure, can change online sponge or fiber filter cloth during extraction.
Further, described ceramic micro filter device filters cylinder by many row of horizontal horizontal type and forms, and is equiped with ceramic micro filter film in described filtration cylinder.
Further, the filter opening diameter of described ceramic micro filter film is 5 ~ 20 μm.This microfiltration membranes can the impurity of more than 20 μm in filtering syrup.
Further, described Ceramic excessive filtration device filters cylinder by many row of horizontal horizontal type and forms, and is equiped with ceramic super-filtering film in described filtration cylinder.
Further, the filter opening diameter of described ceramic super-filtering film is 20 ~ 30nm.This milipore filter can the impurity of more than 30nm in filtering syrup.
Further, the available pressure limit of described pressure controller one is 1 ~ 1.5MPa, and the available pressure limit of described pressure controller two is 0.5 ~ 0.8MPa, and the available pressure limit of described pressure controller three is 0.1 ~ 0.3MPa.
The beneficial effects of the utility model are: before syrup carries out hyperfiltration treatment, be disposed with coarse filtration and micro-filtration, the syrup of hyperfiltration treatment is not containing the impurity that particle diameter is excessive, ensure that the filter opening of milipore filter is not easily blocked, pressure controllable during ultrafiltration can filter smoothly syrup in suitable scope, milipore filter long service life, changes once for 1 to two years; Intermediate storage tank one is provided with between rough filtering device and micro-filtration, intermediate storage tank two is provided with between micro-filtration and ultrafiltration apparatus, when needing in production process to change sponge, filter cloth or microfiltration membranes, whole production equipment is not needed to stop, because there being the existence of intermediate storage tank one or two, its back segment process for refining can normally carry out, and enhances productivity.
Accompanying drawing explanation
The structural representation of the membrane filtration system refined for syrup that Fig. 1 provides for the utility model.
Component names in accompanying drawing representated by each label is as follows:
1, syrup original fluid container; 2, multi-layer plate-type rough filtering device; 3, intermediate storage tank one; 4, ceramic micro filter device; 5, intermediate storage tank two; 6, Ceramic excessive filtration device; 7, dehvery pump one; 8, dehvery pump two; 9, dehvery pump three; 10, pressure controller one; 11, pressure controller two; 12, pressure controller three.
Detailed description of the invention
Be described principle of the present utility model and feature below in conjunction with accompanying drawing, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
As shown in Figure 1, the utility model provides a kind of membrane filtration system refining for syrup, comprise successively by the syrup original fluid container 1 of pipeline communication, multi-layer plate-type rough filtering device 2, intermediate storage tank 1, ceramic micro filter device 4, intermediate storage tank 25 and Ceramic excessive filtration device 6, pipeline between described syrup original fluid container 1 and multi-layer plate-type rough filtering device 2 is provided with dehvery pump 1, dehvery pump 28 is provided with between described intermediate storage tank 1 and ceramic micro filter device 4, dehvery pump 39 is provided with between described intermediate storage tank 25 and described Ceramic excessive filtration device 6, impurity filtrate in described ceramic micro filter device 4 flows into described syrup original fluid container 1 by back of pipeline, the impurity filtrate of described Ceramic excessive filtration device 6 flows into described intermediate storage tank 1 by back of pipeline, described multi-layer plate-type rough filtering device 2 is provided with pressure controller 1, described ceramic micro filter device 4 is provided with pressure controller 2 11, described Ceramic excessive filtration device 6 is provided with pressure controller 3 12.
On the basis of technique scheme, the utility model also can do following technological improvement:
Further, every laminate of described multi-layer plate-type rough filtering device 2 is by the sponge of food-grade stainless (steel) wire and upper laying thereof or fiber filter cloth composition.Stainless (steel) wire and sponge or fiber filter cloth carry out preliminary treatment to syrup stoste, can make the whole filtering of the impurity of particle diameter more than 50 μm.
Further, the sponge on described stainless (steel) wire or fiber filter cloth replaceable.
Further, described ceramic micro filter device 4 filters cylinder by many row of horizontal horizontal type and forms, and is equiped with ceramic micro filter film in described filtration cylinder.
Further, the filter opening diameter of described ceramic micro filter film is 5 ~ 20 μm.
Further, described Ceramic excessive filtration device 6 filters cylinder by many row of horizontal horizontal type and forms, and is equiped with ceramic super-filtering film in described filtration cylinder.
Further, the filter opening diameter of described ceramic super-filtering film is 20 ~ 30nm.
Further, the available pressure limit of described pressure controller 1 is 1 ~ 1.5MPa, and the available pressure limit of described pressure controller 2 11 is 0.5 ~ 0.8MPa, and the available pressure limit of described pressure controller 3 12 is 0.1 ~ 0.3MPa.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (8)
1. the membrane filtration system refined for syrup, it is characterized in that, comprise successively by the syrup original fluid container (1) of pipeline communication, multi-layer plate-type rough filtering device (2), intermediate storage tank one (3), ceramic micro filter device (4), intermediate storage tank two (5) and Ceramic excessive filtration device (6), pipeline between described syrup original fluid container (1) and multi-layer plate-type rough filtering device (2) is provided with dehvery pump one (7), pipeline between described intermediate storage tank one (3) and ceramic micro filter device (4) is provided with dehvery pump two (8), pipeline between described intermediate storage tank two (5) and described Ceramic excessive filtration device (6) is provided with dehvery pump three (9), impurity filtrate in described ceramic micro filter device (4) flows into described syrup original fluid container (1) by back of pipeline, the impurity filtrate of described Ceramic excessive filtration device (6) flows into described intermediate storage tank one (3) by back of pipeline, described multi-layer plate-type rough filtering device (2) is provided with pressure controller one (10), described ceramic micro filter device (4) is provided with pressure controller two (11), described Ceramic excessive filtration device (6) is provided with pressure controller three (12).
2. a kind of membrane filtration system refining for syrup according to claim 1, is characterized in that, every laminate of described multi-layer plate-type rough filtering device (2) is by the sponge of food-grade stainless (steel) wire and upper laying thereof or fiber filter cloth composition.
3. a kind of membrane filtration system refining for syrup according to claim 2, is characterized in that, the sponge on described stainless (steel) wire or fiber filter cloth replaceable.
4. a kind of membrane filtration system refining for syrup according to claim 1, is characterized in that, described ceramic micro filter device (4) is filtered cylinder by many row of horizontal horizontal type and formed, and is equiped with ceramic micro filter film in described filtration cylinder.
5. a kind of membrane filtration system refining for syrup according to claim 4, it is characterized in that, the filter opening diameter of described ceramic micro filter film is 5 ~ 20 μm.
6. a kind of membrane filtration system refining for syrup according to claim 1, is characterized in that, described Ceramic excessive filtration device (6) is filtered cylinder by many row of horizontal horizontal type and formed, and is equiped with ceramic super-filtering film in described filtration cylinder.
7. a kind of membrane filtration system refining for syrup according to claim 6, it is characterized in that, the filter opening diameter of described ceramic super-filtering film is 20 ~ 30nm.
8. a kind of membrane filtration system refining for syrup according to any one of claim 1 to 7, it is characterized in that, the available pressure limit of described pressure controller one (10) is 1 ~ 1.5MPa, the available pressure limit of described pressure controller two (11) is 0.5 ~ 0.8MPa, and the available pressure limit of described pressure controller three (12) is 0.1 ~ 0.3MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520712313.XU CN204952454U (en) | 2015-09-15 | 2015-09-15 | Be used for refine membrane filtration system of syrup |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520712313.XU CN204952454U (en) | 2015-09-15 | 2015-09-15 | Be used for refine membrane filtration system of syrup |
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| Publication Number | Publication Date |
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| CN204952454U true CN204952454U (en) | 2016-01-13 |
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| CN201520712313.XU Active CN204952454U (en) | 2015-09-15 | 2015-09-15 | Be used for refine membrane filtration system of syrup |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106901322A (en) * | 2017-04-13 | 2017-06-30 | 盐城宇峰食品科技有限公司 | A kind of jam is syrup dedicated and preparation method thereof |
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2015
- 2015-09-15 CN CN201520712313.XU patent/CN204952454U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106901322A (en) * | 2017-04-13 | 2017-06-30 | 盐城宇峰食品科技有限公司 | A kind of jam is syrup dedicated and preparation method thereof |
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