CN206463617U - A kind of L alanine microporous filter pipeline surplus material recovery device - Google Patents
A kind of L alanine microporous filter pipeline surplus material recovery device Download PDFInfo
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- CN206463617U CN206463617U CN201720156165.7U CN201720156165U CN206463617U CN 206463617 U CN206463617 U CN 206463617U CN 201720156165 U CN201720156165 U CN 201720156165U CN 206463617 U CN206463617 U CN 206463617U
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- valve
- connecting pipe
- filter
- microporous filter
- prefilter
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Abstract
The utility model provides a kind of L alanine microporous filter pipeline surplus material recovery device, including：Bleacher, pump, microporous filter and crystallization concentration tank are dissolved, valve one is housed on the connecting pipe of dissolving bleacher and pump；Valve two is housed on the connecting pipe of pump and microporous filter；Microporous filter outlet is connected with dissolving bleacher and prefilter respectively, is exported in microporous filter and valve three is housed on the connecting pipe with dissolving bleacher, connected on connecting pipe of the microporous filter outlet with prefilter and be connected with valve four and valve five；The prefilter is connected with fine filter by pipeline, and valve six is provided with connecting pipe of the fine filter with crystallization concentration tank；Water purification equipment and air compressor are connected with by pipeline parallel connection on the connecting pipe of valve five and prefilter, and are respectively provided with connecting pipe valve seven and valve eight.The utility model has the advantages that to improve product quality, reduce environmental pollution and save the energy.
Description
Technical field
The utility model is related to the retracting device of amino acids production clout, specially a kind of ALANINE microporous filter pipe
Road surplus material recovery device.
Background technology
In process of production, the processing procedure of its intermediate mainly includes ALANINE：Dissolved simultaneously in dissolving bleacher
Decolourized with activated carbon, then destainer enters microporous filter, the destainer after filtering enters crystallization concentration tank and tied
Crystalline substance concentration.In the process, the clout for being introduced into crystallization concentration tank can be remained in pipeline, the processing mode to clout is included to remaining
The method that material is washed using water top makes it into crystallization concentration tank or emptied with air, when with water top washing method, due to existing
Used in technology and the whole pipe-line system after dissolving bleacher is rinsed, so as to water consumption can be caused many, cause water to enter
The amount of crystallization concentration tank increases, and causes the steam wasting of resources, meanwhile, have a strong impact on crystallization rate；But use what air was emptied
Mode then pollutes the environment and causes feed liquid to waste；Further, since microporous filter is built with carbon-point, carbon-point holds as consumptive material
Easily it is damaged, and does not have equipment presence between microporous filter and crystallization concentration tank, the carbon-point of damage then can be dense into crystallizing
Contracting tank, causes the pollution of feed liquid.
The content of the invention
In consideration of it, the utility model provides a kind of ALANINE microporous filter pipeline surplus material recovery device, it is specially
A kind of feed liquid is recyclable to decolourize and filtering, feed liquid enter crystallization concentration tank, purified water and clean after prefilter and fine filter
Net air can be segmented the pipeline surplus material recovery device into pipeline as needed.Decolourize and filter by circulating, feed liquid can be improved
Into clarity during pretreatment tank；The setting of prefilter and fine filter can both ensure the filtering accuracy and matter of feed liquid
Amount, in the case where carbon-point is damaged, can ensure the quality of feed liquid in crystallization concentration tank again；Point of purified water and pure air
When, segmentation add can both save the energy, the yield of product can be improved again.
On the basis of existing technology, the utility model is reclaimed there is provided a kind of ALANINE microporous filter pipeline clout
Device, including：Bleacher, pump, microporous filter and crystallization concentration tank are dissolved, is filled on the connecting pipe of dissolving bleacher and pump
There is valve one；Valve two is housed on the connecting pipe of pump and microporous filter；Decolourized respectively with dissolving microporous filter outlet
Tank and prefilter connection, export in microporous filter and valve three are housed on the connecting pipe with dissolving bleacher, in micropore mistake
Filter outlet is connected with valve four and valve five with being connected on the connecting pipe of prefilter；The prefilter leads to fine filter
Piping is connected, and valve six is provided with connecting pipe of the fine filter with crystallization concentration tank；In valve five and prefilter
Water purification equipment and air compressor are connected with by pipeline parallel connection on connecting pipe, and are respectively provided with connecting pipe valve seven
With valve eight.
Export to be equipped with the connecting pipe with prefilter in microporous filter and regard hydroscope one.
It is equipped with the connecting pipe of valve four and valve five and regards hydroscope two.
The prefilter is sterilizing filter, and filtering accuracy is 0.22 μm.
The fine filter is sterilizing filter, and filtering accuracy is 0.1 μm.
Valve four and on the connecting pipe of hydroscope two be equipped with valve nine.
The beneficial effects of the utility model：By setting prefilter and fine filter, filtering accuracy can be effectively improved,
Simultaneously can be when carbon-point be damaged, it is ensured that crystallize the quality of feed liquid in concentration tank, in addition, passing through prefilter and fine filter
Set, it is ensured that the aseptic filtration of feed liquid, moreover it is possible to the effective generation for reducing finished product stain color dot, improve product quality；Pass through
Air compressor and water purification equipment are set, and reasonable Arrangement is carried out to its position, it is possible to reduce 90% purified water enters crystallization
Concentration tank, so as to save crystallization concentration time, improve production efficiency and reduce the wasting of resources；Water purification equipment coordinates the He of valve seven
Valve six, can make the clout in pipeline by the back dissolving solution bleacher of purified water top, participating in the ALANINE intermediate of next group
Dissolving is decolourized, and it is about 20 ~ 30kg that every batch, which is improved yield,；Air compressor coordinates valve eight and valve six, can will be residual in pipeline
Water is blown in dissolving bleacher, reduces environmental protection pressure；In addition, the setting of valve nine can be arranged whole surplus material recovery device
Sky, makes do not have any material to exist in pipeline.
Brief description of the drawings
Fig. 1 is ALANINE microporous filter pipeline surplus material recovery device side view.
In figure, 1- dissolving bleachers, 2- pumps, 3- microporous filters, 4- crystallization concentration tanks, 5- valves one, 6- valves two, 7-
Prefilter, 8- valves three, 9- regards hydroscope one, and 10- valves four, 11- valves five, 12- regards hydroscope two, 13- valves nine, 14- essences
Filter, 15- valves six, 16- water purification equipments, 17- air compressors, 18- valves seven, 19- valves eight.
Embodiment
The utility model is described in detail below in conjunction with the accompanying drawings.
As shown in figure 1, the utility model provides a kind of ALANINE microporous filter pipeline surplus material recovery device, bag
Include：Bleacher 1, pump 2, microporous filter 3 and crystallization concentration tank 4 are dissolved, is filled on the connecting pipe of dissolving bleacher 1 and pump 2
There is valve 1；Valve 26 is housed on the connecting pipe of pump 2 and microporous filter 3；Microporous filter 3 export respectively with dissolving
Bleacher 1 and prefilter 7 are connected, and exported in microporous filter 3 and valve 38 is housed on the connecting pipe with dissolving bleacher 1,
It is equipped with connecting pipe of the valve 38 with dissolving bleacher 1 and regards hydroscope 1；In the outlet of microporous filter 3 and prefilter 7
Connecting pipe on series connection be connected with valve 4 10 and valve 5 11, equipped with regarding on the connecting pipe of valve 4 10 and valve 5 11
Hydroscope 2 12；Valve 4 10 and on the connecting pipe of hydroscope 2 12 be equipped with valve 9 13；The prefilter 7 is filtered with essence
Device 14 is connected by pipeline, and valve 6 15 is provided with connecting pipe of the fine filter 14 with crystallization concentration tank 4；In valve 5 11
With water purification equipment 16 and air compressor 17 are connected with by pipeline parallel connection on the connecting pipe of prefilter 7, and in connecting tube
Valve 7 18 and valve 8 19 are respectively provided with road.
The prefilter 7 is sterilizing filter, and filtering accuracy is 0.22 μm.
The fine filter 14 is sterilizing filter, and filtering accuracy is 0.1 μm.
Occupation mode of the present utility model：After ALANINE intermediate is decolourized into dissolving bleacher 1, pass through pump 2
Effect, makes destainer enter microporous filter 3, Open valve 38, by being observed regarding hydroscope 1 by valve 1, valve 26
The clarification situation of feed liquid, after solution clarification, Open valve 4 10, feed liquid depending on hydroscope 2 12 and valve 5 11 by entering pre-filtering
Device 7 and fine filter 14, then enter crystallization concentration tank 4 by valve 6 15, complete decolouring, the mistake of ALANINE intermediate
Filter, crystallization concentration process；Open water purification equipment 16 and valve 7 18 and close valve 5 11, purified water is entered prefilter
7 and fine filter 14 pass through valve 6 15 enter crystallization concentration tank 4；Valve 6 15 and Open valve 5 11 are closed, makes purified water
Into dissolving bleacher 1, the cleaning of complete twin conduit clout；Water purification equipment 16 is closed, air compressor 17 is opened, makes pure
Air enters pipeline by valve 8 19, and the remaining water in pipeline is blown into dissolving bleacher 1, after terminating, and closes air compression
Machine 17 and valve 8 19, Open valve 9 13 are emptied to pipeline.
Claims (6)
1. a kind of ALANINE microporous filter pipeline surplus material recovery device, it is characterised in that including：Dissolve bleacher, it is pump, micro-
Hole filter and crystallization concentration tank, are equipped with valve one on the connecting pipe of dissolving bleacher and pump；In pump and microporous filter
Connecting pipe on be equipped with valve two；Microporous filter outlet is connected with dissolving bleacher and prefilter respectively, in micropore mistake
Filter is exported and valve three is housed on the connecting pipe with dissolving bleacher, and the connecting tube with prefilter is exported in microporous filter
Series connection is connected with valve four and valve five on road；The prefilter is connected with fine filter by pipeline, in fine filter and knot
The connecting pipe of brilliant concentration tank is provided with valve six；It is connected with the connecting pipe of valve five and prefilter by pipeline parallel connection
Water purification equipment and air compressor, and it is respectively provided with connecting pipe valve seven and valve eight.
2. ALANINE microporous filter pipeline surplus material recovery device as claimed in claim 1, it is characterised in that in micropore mistake
Filter, which exports to be equipped with the connecting pipe with prefilter, regards hydroscope one.
3. ALANINE microporous filter pipeline surplus material recovery device as claimed in claim 1, it is characterised in that in valve four
Hydroscope two is regarded with being equipped with the connecting pipe of valve five.
4. ALANINE microporous filter pipeline surplus material recovery device as claimed in claim 1, it is characterised in that the pre- mistake
Filter is sterilizing filter, and filtering accuracy is 0.22 μm.
5. ALANINE microporous filter pipeline surplus material recovery device as claimed in claim 1, it is characterised in that the smart mistake
Filter is sterilizing filter, and filtering accuracy is 0.1 μm.
6. ALANINE microporous filter pipeline surplus material recovery device as claimed in claim 3, it is characterised in that in valve four
With on the connecting pipe of hydroscope two be equipped with valve nine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720156165.7U CN206463617U (en) | 2017-02-21 | 2017-02-21 | A kind of L alanine microporous filter pipeline surplus material recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720156165.7U CN206463617U (en) | 2017-02-21 | 2017-02-21 | A kind of L alanine microporous filter pipeline surplus material recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206463617U true CN206463617U (en) | 2017-09-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720156165.7U Active CN206463617U (en) | 2017-02-21 | 2017-02-21 | A kind of L alanine microporous filter pipeline surplus material recovery device |
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| Country | Link |
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| CN (1) | CN206463617U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108484422A (en) * | 2018-05-29 | 2018-09-04 | 成都本则生科技有限公司 | The purified crystals technique and its system of Beta-alanine are extracted from enzymatic conversion liquid |
-
2017
- 2017-02-21 CN CN201720156165.7U patent/CN206463617U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108484422A (en) * | 2018-05-29 | 2018-09-04 | 成都本则生科技有限公司 | The purified crystals technique and its system of Beta-alanine are extracted from enzymatic conversion liquid |
| CN108484422B (en) * | 2018-05-29 | 2022-01-07 | 成都本则生科技有限公司 | Purification and crystallization process for extracting beta-alanine from enzyme conversion solution and system thereof |
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