CN203976680U - A kind of refining plant of high purity taurine - Google Patents
A kind of refining plant of high purity taurine Download PDFInfo
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- CN203976680U CN203976680U CN201420371191.8U CN201420371191U CN203976680U CN 203976680 U CN203976680 U CN 203976680U CN 201420371191 U CN201420371191 U CN 201420371191U CN 203976680 U CN203976680 U CN 203976680U
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Abstract
The utility model provides a kind of refining plant of high purity taurine.It is by bleacher (1), pressure filter (2), anion-exchange column (3), cationic exchange coloum (4), receiving tank (5), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), depending on cup (9), bleacher baiting valve (10), gac outlet (11), pressure filter outlet valve (12), washing water baiting valve (13), anion-exchange column baiting valve (14), resin activated acids feed valve (15), anion-exchange column outlet valve (16), cationic exchange coloum baiting valve (17), resin activation alkali imported valve (18), cationic exchange coloum outlet valve (19), storage tank vent valve (20), bleacher stirs (21), bleacher opening for feed (22) composition.The utility model adopts activated carbon decolorizing, filtration, anion-cation exchange resin to obtain highly purified taurine after processing.The refining number of times of the method taurine is few, and product yield is high, and purity is high, with short production cycle.
Description
Technical field
The utility model provides a kind of refining plant of high purity taurine, belongs to pharmaceutical equipment field.
Background technology
Taurine be a kind of needed by human with amino sulfonic acid (not being amino acid), all playing the part of important role maintaining aspect brain running and development.The hyperplasia of taurine energy promoting nerve unit and the effect of prolongation.Also be conducive to cell moves and increases neural axon simultaneously in brain.Maintaining aspect the potential balance of cytolemma in addition, taurine is no less important also.Because it can help ionogen as potassium, sodium, calcium and magnesia turnover cell, thus the function of reinforcement brain.
The taurine that my company produces is at present synthetics, and product needed, through refining crystallization repeatedly, just can reach the standard that expensive goods adds, and due to repeatedly refining, causes product yield low, and cost is high.
Summary of the invention
The purpose of this utility model is to provide a kind of refining plant of high purity taurine, adopts activated carbon decolorizing, filtration, anion-cation exchange resin to obtain highly purified taurine after processing.The refining number of times of the method taurine is few, and product yield is high, and purity is high, with short production cycle.
The utility model is achieved in that it is by bleacher (1), pressure filter (2), anion-exchange column (3), cationic exchange coloum (4), receiving tank (5), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), depending on cup (9), bleacher baiting valve (10), gac outlet (11), pressure filter outlet valve (12), washing water baiting valve (13), anion-exchange column baiting valve (14), resin activated acids feed valve (15), anion-exchange column outlet valve (16), cationic exchange coloum baiting valve (17), resin activation alkali imported valve (18), cationic exchange coloum outlet valve (19), storage tank vent valve (20), bleacher stirs (21), bleacher opening for feed (22) composition.
Opening for feed (22), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), bleacher stirring (21) are housed on bleacher (1), bleacher bottom is equipped with and is looked cup (9), depending on cup (9) below, bleacher baiting valve (10) is housed, bleacher baiting valve (10) is connected with pressure filter (2), gac outlet (11) is equipped with in pressure filter (2) top, pressure filter outlet valve (12) is equipped with in below, and pressure filter outlet valve (12) is connected with anion-exchange column baiting valve (14) with washing water baiting valve (13) respectively; Anion-exchange column (3) lower end is connected with anion-exchange column baiting valve (14), upper end is connected with anion-exchange column outlet valve (16) with resin activated acids feed valve (15) respectively, and anion-exchange column outlet valve (16) is connected with cationic exchange coloum baiting valve (17) with cationic exchange coloum (4) bottom; Cationic exchange coloum (4) bottom is connected with cationic exchange coloum baiting valve (17) with anion-exchange column outlet valve (16) respectively, and cationic exchange coloum (4) top is connected with cationic exchange coloum outlet valve (19) with resin activation alkali imported valve (18) respectively; Storage tank vent valve (20) is equipped with on receiving tank (5) top, and another outlet of receiving tank (5) top is connected with cationic exchange coloum outlet valve (19).
The taurine refining plant of said structure, refining number of times is few, and product yield is high, and purity is high, with short production cycle.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model.
In accompanying drawing 1: the 1st, bleacher, the 2nd, pressure filter, the 3rd, anion-exchange column, the 4th, cationic exchange coloum, the 5th, receiving tank, the 6th, pressurized air valve, the 7th, vapour outlet valve, the 8th, steam inlet valve, the 9th, depending on cup, the 10th, bleacher baiting valve, the 11st, gac outlet, the 12nd, pressure filter outlet valve, the 13rd, washing water baiting valve, the 14th, anion-exchange column baiting valve, the 15th, resin activated acids feed valve, the 16th, anion-exchange column outlet valve, the 17th, cationic exchange coloum baiting valve, the 18th, resin activation alkali imported valve, the 19th, cationic exchange coloum outlet valve, the 20th, storage tank vent valve, the 21st, bleacher stirs, the 22nd, bleacher opening for feed.
Embodiment
Below in conjunction with accompanying drawing 1, concrete structure of the present utility model and using method are described.
As shown in Figure 1, the taurine refining plant of the utility model, it is by bleacher (1), pressure filter (2), anion-exchange column (3), cationic exchange coloum (4), receiving tank (5), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), depending on cup (9), bleacher baiting valve (10), gac outlet (11), pressure filter outlet valve (12), washing water baiting valve (13), anion-exchange column baiting valve (14), resin activated acids feed valve (15), anion-exchange column outlet valve (16), cationic exchange coloum baiting valve (17), resin activation alkali imported valve (18), cationic exchange coloum outlet valve (19), storage tank vent valve (20), bleacher stirs (21), bleacher opening for feed (22) composition.
Bleacher opening for feed (22) is housed on bleacher (1), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), bleacher stirs (21), bleacher bottom is equipped with and is looked cup (9), depending on cup (9) below, bleacher baiting valve (10) is housed, bleacher baiting valve (10) is connected with pressure filter (2), gac outlet (11) is equipped with in pressure filter (2) top, pressure filter outlet valve (12) is equipped with in below, pressure filter outlet valve (12) is connected with anion-exchange column baiting valve (14) with washing water baiting valve (13) respectively, anion-exchange column (3) lower end is connected with anion-exchange column baiting valve (14), upper end is connected with anion-exchange column outlet valve (16) with resin activated acids feed valve (15) respectively, and anion-exchange column outlet valve (16) is connected with cationic exchange coloum baiting valve (17) with cationic exchange coloum (4) bottom, cationic exchange coloum (4) bottom is connected with cationic exchange coloum baiting valve (17) with anion-exchange column outlet valve (16) respectively, and cationic exchange coloum (4) top is connected with cationic exchange coloum outlet valve (19) with resin activation alkali imported valve (18) respectively, storage tank vent valve (20) is equipped with on receiving tank (5) top, and another outlet of receiving tank (5) top is connected with cationic exchange coloum outlet valve (19).
When operation, first bleacher baiting valve (10) is closed, material is added in bleacher (1) by opening for feed (22), open vapour outlet valve (7) and steam inlet valve (8), pass into steam and heat, start bleacher simultaneously and stir (21), after decolouring, steam off outlet valve (7) and steam inlet valve (8), stop heating, closes simultaneously
Bleacher opening for feed (22), stop stirring, by gac outlet (11), washing water baiting valve (13), resin activated acids feed valve (15), cationic exchange coloum baiting valve (17), resin activation alkali imported valve (18) is closed, by pressure filter outlet valve (12), anion-exchange column baiting valve (14), anion-exchange column outlet valve (16), cationic exchange coloum outlet valve (19), storage tank vent valve (20) is opened, and then bleacher baiting valve (10) and pressurized air valve (6) are opened, start press filtration, carry out entering in receiving tank after cation and anion exchange simultaneously, distill again, concentrated, crystallization, dry, pack and obtain high purity taurine.
Detect according to the national standard of foodstuff additive taurine " National Standard of the People's Republic of China " GB14759-2010, three batch sample detected results are as follows:
Claims (1)
1. the refining plant of a high purity taurine, it is characterized in that, it is by bleacher (1), pressure filter (2), anion-exchange column (3), cationic exchange coloum (4), receiving tank (5), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), depending on cup (9), bleacher baiting valve (10), gac outlet (11), pressure filter outlet valve (12), washing water baiting valve (13), anion-exchange column baiting valve (14), resin activated acids feed valve (15), anion-exchange column outlet valve (16), cationic exchange coloum baiting valve (17), resin activation alkali imported valve (18), cationic exchange coloum outlet valve (19), storage tank vent valve (20), bleacher stirs (21), bleacher opening for feed (22) composition,
Opening for feed (22), pressurized air valve (6), vapour outlet valve (7), steam inlet valve (8), bleacher stirring (21) are housed on bleacher (1), bleacher bottom is equipped with and is looked cup (9), depending on cup (9) below, bleacher baiting valve (10) is housed, bleacher baiting valve (10) is connected with pressure filter (2), gac outlet (11) is equipped with in pressure filter (2) top, pressure filter outlet valve (12) is equipped with in below, and pressure filter outlet valve (12) is connected with anion-exchange column baiting valve (14) with washing water baiting valve (13) respectively; Anion-exchange column (3) lower end is connected with anion-exchange column baiting valve (14), upper end is connected with anion-exchange column outlet valve (16) with resin activated acids feed valve (15) respectively, and anion-exchange column outlet valve (16) is connected with cationic exchange coloum baiting valve (17) with cationic exchange coloum (4) bottom; Cationic exchange coloum (4) bottom is connected with cationic exchange coloum baiting valve (17) with anion-exchange column outlet valve (16) respectively, and cationic exchange coloum (4) top is connected with cationic exchange coloum outlet valve (19) with resin activation alkali imported valve (18) respectively; Storage tank vent valve (20) is equipped with on receiving tank (5) top, and another outlet of receiving tank (5) top is connected with cationic exchange coloum outlet valve (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420371191.8U CN203976680U (en) | 2014-07-07 | 2014-07-07 | A kind of refining plant of high purity taurine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420371191.8U CN203976680U (en) | 2014-07-07 | 2014-07-07 | A kind of refining plant of high purity taurine |
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| CN203976680U true CN203976680U (en) | 2014-12-03 |
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| CN201420371191.8U Active CN203976680U (en) | 2014-07-07 | 2014-07-07 | A kind of refining plant of high purity taurine |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452136A (en) * | 2019-07-10 | 2019-11-15 | 湖北远大生命科学与技术有限责任公司 | A method of preparing taurine |
| CN110483342A (en) * | 2019-09-02 | 2019-11-22 | 潜江永安药业股份有限公司 | A kind of method and removal of impurities recovery system of taurine mother liquor removal of impurities recycling |
-
2014
- 2014-07-07 CN CN201420371191.8U patent/CN203976680U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452136A (en) * | 2019-07-10 | 2019-11-15 | 湖北远大生命科学与技术有限责任公司 | A method of preparing taurine |
| CN110483342A (en) * | 2019-09-02 | 2019-11-22 | 潜江永安药业股份有限公司 | A kind of method and removal of impurities recovery system of taurine mother liquor removal of impurities recycling |
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