CN103012622B - Entirely-stirring tank used for heparin sodium extraction process - Google Patents
Entirely-stirring tank used for heparin sodium extraction process Download PDFInfo
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- CN103012622B CN103012622B CN201210537757.5A CN201210537757A CN103012622B CN 103012622 B CN103012622 B CN 103012622B CN 201210537757 A CN201210537757 A CN 201210537757A CN 103012622 B CN103012622 B CN 103012622B
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- heparin sodium
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Abstract
The invention relates to a stirring tank, and particularly relates to a stirring tank body used for a heparin sodium extraction process. The problem to be solved is to provide an entirely-stirring tank used for the heparin sodium extraction process. With the adoption of the entirely-stirring tank provided by the invention, a material is sufficiently stirred while reaction time is reduced by 3-4 hours, so that the yield is higher than the yield of a traditional tank body. A pipeline opening is formed outside the tank body, and the outside of the tank body is connected with a high-pressure drainage pump at the bottom; and a valve is arranged on a pipeline. In the prior art, an auxiliary material or alkaline water needs to be manually added in a reaction process. With the adoption of the entirely-stirring tank provided by the invention, automatic stirring can be realized through one-off pouring. With the adoption of the manner, the addition is more uniform, and the reaction rate is higher.
Description
Technical field
The present invention relates to a kind of stirred pot, specially refer to the stirring tank body using for heparin sodium leaching process.
Background technology
Heparin sodium is in logical large intestine small intestine, to extract and obtain, under normal circumstances, from decomposing, quite long to collecting most the time used, its process is quite complicated, with regard to present circumstances, general reaction once, take the time of several days, and its output capacity is quite low, the main problem that just relates to a tank body in the middle of this, certainly main relating to, the problem stirring, because stirring body is the material in intestines, its speed can not be too fast, also to ensure that the added ingredients adding is quite even simultaneously, only in this way could shorten the time, another side, just because of in adding procedure, what adopt is to manually add, as long as think and pour into, anyway the inside has caused in the thought concept stirring, react insufficient, this is when entering also to have comprised non-uniform temperature, and whether entering of additive contacts with whole materials at short notice, and quick response problem.
Summary of the invention
Problem to be solved by this invention is to provide a kind of complete stirred pot for heparin sodium leaching process, and it can, ensure well-beaten reaction times shortening three to four hours that allow of material simultaneously, allow output capacity react higher than traditional tank body.
For completing foregoing invention object, the present invention is achieved in that a kind of complete stirred pot for heparin sodium leaching process, and its main body is a tank body, is provided with agitator, inwall middle portion is provided with temperature inductor in tank body; Liquid level meter is all equipped with in upper and lower; Described temperature inductor is all connected with watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of tank body; Upper and lower by the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is double-layer hollow rotating shaft, has shaft seat in the bottom of rotating shaft; Shaft seat is hollow, and shaft seat is provided with fluid inlet; At the bottom of tank, establish drainage pump; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to High Voltage by pipeline and draws pump outlet; The import of described drainage pump connects in the edge collector with tank base.This patent adopts high-voltage bidirectional drainage, allows the material in tank thoroughly roll, and there is no dead point, sediment-free.
Technique scheme is improved further, and described edge collector invests wall at the bottom of tank, is cavity-like, has certain height; Be connected to the entrance of drainage pump by pipeline, collector top has some Chen Ji to reclaim mouth.Because tank body is very large, often throw out can stay in bottom week, and, what tank body adopted is steam heating, and therefore, the content of this part is difficult to heated or reaction, need to after collecting, be reintroduced back to, allow the content of this part ceaselessly exchange with top, thereby form inner stream material, final solution Dead Core Problems in the past.Design several Chen Ji and reclaim mouth, and be not the notch of open type, be connected with the pump housing again in the position being staggered with Chen Ji recovery mouth; Can allow like this sufficient movement in cavity, and can in tank, form many places whirling current, thereby increase mixing effect.
Technique scheme is improved further, is provided with a pipeline opening in tank body outside, be connected with bottom drainage pump; Its pipeline is provided with valve.In the prior art, in reaction process, need to add auxiliary material or buck, be all manually to add, and this disposable pouring into, then by naturally stirring.And the interpolation of the manner is evener all, reactivity is higher.
Technique scheme is improved further, and its inside of described shaft seat is connected with the skin of double-layer hollow rotating shaft, and the center of double-layer hollow rotating shaft is main drive shaft; Main drive shaft, through shaft seat, is connected with the bearing of shaft seat bottom.Described sprinkler head is opened in double-layer hollow axle middle and upper part.The design of double-layer hollow axle, allows spray and be rotated into be integrated, and reduces on the one hand the volatilization of heat, reduces on the other hand taking of the interior space of tank.
Brief description of the drawings
Fig. 1 is structural representation of the present invention.
Embodiment
As shown in the figure, a kind of complete stirred pot for heparin sodium leaching process, its main body is a tank body, is provided with agitator, inwall middle portion is provided with temperature inductor in tank body; Liquid level meter is all equipped with in upper and lower; Described temperature inductor is all connected with watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of tank body; Upper and lower by the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is double-layer hollow rotating shaft, has shaft seat in the bottom of rotating shaft; Shaft seat is hollow, and shaft seat is provided with fluid inlet; At the bottom of tank, establish drainage pump; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to High Voltage by pipeline and draws pump outlet; The import of described drainage pump connects in the edge collector with tank base.This patent adopts high-voltage bidirectional drainage, allows the material in tank thoroughly roll, and there is no dead point, sediment-free.
Described edge collector invests wall at the bottom of tank, is cavity-like, has certain height; Its portion is connected to the entrance of drainage pump by pipeline, collector top has some Chen Ji to reclaim mouth.Because tank body is very large, often throw out can stay in bottom week, and, what tank body adopted is steam heating, and therefore, the content of this part is difficult to heated or reaction, need to after collecting, be reintroduced back to, allow the content of this part ceaselessly exchange with top, thereby form inner stream material, final solution Dead Core Problems in the past.Design several Chen Ji and reclaim mouth, and be not the notch of open type, be connected with the pump housing again in the position being staggered with Chen Ji recovery mouth; Can allow like this sufficient movement in cavity, and can in tank, form many places whirling current, thereby increase mixing effect.
Be provided with a pipeline opening in tank body outside, be connected with bottom drainage pump; Its pipeline is provided with valve.In the prior art, in reaction process, need to add auxiliary material or buck, be all manually to add, and this disposable pouring into, then by naturally stirring.And the interpolation of the manner is evener all, reactivity is higher.
Technique scheme is improved further, and its inside of described shaft seat is connected with the skin of double-layer hollow rotating shaft, and the center of double-layer hollow rotating shaft is main drive shaft; Main drive shaft, through shaft seat, is connected with the bearing of shaft seat bottom.Described sprinkler head is opened in double-layer hollow axle middle and upper part.The design of double-layer hollow axle, allows spray and be rotated into be integrated, and reduces on the one hand the volatilization of heat, reduces on the other hand taking of the interior space of tank.
Claims (3)
1. for a complete stirred pot for heparin sodium leaching process, its main body is a tank body, is provided with agitator, inwall middle portion is provided with temperature inductor in tank body; Liquid level meter is all equipped with in upper and lower; Described temperature inductor is all connected with watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of tank body; Upper and lower by the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is double-layer hollow rotating shaft, has shaft seat in the bottom of rotating shaft; Shaft seat is hollow, and shaft seat is provided with fluid inlet; At the bottom of tank, establish drainage pump; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to drainage pump outlet by pipeline; The import of described drainage pump connects in the edge collector with tank base.
2. a kind of complete stirred pot for heparin sodium leaching process according to claim 1, is characterized in that: its inside of described shaft seat is connected with the skin of double-layer hollow rotating shaft, and the center of double-layer hollow rotating shaft is main drive shaft; Main drive shaft, through shaft seat, is connected with the bearing of shaft seat bottom.
3. a kind of complete stirred pot for heparin sodium leaching process according to claim 1, is characterized in that: described sprinkler head is opened in double-layer hollow axle middle and upper part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210537757.5A CN103012622B (en) | 2012-12-13 | 2012-12-13 | Entirely-stirring tank used for heparin sodium extraction process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210537757.5A CN103012622B (en) | 2012-12-13 | 2012-12-13 | Entirely-stirring tank used for heparin sodium extraction process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103012622A CN103012622A (en) | 2013-04-03 |
| CN103012622B true CN103012622B (en) | 2014-08-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210537757.5A Active CN103012622B (en) | 2012-12-13 | 2012-12-13 | Entirely-stirring tank used for heparin sodium extraction process |
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Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107081113B (en) * | 2017-03-24 | 2018-05-01 | 北京长峰金鼎科技有限公司 | Wet mixing pelletizer continuously adds paste-making method and uses its wet mixing pelletizer |
| CN107286271A (en) * | 2017-08-10 | 2017-10-24 | 盐城盛大肠衣食品有限公司 | A kind of resin adsorption extracts liquaemin device |
| CN117619456A (en) * | 2024-01-26 | 2024-03-01 | 祁县凯盛畜产品有限公司 | Resin elution device for preparing heparin sodium crude product and process method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN100467493C (en) * | 2007-02-01 | 2009-03-11 | 高树华 | Producing process for low molecular weight calcium heparin |
| CN101735340B (en) * | 2010-01-18 | 2012-08-22 | 叶青理 | Method for preparing heparin sodium by combining enzymolysis and salt decomposition |
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