CN103012622A - 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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- CN103012622A CN103012622A CN2012105377575A CN201210537757A CN103012622A CN 103012622 A CN103012622 A CN 103012622A CN 2012105377575 A CN2012105377575 A CN 2012105377575A CN 201210537757 A CN201210537757 A CN 201210537757A CN 103012622 A CN103012622 A CN 103012622A
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- tank body
- rotating shaft
- 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 that uses for the heparin sodium leaching process.
Background technology
Heparin sodium is to extract in the logical large intestine small intestine and obtain, generally, from decomposing, to collecting most the used time quite long, its process very complex is with regard to present circumstances, general reaction once, take several days time, and its output capacity is quite low, what this was central mainly just relates to the problem of a tank body, certain main relating to, the problem that stirs, because stirring body is the material in the intestines, its speed can not be too fast, to guarantee also that simultaneously the added ingredients that adds is quite even, only in this way could shorten the time, another side is 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 that stirs, react insufficient; This is when advancing also to have comprised non-uniform temperature, and whether entering of additive contacts with whole materials at short notice, and the quick response problem.
Summary of the invention
Problem to be solved by this invention provides a kind of complete stirred pot for the heparin sodium leaching process, and it can guaranteeing well-beaten reaction times shortening three to four hours that allow simultaneously of material, allow output capacity be higher than traditional tank body reaction.
For finishing the foregoing invention purpose, the present invention is achieved in that a kind of complete stirred pot for the heparin sodium leaching process, and its main body is a tank body, is provided with agitator in tank body, the inwall middle portion is provided with temperature inductor; Liquid level meter all is equipped with in the upper and lower; Described temperature inductor all is connected with the watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of the tank body; About the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at the tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is the double-layer hollow rotating shaft, in the bottom of rotating shaft shaft seat is arranged; Shaft seat is hollow, and shaft seat is provided with the high pressure fluid inlet; Establish High Voltage drainage pump at the bottom of the tank; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to the outlet of High Voltage pump priming by pipeline; The import of described High Voltage drainage pump connects in the edge collector with tank base.This patent adopts the high-voltage bidirectional drainage, allows the interior material of tank thoroughly roll, and does not have the dead point, sediment-free.
Technique scheme is done further to improve, and described edge collector invests wall at the bottom of tank, is cavity-like, and certain height is arranged; Its one is connected to the entrance of High Voltage drainage pump by pipeline, the 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 be heated or react, need again to introduce by after collecting, 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 with a Chen Ji recovery mouthful position that is staggered; Sufficient movement in the cavity can be allowed like this, and the many places whirling current can be in tank, formed, thus the increase mixing effect.
Technique scheme is done further to improve, be provided with a pipeline opening in the tank body outside, be connected with bottom High Voltage drainage pump; Its pipeline is provided with valve.In the prior art, in reaction process, need adding auxiliary material or buck, all is artificial adding, this disposable pouring into, the then stirring by nature.And the interpolation of the manner is more all even, and reactivity is higher.
Technique scheme is done further to improve, 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 passes 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.
Description of drawings
Fig. 1 is structural representation of the present invention.
Embodiment
As shown in the figure, a kind of complete stirred pot for the heparin sodium leaching process, its main body is a tank body, is provided with agitator in tank body, the inwall middle portion is provided with temperature inductor; Liquid level meter all is equipped with in the upper and lower; Described temperature inductor all is connected with the watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of the tank body; About the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at the tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is the double-layer hollow rotating shaft, in the bottom of rotating shaft shaft seat is arranged; Shaft seat is hollow, and shaft seat is provided with the high pressure fluid inlet; Establish High Voltage drainage pump at the bottom of the tank; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to the outlet of High Voltage pump priming by pipeline; The import of described High Voltage drainage pump connects in the edge collector with tank base.This patent adopts the high-voltage bidirectional drainage, allows the interior material of tank thoroughly roll, and does not have the dead point, sediment-free.
Described edge collector invests wall at the bottom of tank, is cavity-like, and certain height is arranged; Its one is connected to the entrance of High Voltage drainage pump by pipeline, the 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 be heated or react, need again to introduce by after collecting, 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 with a Chen Ji recovery mouthful position that is staggered; Sufficient movement in the cavity can be allowed like this, and the many places whirling current can be in tank, formed, thus the increase mixing effect.
Be provided with a pipeline opening in the tank body outside, be connected with bottom High Voltage drainage pump; Its pipeline is provided with valve.In the prior art, in reaction process, need adding auxiliary material or buck, all is artificial adding, this disposable pouring into, the then stirring by nature.And the interpolation of the manner is more all even, and reactivity is higher.
Technique scheme is done further to improve, 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 passes 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 (5)
1. complete stirred pot that is used for the heparin sodium leaching process, its main body is a tank body, is provided with agitator in tank body, the inwall middle portion is provided with temperature inductor; Liquid level meter all is equipped with in the upper and lower; Described temperature inductor all is connected with the watch-keeping cubicle by line with liquid level meter; Described agitator stands in the middle of the tank body; About the straight-through tank body of a rotating shaft, which is provided with stirrer gear; Agitator comprises a motor, and motor is positioned at the tank body top; Be connected with rotating shaft by speed reduction unit; It is characterized in that: described rotating shaft is the double-layer hollow rotating shaft, in the bottom of rotating shaft shaft seat is arranged; Shaft seat is hollow, and shaft seat is provided with the high pressure fluid inlet; Establish High Voltage drainage pump at the bottom of the tank; Described its skin of double-layer hollow rotating shaft is provided with sprinkler head, and each sprinkler head is connected to the outlet of High Voltage pump priming by pipeline; The import of described High Voltage drainage pump connects in the edge collector with tank base.
2. a kind of complete stirred pot for the heparin sodium leaching process according to claim 2, it is characterized in that: described edge collector invests wall at the bottom of tank, is cavity-like, and certain height is arranged; Its one is connected to the entrance of High Voltage drainage pump by pipeline, the collector top has some Chen Ji to reclaim mouth.
3. a kind of complete stirred pot for the heparin sodium leaching process according to claim 2 is characterized in that: be provided with a pipeline opening in the tank body outside, be connected with bottom High Voltage drainage pump; Its pipeline is provided with valve.
4. a kind of complete stirred pot for the heparin sodium leaching process according to claim 1 is characterized in that: it innerly is connected described shaft seat 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 passes shaft seat, is connected with the bearing of shaft seat bottom.
5. a kind of complete stirred pot for the heparin sodium leaching process according to claim 1, it 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 true CN103012622A (en) | 2013-04-03 |
| CN103012622B 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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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107081113A (en) * | 2017-03-24 | 2017-08-22 | 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 |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101012289A (en) * | 2007-02-01 | 2007-08-08 | 高树华 | Producing process for low molecular weight calcium heparin |
| CN101735340A (en) * | 2010-01-18 | 2010-06-16 | 叶青理 | Method for preparing heparin sodium by combining enzymolysis and salt decomposition |
-
2012
- 2012-12-13 CN CN201210537757.5A patent/CN103012622B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101012289A (en) * | 2007-02-01 | 2007-08-08 | 高树华 | Producing process for low molecular weight calcium heparin |
| CN101735340A (en) * | 2010-01-18 | 2010-06-16 | 叶青理 | Method for preparing heparin sodium by combining enzymolysis and salt decomposition |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107081113A (en) * | 2017-03-24 | 2017-08-22 | 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103012622B (en) | 2014-08-27 |
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