CN203613131U - Heparin sodium production device - Google Patents
Heparin sodium production device Download PDFInfo
- Publication number
- CN203613131U CN203613131U CN201320667274.7U CN201320667274U CN203613131U CN 203613131 U CN203613131 U CN 203613131U CN 201320667274 U CN201320667274 U CN 201320667274U CN 203613131 U CN203613131 U CN 203613131U
- Authority
- CN
- China
- Prior art keywords
- tank
- absorption
- retort
- wash
- heparin sodium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 229920000669 heparin Polymers 0.000 title claims abstract description 16
- ZFGMDIBRIDKWMY-PASTXAENSA-N heparin Chemical compound CC(O)=N[C@@H]1[C@@H](O)[C@H](O)[C@@H](COS(O)(=O)=O)O[C@@H]1O[C@@H]1[C@@H](C(O)=O)O[C@@H](O[C@H]2[C@@H]([C@@H](OS(O)(=O)=O)[C@@H](O[C@@H]3[C@@H](OC(O)[C@H](OS(O)(=O)=O)[C@H]3O)C(O)=O)O[C@@H]2O)CS(O)(=O)=O)[C@H](O)[C@H]1O ZFGMDIBRIDKWMY-PASTXAENSA-N 0.000 title claims abstract description 16
- 229960001008 heparin sodium Drugs 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 238000010521 absorption reaction Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000003756 stirring Methods 0.000 claims abstract description 11
- 239000012267 brine Substances 0.000 claims description 12
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 239000012266 salt solution Substances 0.000 claims description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract 4
- 238000010828 elution Methods 0.000 abstract 4
- 239000011780 sodium chloride Substances 0.000 abstract 4
- 238000006243 chemical reaction Methods 0.000 abstract 2
- 238000004062 sedimentation Methods 0.000 abstract 2
- 238000004064 recycling Methods 0.000 abstract 1
- 229920002683 Glycosaminoglycan Polymers 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000003146 anticoagulant agent Substances 0.000 description 1
- 229940127219 anticoagulant drug Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 210000004347 intestinal mucosa Anatomy 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- -1 sulfuric acid ester Chemical class 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a heparin sodium production device. The device is characterized by comprising a reaction tank, an absorption and elution tank and a sedimentation tank which are arranged from top to bottom sequentially, wherein the absorption and elution tank is connected with the sedimentation tank through a pipeline, and an on-off valve is arranged on the pipeline; a stirring paddle, temperature sensors, a pressure inductor, a PH value detector, a concentration inductor, an automatic liquid level detector and a proportion inductor are arranged in the reaction tank; and a clear water inlet and a saline water outlet are formed in the absorption and elution tank, the clear water inlet is connected with a clear water pipe, the saline water outlet is connected with a saline water pipe which is put into a saline water recycling tank, and the stirring paddle is arranged in the absorption and elution tank. The heparin sodium production device is simple and compact in structure, small in occupied area, more accurate in operation and high in product yield.
Description
Technical field
The utility model relates to a kind of extraction element of heparin sodium, is specifically related to a kind of high yield, the production equipment of easy-operating heparin sodium.
Background technology
Heparin sodium is mucopolysaccharide sulfuric acid ester anticoagulant.Heparin sodium is the sodium salt of the CSSO3 extracted in the intestinal mucosa by pig or ox, belongs to mucopolysaccharide material.Recent study proves that heparin sodium also has reducing blood lipid.At present, in heparin sodium production process, after raw material react in retort, pass through naturally cooling, the feed liquid in retort is pumped into adsorption tanks with pump; Equally, between other tank body, the conveying of feed liquid all needs to pump with pump, and therefore, existing equipment has following shortcoming: 1, between tank body, the conveying of feed liquid all needs to pump with pump, has caused the waste of the energy; 2, tank body is installed in same level, and tank body is more, and it is larger that it takies plant area; 3, adopt manual operation, production efficiency is low, and monitor data is inaccurate, causes the problems such as output capacity is low.
Summary of the invention
The purpose of this utility model is for deficiency of the prior art, provides a kind of and can effectively improve product quality and production efficiency, the heparin sodium production equipment of save energy and manufacturer's floor space.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of production equipment of heparin sodium, its innovative point is: comprise retort, absorption and wash-out tank and setting tank, described retort, absorption and wash-out tank, setting tank are disposed in order from top to bottom, between retort, absorption and wash-out tank and setting tank, be connected by pipeline, on pipeline, be provided with opening/shutting valve;
Described retort connects material source, in described retort, be provided with stirring rake, temperature sensor, pressure inductor, pH value detector, concentration inductor block, automatic liquid level detector and proportioning inductor block, retort arranged outside controller, temperature, pressure, pH value, concentration, liquid level and proportioning are by controller control, and retort lower end arranges and is adsorbed in wash-out tank;
On described absorption and wash-out tank, clear water import and brine outlet are set, clear water import connects clear water pipe, and brine outlet connects brine tube, and brine tube passes into salt solution pond for recovering, in absorption and wash-out tank, stirring rake is set;
In described setting tank, be provided with stirring rake.
Further, on described retort, absorption and wash-out tank and setting tank, be provided with viewing window.
The beneficial effects of the utility model: heparin sodium production equipment of the present utility model, between tank body, rely on the action of gravity of self to complete, between tank body, adopt mode from top to bottom to arrange, save floor space; In retort, be provided with temperature sensor, pressure inductor, pH value detector, concentration inductor block, automatic liquid level detector and proportioning inductor block, control by controller, operate more accurately, the yield of product is higher.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the schematic internal view of retort of the present utility model.
Embodiment
Below in conjunction with the drawings and specific embodiments, the technical solution of the utility model is elaborated.
The production equipment of a kind of heparin sodium as shown in Figure 1, comprise retort 1, absorption and wash-out tank 2 and setting tank 3, described retort 1, absorption and wash-out tank 2, setting tank 3 are disposed in order from top to bottom, between retort 1, absorption and wash-out tank 2 and setting tank 3, be connected by pipeline 4, on pipeline 4, be provided with opening/shutting valve 5; Retort 1 connects material source, in retort 1, be provided with stirring rake 11, temperature sensor 12, pressure inductor 13, pH value detector 14, concentration inductor block 15, automatic liquid level detector 16 and proportioning inductor block 17, retort 1 arranged outside controller 18, temperature, pressure, pH value, concentration, liquid level and proportioning are controlled by controller 18, and retort 1 lower end arranges absorption and wash-out tank 2; On absorption and wash-out tank 2, clear water import 21 and brine outlet 22 are set, clear water import 21 connects clear water pipe 23, and brine outlet 22 connects brine tube 24, and brine tube 24 passes into salt solution pond for recovering, absorption and the interior stirring rake 25 that arranges of wash-out tank 2; On described retort 1, absorption and wash-out tank 2 and setting tank 3, be provided with viewing window 6; In described setting tank 3, be provided with stirring rake 31.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (2)
1. the production equipment of a heparin sodium, it is characterized in that: comprise retort, absorption and wash-out tank and setting tank, described retort, absorption and wash-out tank, setting tank are disposed in order from top to bottom, between retort, absorption and wash-out tank and setting tank, be connected by pipeline, on pipeline, be provided with opening/shutting valve;
Described retort connects material source, in retort, be provided with stirring rake, temperature sensor, pressure inductor, pH value detector, concentration inductor block, automatic liquid level detector and proportioning inductor block, retort arranged outside controller, temperature, pressure, pH value, concentration, liquid level and proportioning are by controller control, and retort lower end arranges absorption and wash-out tank;
On described absorption and wash-out tank, clear water import and brine outlet are set, clear water import connects clear water pipe, and brine outlet connects brine tube, and brine tube passes into salt solution pond for recovering, in absorption and wash-out tank, stirring rake is set;
In described setting tank, be provided with stirring rake.
2. the production equipment of a kind of heparin sodium according to claim 1, is characterized in that: on described retort, absorption and wash-out tank and setting tank, be provided with viewing window.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320667274.7U CN203613131U (en) | 2013-10-28 | 2013-10-28 | Heparin sodium production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320667274.7U CN203613131U (en) | 2013-10-28 | 2013-10-28 | Heparin sodium production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203613131U true CN203613131U (en) | 2014-05-28 |
Family
ID=50765788
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320667274.7U Expired - Fee Related CN203613131U (en) | 2013-10-28 | 2013-10-28 | Heparin sodium production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203613131U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324530A (en) * | 2014-10-27 | 2015-02-04 | 南通天龙畜产品有限公司 | Waste alcohol sediment separation device for sausage casing residues |
| CN117504436A (en) * | 2024-01-08 | 2024-02-06 | 扬州金丽生物科技有限公司 | Heparin sodium precipitation filtration tank |
-
2013
- 2013-10-28 CN CN201320667274.7U patent/CN203613131U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324530A (en) * | 2014-10-27 | 2015-02-04 | 南通天龙畜产品有限公司 | Waste alcohol sediment separation device for sausage casing residues |
| CN104324530B (en) * | 2014-10-27 | 2016-08-03 | 南通天龙畜产品有限公司 | Waste alcohol precipitation separation device in casing slag |
| CN117504436A (en) * | 2024-01-08 | 2024-02-06 | 扬州金丽生物科技有限公司 | Heparin sodium precipitation filtration tank |
| CN117504436B (en) * | 2024-01-08 | 2024-04-26 | 扬州金丽生物科技有限公司 | Heparin sodium precipitation filtration tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140528 |