CN204582602U - Circulation extraction concentration in oral liquid process process - Google Patents
Circulation extraction concentration in oral liquid process process Download PDFInfo
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- CN204582602U CN204582602U CN201520040087.5U CN201520040087U CN204582602U CN 204582602 U CN204582602 U CN 204582602U CN 201520040087 U CN201520040087 U CN 201520040087U CN 204582602 U CN204582602 U CN 204582602U
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Abstract
Circulation extraction concentration in oral liquid process process, comprising: extractor, froth breaker, extractor condenser, extractor cooler, concentrated cooler, concentrated condenser, evaporation material liquid tank, concentration evaporator, concentration heater, nuclepore membrane filter, filter, reflux cycle pipe; Advantage of the present utility model: receive cream rate than multi-function extractor height 10-15%, high more than 1 times containing active ingredient, medicine active constituent content is high; Leaching velocity is fast, and leaching cycle is short, and utilization rate of equipment and installations is high; Solvent load fewer than multi-function extractor more than 30%, consumption rate can reduce 50-70%; Equipment takes up an area little, and economize energy and solvent, small investment, cost is low.
Description
Technical field
The utility model relates to the circulation extraction concentration in oral liquid process process, belongs to field of pharmaceutical equipment.
Background technology
Extractor recovery rate in existing oral liquor medicine production process is not high, and active constituent content is few, and the cycle is long, and production cost is higher, and medicine active constituent content is low.
Summary of the invention
The purpose of this utility model is to provide the circulation extraction concentration in oral liquid process process, extractor sidewall adds reflux cycle pipe, improve extraction efficiency, a nuclepore membrane filter has been increased newly after filter, improve the active ingredient of leachate, make the medicine active constituent content of preparation high.
The purpose of this utility model is achieved in that
Circulation extraction concentration in oral liquid process process, comprising: extractor, froth breaker, extractor condenser, extractor cooler, concentrated cooler, concentrated condenser, evaporation material liquid tank, concentration evaporator, concentration heater, nuclepore membrane filter, filter, reflux cycle pipe, extractor top is provided with froth breaker, froth breaker top is connected with extractor condenser overhead by pipeline, be connected with extractor cooler top by pipeline bottom extractor condenser, be connected with froth breaker top by pipeline bottom extractor cooler, froth breaker sidewall is connected with concentration evaporator and nuclepore membrane filter respectively by pipeline, concentration evaporator top is provided with concentrated cooler, concentrated cooler is connected with concentrated condenser, concentrated condenser is connected with evaporation material liquid tank, be connected with concentration heater by pipeline bottom concentration evaporator, be connected with filter and nuclepore membrane filter successively by pipeline bottom extractor, extractor sidewall is provided with reflux cycle pipe.
Operation principle of the present utility model: medicine is placed in extractor and extracts, extract while carry out circulating reflux with reflux cycle pipe, after extracting, leachate enters concentration evaporator by filter and nuclepore membrane filter, opening concentration heater makes leachate concentrate, the concentrated steam part produced enters extractor and seethes with excitement as in thermal source maintenance tank, and a part falls back in extractor as new solvent through extractor condenser and extractor cooler.
Circulation extraction concentration of the present utility model may be used for Compound pholcodine, SangCya, the production process of the oral liquids such as the pseudo-numb hydrocodone oral administration solution of phenol of healing.
Advantage of the present utility model:
1, receive cream rate than multi-function extractor height 10-15%, high more than 1 times containing active ingredient, medicine active constituent content is high.
2, leaching velocity is fast, and leaching cycle is short, and utilization rate of equipment and installations is high.
3, solvent load fewer than multi-function extractor more than 30%, consumption rate can reduce 50-70%.
4, equipment takes up an area little, and economize energy and solvent, small investment, cost is low.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Reference numeral: extractor 1, froth breaker 2, extractor condenser 3, extractor cooler 4, concentrated cooler 5, concentrated condenser 6, evaporation material liquid tank 7, concentration evaporator 8, concentration heater 9, nuclepore membrane filter 10, filter 11, reflux cycle pipe 12.
Detailed description of the invention
Contrast accompanying drawing be described in further detail this reality is novel below in conjunction with embodiment.
Embodiment 1:
Circulation extraction concentration in oral liquid process process, comprising: extractor 1, froth breaker 2, extractor condenser 3, extractor cooler 4, concentrated cooler 5, concentrated condenser 6, evaporation material liquid tank 7, concentration evaporator 8, concentration heater 9, nuclepore membrane filter 10, filter 11, reflux cycle pipe 12, extractor 1 top is provided with froth breaker 2, froth breaker 2 top is connected with extractor condenser 3 top by pipeline, be connected with extractor cooler 4 top by pipeline bottom extractor condenser 3, be connected with froth breaker 2 top by pipeline bottom extractor cooler 4, froth breaker 2 sidewall is connected with concentration evaporator 8 and nuclepore membrane filter 10 respectively by pipeline, concentration evaporator 8 top is provided with concentrated cooler 5, concentrated cooler 5 is connected with concentrated condenser 6, concentrated condenser 6 is connected with evaporation material liquid tank 7, be connected with concentration heater 9 by pipeline bottom concentration evaporator 8, be connected with filter 11 and nuclepore membrane filter 10 successively by pipeline bottom extractor 1, extractor 1 sidewall is provided with reflux cycle pipe 12.
Embodiment 2:
The operation principle of the circulation extraction concentration in oral liquid process process: medicine is placed in extractor 1 and extracts, extract while carry out circulating reflux with reflux cycle pipe 12, after extracting, leachate enters concentration evaporator 8 by filter 11 and nuclepore membrane filter 10, opening concentration heater 9 makes leachate concentrate, the concentrated steam part produced enters extractor 1 and seethes with excitement as in thermal source maintenance tank, and a part falls back in extractor 1 as new solvent through extractor condenser 3 and extractor cooler 4.
All the other are with embodiment 1.
Embodiment 3:
Circulation extraction concentration in oral liquid process process, may be used for Compound pholcodine, SangCya, the production process of the oral liquids such as the pseudo-numb hydrocodone oral administration solution of phenol of healing.
All the other are with embodiment 1.
Claims (1)
1. the circulation extraction concentration in oral liquid process process, is characterized in that: comprising: extractor (1), froth breaker (2), extractor condenser (3), extractor cooler (4), concentrated cooler (5), concentrated condenser (6), evaporation material liquid tank (7), concentration evaporator (8), concentration heater (9), nuclepore membrane filter (10), filter (11), reflux cycle pipe (12), extractor (1) top is provided with froth breaker (2), froth breaker (2) top is connected with extractor condenser (3) top by pipeline, extractor condenser (3) bottom is connected with extractor cooler (4) top by pipeline, extractor cooler (4) bottom is connected with froth breaker (2) top by pipeline, froth breaker (2) sidewall is connected with concentration evaporator (8) and nuclepore membrane filter (10) respectively by pipeline, concentration evaporator (8) top is provided with concentrated cooler (5), concentrated cooler (5) is connected with concentrated condenser (6), concentrated condenser (6) is connected with evaporation material liquid tank (7), concentration evaporator (8) bottom is connected with concentration heater (9) by pipeline, extractor (1) bottom is connected with filter (11) and nuclepore membrane filter (10) successively by pipeline, extractor (1) sidewall is provided with reflux cycle pipe (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520040087.5U CN204582602U (en) | 2015-01-21 | 2015-01-21 | Circulation extraction concentration in oral liquid process process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520040087.5U CN204582602U (en) | 2015-01-21 | 2015-01-21 | Circulation extraction concentration in oral liquid process process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204582602U true CN204582602U (en) | 2015-08-26 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520040087.5U Expired - Fee Related CN204582602U (en) | 2015-01-21 | 2015-01-21 | Circulation extraction concentration in oral liquid process process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204582602U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105125406A (en) * | 2015-09-08 | 2015-12-09 | 培力(南宁)药业有限公司 | Efficient dynamic drug-decocting machine |
-
2015
- 2015-01-21 CN CN201520040087.5U patent/CN204582602U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105125406A (en) * | 2015-09-08 | 2015-12-09 | 培力(南宁)药业有限公司 | Efficient dynamic drug-decocting machine |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150826 Termination date: 20210121 |