CN2505078Y - Chinese medicine separator - Google Patents
Chinese medicine separator Download PDFInfo
- Publication number
- CN2505078Y CN2505078Y CN 01257878 CN01257878U CN2505078Y CN 2505078 Y CN2505078 Y CN 2505078Y CN 01257878 CN01257878 CN 01257878 CN 01257878 U CN01257878 U CN 01257878U CN 2505078 Y CN2505078 Y CN 2505078Y
- Authority
- CN
- China
- Prior art keywords
- explosive barrel
- membrane
- ball valve
- ceramic membrane
- valve
- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a Chinese medicine separator which is characterized in that the extractor is composed of an explosive barrel, a low-pressure pump, a high-pressure pump, a safety colander, a ceramic membrane, a nano membrane, a reverse osmosis film, a ball valve, a pressure regulating valve, a heat exchanger, a pipe and a discharge valve. The physic liquor is filtered by the ceramic membrane and is compressed by the nano film or the reverse osmosis film (water extract uses nano membrane, but alcohol extract uses reverse osmosis membrane). Compared with a traditional heating and concentration method for compressing physic liquor, the Chinese medicine separator has the advantage of low energy consumption, fast compression speed, and small volume of equipment, etc. The phenomenon of boiling paste can not happen, the activity of the medicine can be kept, and the utility model is suitable for the compression of traditional medicine physic liquor.
Description
This utility model relates to seperator, and particularly a kind of Chinese medicine medicine seperator is fit to Chinese medicine and concentrates use.
Traditional Chinese patent medicine system extracting method is that first water or alcohol boil and carries or lixiviate, generally turns over and carries once, and reheat concentrates after filtration then.The shortcoming of this way maximum is through long-time heating, and pharmaceutically active is subjected to bigger destruction, and equipment is huge, and speed is slow, and power consumption is big.If monitor wrongly, be easy to cause and boil the paste phenomenon, influence the quality of Chinese patent medicine.
The purpose of this utility model is to provide that a kind of volume is little, power consumption is low, efficient is high, is not easy to lose the Chinese medicine medicine seperator of pharmaceutically active.
Above-mentioned task realizes by this way with this: this seperator is by the A explosive barrel, the B explosive barrel, low-lift pump, high-pressure pump, security personnel's filter, ceramic membrane, nanometer film, anti-seepage membrane, ball valve, pressure regulator valve, heat exchanger, pipeline and dump valve are formed, the medicine outlet of A explosive barrel and B explosive barrel is respectively with after two ball valves are connected, be connected with the inlet of low-lift pump, the liquid outlet of low-lift pump is connected with the inlet of high-pressure pump, another branch of low-lift pump liquid outlet is connected with the ceramic membrane inlet behind security personnel filter and ball valve, the discharge channel of ceramic membrane is connected with the A explosive barrel, the filtrate outlet is connected with the B explosive barrel behind ball valve, the high-pressure pump liquid outlet is provided with two branches behind security personnel's filter, be connected the back respectively is connected with anti-seepage membrane with nanometer film with two ball valves, its discharge channel all is connected with the A explosive barrel, the outlet of its filtrate is connected with heat exchanger with separately pressure regulator respectively and then is connected with the B explosive barrel, connection between in each group all connects with pipeline, at the A explosive barrel, be equipped with tapping valve on B explosive barrel and the high-pressure pump.
The purpose of this utility model also can take following measure to realize: also be provided with a branch on the pipeline between the ball valve of ceramic membrane front end and the security personnel's filter, this branch exports with the filtrate of ceramic membrane after through a ball valve and is connected.So that back flush.
Be further described below in conjunction with attached affair traffic rules structure of the present utility model.
Fig. 1 is the sketch map of the annexation between each assembly of this utility model.
As shown in Figure 1,1 is the A explosive barrel among the figure, and 2 is the B explosive barrel, the medicine outlet (3 and 4) of two explosive barrels (1 and 2) respectively with ball valve (5 and 6) with pipeline, be connected in parallel after the connection, be connected with the inlet of low-lift pump 8 by pipeline 7, its liquid outlet 8 is rolled the liquid mouth with high-pressure pump 9 and is connected.Another branch at low-lift pump 8 liquid outlets is connected with ceramic membrane 12 behind security personnel's filter 10 ball valves 11.The discharge channel 13 of ceramic membrane 12 is connected with A explosive barrel 1, and its filtrate outlet 14 is connected with the B explosive barrel behind ball valve 15.The liquid outlet 16 of high-pressure pump 9 is divided into two branches behind security personnel's filter 17, be connected the back respectively is connected with anti-seepage membrane 21 with nanometer film 20 with ball valve (18 and 19), its discharge channel 23 all is connected with A explosive barrel 1 with 24, and its filtrate outlet 25 and 26 is connected with 30 with heat exchanger 29 with separately pressure regulator 27 and 28 respectively and then is connected with B explosive barrel 2.On A explosive barrel 1 and B explosive barrel 2 and high-pressure pump 9, be equipped with tapping valve 31,32 and 33, also be provided with a branch on security personnel's filter 10 before ceramic membrane 12 on the linkage section and the pipeline between the ball valve 11, this branch is connected with the filtrate outlet 14 of ceramic membrane 12 behind a ball valve 34.Each assembly all connects with pipeline 35.Ceramic membrane 12 of the present utility model adopts Nanjing University, the product of my high-tech stock company limited for a long time.Nanometer film 20 and anti-seepage membrane 21 then adopt the product of U.S. Dow chemical company (Dow.Chemical Company).Described heat exchanger 29 and 30 is a kind of water-cooled heat exchanger.All the other used assemblies are the product of prior art.
This utility model is to use like this:
1, with macromole and Separation of Proteins: will propose medicinal liquid (lixiviate or boil and carry) earlier and pour in the A explosive barrel 1, then open ball valve 5,11 and 15, start low-lift pump 8 at last, this moment medicinal liquid by ball valve 5 after pipeline 36 flow to low-lift pump 8, behind flow through after low-lift pump 8 pressurizations security personnel's filter 10 and ball valve 11, enter ceramic membrane 12 again, will be through ceramic membrane 12 microfiltration greater than 0.2 microns material is removed the back and is flowed out from filtrate outlet 14, flows to behind ball valve 15 in the B explosive barrel 2.All the other flow back in the A explosive barrel from discharge channel 13.
2, filtered medicine liquid concentrates: close ball valve 5 earlier, open ball valve 6 and ball valve 18 or 19, (the valve 18 if the water extract is kicked off; Valve 19 if alcohol extract is kicked off), then start low-lift pump 8 and high-pressure pump 9.At this moment, flow through ball valve 6, low-lift pump 8 and high-pressure pump 9 through ceramic membrane 12 filtered medicine liquid from B explosive barrel 2, by two pumps medicinal liquid is added to and to flow into security personnel's filter 17 behind the high pressure, flow into nanometer film 20 or anti-seepage membrane 21 through ball valve 18 or 19 again, medicinal liquid after concentrating flows out from filtrate ( liquid 25 or 26, again through pressure regulator valve 27 or 28 and heat exchanger 29 or 30 coolings after flow in the B explosive barrel 2; And moisture content that is separated or alcohol flow in the A explosive barrel 1 from discharge channel 23 or 24, thereby medicinal liquid is concentrated.By regulating the open degree of pressure regulator valve 27 or 28, can change pressure reduction, the quickening separating rate of film both sides.When the operation long more its concentration ratio of time big more.
When 3, needing to clean film:
(1) situation of ceramic membrane
Square impact: clear water is added in the A explosive barrel 1, open ball valve 5,11 and 15, and corresponding dump valve 31 opened and start low-lift pump 8 get final product, clear water is pressed forward and is washed.
Recoil: close ball valve 11 and 15, open ball valve 34, again dump valve 31 is opened and started low-lift pump 8 and get final product.
(2) situation of nanometer film 20 and anti-seepage membrane 21: clear water is added in the B explosive barrel 2, just can by concentrating the running route flushing.
From structure of the present utility model and operation principle as can be known, the utility model is to use micro-filtration Film comes concentrated medicament, with existing by heat concentrated method compare have power consumption low, Fast, the easily monitoring of the speed of concentrating can not produce and boil the paste phenomenon, can keep pharmaceutically active And the advantage such as equipment volume is little, be fit to soup and concentrate and use.
Claims (2)
1, a kind of Chinese medicine medicine seperator, it is characterized in that this seperator is by A explosive barrel (1), B explosive barrel (2), low-lift pump (8), high-pressure pump (9), security personnel's filter (10,17), ceramic membrane (12), nanometer film (20), anti-seepage membrane (21), ball valve (5,6,11,18,19,34), pressure regulator valve (27,28), heat exchanger (29,30), pipeline (36) and dump valve (31,32,33) form, the medicine outlet (3 of A explosive barrel (1) and B explosive barrel (2), 4) respectively with two ball valves (5,6) connecting the back is connected with the inlet of low-lift pump (8), the liquid outlet (7) of low-lift pump (8) is connected with the inlet of high-pressure pump (9), another branch of low-lift pump (8) liquid outlet (7) through security personnel filters (10) with ball valve (11) after be connected with ceramic membrane (12) inlet, the discharge channel (13) of ceramic membrane (12) is connected with A explosive barrel (1), filtrate outlet (14) is connected with B explosive barrel (2) behind ball valve (15), high-pressure pump (9) liquid outlet (16) is provided with two branches behind security personnel's filters (17), with two ball valves (18,19) connecting the back is connected with anti-seepage membrane (21) with nanometer film (20), its discharge channel (23,24) all be connected with A explosive barrel (1), its concentrated solution outlet (25,26) respectively with separately pressure regulator (27,28) and heat exchanger (29,30) connecting the back is connected with B explosive barrel (2), connection between in each group all uses pipeline (36) to connect, in A explosive barrel (1), be equipped with tapping valve (31 on B explosive barrel (2) and the high-pressure pump (9), 32,33).
2, medicine seperator according to claim 1, it is characterized in that also being provided with a branch on the pipeline between the ball valve (11) of ceramic membrane (12) front end and the security personnel's filters (10), this branch is connected with the filter liquid outlet (14) of ceramic membrane (12) afterwards through a ball valve (34).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01257878 CN2505078Y (en) | 2001-11-08 | 2001-11-08 | Chinese medicine separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01257878 CN2505078Y (en) | 2001-11-08 | 2001-11-08 | Chinese medicine separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2505078Y true CN2505078Y (en) | 2002-08-14 |
Family
ID=33666556
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01257878 Expired - Fee Related CN2505078Y (en) | 2001-11-08 | 2001-11-08 | Chinese medicine separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2505078Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100355766C (en) * | 2005-10-21 | 2007-12-19 | 安徽农业大学 | Method for preparing and purifying uperarin through membrane technology |
-
2001
- 2001-11-08 CN CN 01257878 patent/CN2505078Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100355766C (en) * | 2005-10-21 | 2007-12-19 | 安徽农业大学 | Method for preparing and purifying uperarin through membrane technology |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20020814 Termination date: 20091208 |