CN203971767U - Traditional Chinese medicine injection production ultrafiltration system - Google Patents
Traditional Chinese medicine injection production ultrafiltration system Download PDFInfo
- Publication number
- CN203971767U CN203971767U CN201420412891.7U CN201420412891U CN203971767U CN 203971767 U CN203971767 U CN 203971767U CN 201420412891 U CN201420412891 U CN 201420412891U CN 203971767 U CN203971767 U CN 203971767U
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- China
- Prior art keywords
- stoste
- ultrafilter
- valve
- delivery port
- pipeline
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- Expired - Fee Related
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- 239000003814 drug Substances 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 238000002347 injection Methods 0.000 title claims abstract description 15
- 239000007924 injection Substances 0.000 title claims abstract description 15
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 15
- 239000012535 impurity Substances 0.000 claims abstract description 28
- 238000004140 cleaning Methods 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 238000011084 recovery Methods 0.000 claims description 6
- 230000000740 bleeding effect Effects 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 239000000706 filtrate Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000003749 cleanliness Effects 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of traditional Chinese medicine injection production ultrafiltration system, comprise stoste circulating tank, multistage pump, ultrafilter group, impurities removal pipeline, see through liquid pipeline and frequency-variable controller, between ultrafilter group top delivery port and stoste circulating tank top, cleaning blow-off pipe is set, cleans blow-off pipe end and connect impurities removal pipeline; Frequency-variable controller connects and controls multistage pump.The utility model can not only carry out good removal of impurities to impurity remaining in ultrafilter, can also carry out to milipore filter the cleaning of works very well; The a large amount of stoste wastes that can avoid frequent clean to bring, have reduced production cost admirably, have improved utilization rate of active components; The utility model works very well simple in structure, is particularly suitable for traditional Chinese medicine injection production and application.
Description
Technical field
The utility model relates to pharmaceuticals industry filtration art, more particularly, relates in particular to a kind of traditional Chinese medicine injection production ultrafiltration system.
Background technology
Membrane separation technique is the separation technology emerging rapidly after the nineties in 20th century, be from the different of traditional filtering, the ultrafiltration apparatus that membrane separation technique is produced can carry out separation in molecular range, and this process is a kind of physical process, do not need the variation of phase occurs and add auxiliary agent, be widely used in the separation of the industries such as medicine, food, biology, environmental protection, concentrated and purifying.
The ultrafiltration system of producing for traditional Chinese medicine injection is after producing after a while, need to clean the milipore filter in ultrafilter and remove filtering rear remaining impurity (particulate, colloid, thermal source and various organic matter), in prior art, clean and all thorough and affect filtrate pipeline cleanliness factor during removal of impurities; In addition, because the drug molecule amount of producing is all less, cleaning need be comparatively frequent, causes a large amount of stoste wastes, has a strong impact on production cost.
Utility model content
The purpose of this utility model is for above-mentioned the deficiencies in the prior art, provides a kind of cleaning and removal of impurities thoroughly, not to affect filtrate pipeline cleanliness factor and can not cause a large amount of traditional Chinese medicine injection production ultrafiltration systems of wasting of stoste.
The technical solution of the utility model is achieved in that a kind of traditional Chinese medicine injection production ultrafiltration system, comprise stoste circulating tank, multistage pump, ultrafilter group, impurities removal pipeline, see through liquid pipeline and frequency-variable controller, described stoste circulating tank bottom delivery port connects multistage pump water inlet end, described multistage pump water side connects ultrafilter group bottom water inlet and impurities removal pipeline successively, described ultrafilter group bottom delivery port connects through liquid pipeline, and top delivery port connects stoste circulating tank top; Between described ultrafilter group top delivery port and stoste circulating tank top, cleaning blow-off pipe is set, described cleaning blow-off pipe end connects impurities removal pipeline; Described frequency-variable controller connects and controls multistage pump.
As to further improvement of the utility model, described ultrafilter group is comprised of at least two ultrafilters, and all ultrafilters bottom water inlet, delivery port and top delivery port are all in parallel, described bottom water inlet place in parallel and top delivery port place in parallel are equipped with Pressure gauge; The in parallel blast pipe that also has center of top, the end after described blast pipe parallel connection is provided with air bleeding valve.
As to further improvement of the utility model, the bottom delivery port of described ultrafilter group and seeing through between liquid pipeline is provided with through liquid valve, between bottom water inlet and impurities removal pipeline, is provided with eduction valve, is provided with feed liquor butterfly valve between bottom water inlet and multistage pump; Pipeline between described feed liquor butterfly valve and multistage pump adopts pipeline to be connected with cleaning blow-off pipe middle part, and between be provided with recovery valve.
As to further improvement of the utility model, described cleaning blow-off pipe beginning and end arrange respectively into dirty valve and blowoff valve, between described cleaning blow-off pipe beginning and stoste circulating tank, are provided with diaphragm valve.
As to further improvement of the utility model, described stoste circulating tank can body outside is provided with fluid level controller.
The utility model adopts after said structure, can not only carry out good removal of impurities to remaining impurity in ultrafilter after use a period of time, can also carry out to the milipore filter in ultrafilter the cleaning of works very well; In addition, a large amount of stoste wastes that can also avoid frequent clean to bring, have reduced production cost admirably, have improved utilization rate of active components; The utility model works very well simple in structure, is particularly suitable for traditional Chinese medicine injection production and application.
Accompanying drawing explanation
Below in conjunction with the embodiment in accompanying drawing, the utility model is described in further detail, but do not form any restriction of the present utility model.
Fig. 1 is structural representation of the present utility model.
In figure: 1-stoste circulating tank; 2-multistage pump; 3-ultrafilter group; 4-impurities removal pipeline; 5-sees through liquid pipeline; 6-frequency-variable controller; 7-cleans blow-off pipe; 8-Pressure gauge; 9-air bleeding valve; 10-feed liquor butterfly valve; 11-eduction valve; 12-recovery valve; 13-enters dirty valve; 14-blowoff valve; 15-diaphragm valve; 16-fluid level controller; 17-sees through liquid valve.
The specific embodiment
Consult shown in Fig. 1, traditional Chinese medicine injection production ultrafiltration system of the present utility model, comprise stoste circulating tank 1, multistage pump 2, ultrafilter group 3, impurities removal pipeline 4, see through liquid pipeline 5 and frequency-variable controller 6, described stoste circulating tank 1 bottom delivery port connects multistage pump 2 water inlet ends, described multistage pump 2 water sides connect ultrafilter group 3 bottom water inlets and impurities removal pipeline successively, described ultrafilter group 3 bottom delivery ports connect through liquid pipeline 5, and top delivery port connects stoste circulating tank 1 top; Between described ultrafilter group 3 top delivery ports and stoste circulating tank 1 top, arrange and clean blow-off pipe 7, described cleaning blow-off pipe 7 ends connect impurities removal pipeline 4; Described frequency-variable controller 6 connects and controls multistage pump 2.
In the utility model, described ultrafilter group 3 is comprised of at least two ultrafilters, and all ultrafilters bottom water inlet, delivery port and top delivery port are all in parallel, and described bottom water inlet place in parallel and top delivery port place in parallel are equipped with Pressure gauge 8; The in parallel blast pipe that also has center of top, the end after described blast pipe parallel connection is provided with air bleeding valve 9.
In the utility model, the bottom delivery port of described ultrafilter group 3 and seeing through between liquid pipeline 5 is provided with through liquid valve 17, between bottom water inlet and impurities removal pipeline, is provided with eduction valve 11, between bottom water inlet and multistage pump 2, is provided with feed liquor butterfly valve 10; Pipeline between described feed liquor butterfly valve 10 and multistage pump 2 adopts pipelines to be connected with cleaning blow-off pipe 7 middle parts, and between be provided with recovery valve 12.
In the utility model, described 7 beginnings of cleaning blow-off pipe and end arrange respectively into dirty valve 13 and blowoff valve 14, between described 7 beginnings of cleaning blow-off pipe and stoste circulating tank 1, are provided with diaphragm valve 15.
In the utility model, described stoste circulating tank 1 can body outside is provided with fluid level controller 16.
When the utility model is implemented, stoste flows to multistage pump 2 from stoste circulating tank 1 bottom delivery port, and under frequency-variable controller 6 is controlled, multistage pump 2 presses to rear method, apparatus by stoste according to required flow rate.Open feed liquor butterfly valve 10 and see through liquid valve 17, close all the other valves, stoste enters ultrafilter group 3 and carries out ultrafiltration, and active drug is because passing through milipore filter in the aperture that its molecular weight is less than milipore filter, now, filtrate can be by seeing through liquid valve 17 and entering through liquid pipeline 5 under the effect of pressure.
When system needs removal of impurities, open eduction valve 11, recovery valve 12 and enter dirty valve 13, close all the other valves, utilize 7 pairs of ultrafilter groups 3 of cleaning blow-off pipe to recoil, most of impurity is between bottom water inlet and milipore filter, so under the effect of pressure, most of impurity enters impurities removal pipeline 4 by eduction valve 11.The stoste that removal of impurities process slatterns seldom, in prior art, waste stoste a lot of be the process of cleaning milipore filter.Use on the milipore filter after a period of time and have more impurity, need to open feed liquor butterfly valve 10, diaphragm valve 15, enter dirty valve 13 and recovery valve 12, close other valves, add the scavenger specially that cannot see through diaphragm valve 15, the power amplification of multistage pump 2 is arrived to desired value, utilize the liquid itself existing in system to rinse for a long time, can in this process, all be recycled in stoste circulating tank 1 by the active ingredient of diaphragm valve 15.Rinse after a period of time, then will open blowoff valve 14, sewage is drained.
Claims (5)
1. a traditional Chinese medicine injection production ultrafiltration system, comprise stoste circulating tank, multistage pump, ultrafilter group, impurities removal pipeline, see through liquid pipeline and frequency-variable controller, it is characterized in that: described stoste circulating tank bottom delivery port connects multistage pump water inlet end, described multistage pump water side connects ultrafilter group bottom water inlet and impurities removal pipeline successively, described ultrafilter group bottom delivery port connects through liquid pipeline, and top delivery port connects stoste circulating tank top; Between described ultrafilter group top delivery port and stoste circulating tank top, cleaning blow-off pipe is set, described cleaning blow-off pipe end connects impurities removal pipeline; Described frequency-variable controller connects and controls multistage pump.
2. traditional Chinese medicine injection production ultrafiltration system according to claim 1, it is characterized in that: described ultrafilter group is comprised of at least two ultrafilters, and all ultrafilters bottom water inlet, delivery port and top delivery port are all in parallel, described bottom water inlet place in parallel and top delivery port place in parallel are equipped with Pressure gauge; The in parallel blast pipe that also has center of top, the end after described blast pipe parallel connection is provided with air bleeding valve.
3. traditional Chinese medicine injection production ultrafiltration system according to claim 1, it is characterized in that: the bottom delivery port of described ultrafilter group and seeing through between liquid pipeline is provided with through liquid valve, between bottom water inlet and impurities removal pipeline, be provided with eduction valve, between bottom water inlet and multistage pump, be provided with feed liquor butterfly valve; Pipeline between described feed liquor butterfly valve and multistage pump adopts pipeline to be connected with cleaning blow-off pipe middle part, and between be provided with recovery valve.
4. traditional Chinese medicine injection production ultrafiltration system according to claim 1, is characterized in that: described cleaning blow-off pipe beginning and end arrange respectively into dirty valve and blowoff valve, between described cleaning blow-off pipe beginning and stoste circulating tank, is provided with diaphragm valve.
5. traditional Chinese medicine injection production ultrafiltration system according to claim 1, is characterized in that: described stoste circulating tank can body outside is provided with fluid level controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420412891.7U CN203971767U (en) | 2014-07-25 | 2014-07-25 | Traditional Chinese medicine injection production ultrafiltration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420412891.7U CN203971767U (en) | 2014-07-25 | 2014-07-25 | Traditional Chinese medicine injection production ultrafiltration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203971767U true CN203971767U (en) | 2014-12-03 |
Family
ID=51969242
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420412891.7U Expired - Fee Related CN203971767U (en) | 2014-07-25 | 2014-07-25 | Traditional Chinese medicine injection production ultrafiltration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203971767U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108380054A (en) * | 2018-05-09 | 2018-08-10 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
-
2014
- 2014-07-25 CN CN201420412891.7U patent/CN203971767U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108380054A (en) * | 2018-05-09 | 2018-08-10 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 442100 Taishan Temple Industrial Park, Chengguan Town, Shiyan, Hubei, Fangxian Patentee after: SUNFLOWER GROUP HUBEI WUDANG Co.,Ltd. Address before: 442100 Taishan Temple Industrial Park, Shiyan, Hubei, Fangxian Patentee before: Hubei Wudang Jinding Pharmaceutical Co.,Ltd. |
|
| 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: 20141203 |