CN206868040U - A kind of complete liquid mixing system of liquid drugs injection - Google Patents
A kind of complete liquid mixing system of liquid drugs injection Download PDFInfo
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- CN206868040U CN206868040U CN201720665598.5U CN201720665598U CN206868040U CN 206868040 U CN206868040 U CN 206868040U CN 201720665598 U CN201720665598 U CN 201720665598U CN 206868040 U CN206868040 U CN 206868040U
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- filter
- preparing tank
- tank
- dilute
- liquid
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Abstract
The utility model provides a kind of complete liquid mixing system of liquid drugs injection, including：Injection waterpipe and the concentrated compounding system being sequentially connected with, dilute match system and package system, concentrated compounding system includes dense preparing tank, first sanitary pump and first filter, dilute match system includes dilute preparing tank, second sanitary pump, second filter and the 3rd filter, package system includes the 4th filter and surge tank, dense preparing tank is connected by the first sanitary pump with first filter, first filter is connected by the first pipeline with dense preparing tank, first filter is connected by second pipe with dilute preparing tank, dilute preparing tank is connected by the second sanitary pump with the second filter, second filter is connected with the 3rd filter, 3rd filter is connected by the 3rd pipeline with dilute preparing tank, 3rd filter is connected by the 4th pipeline with the 4th filter, 4th filter is connected with surge tank, the entrance of dense preparing tank dilute preparing tank is connected with injection waterpipe.The utility model can be realized online with liquid, on-line cleaning and online piecewising algorithms sterilizing.
Description
Technical field
It the utility model is related to and match somebody with somebody liquid technical field, more particularly to a kind of complete liquid mixing system of liquid drugs injection.
Background technology
For liquid drugs injection in process of production, it is necessary to which supplementary material is added into water for injection, stirring makes it all dissolve, and adjusts pH value, then
Water for injection is added to full dose, continues to stir, adds needle-use activated carbon stirring and adsorbing, decarburization is filtered, then through sterile
Filtering, obtain being available for the liquid drugs injection of embedding.Many links are by having been manually done in this production process at present, are so easily mixed into micro-
Biology, cause by the gross liquid drugs injection finished product scrap, be also easy to cause in addition uneven with liquid, cause the quality of each production batch of liquid drugs injection
Homogeneity is poor.Meanwhile cleaning for liquid mixing system and sterilizing are also without the cleaning process of standard.
Utility model content
The purpose of this utility model be to provide it is a kind of with liquid precisely and can on-line cleaning and the liquid drugs injection that online piecewising algorithms sterilize into
Cover liquid mixing system.
The technical scheme that the utility model solves above-mentioned technical problem is as follows：
A kind of complete liquid mixing system of liquid drugs injection, including：Injection waterpipe and be sequentially connected with concentrated compounding system, dilute match system and
Package system, the concentrated compounding system include dense preparing tank, the first sanitary pump and first filter, and dilute match system includes dilute match somebody with somebody
Tank, the second sanitary pump, the second filter and the 3rd filter, the package system includes the 4th filter and surge tank, described
Dense preparing tank is connected by first sanitary pump with the first filter, and the first filter passes through the first pipeline and institute
State dense preparing tank to be connected, the first filter is connected by second pipe with the dilute preparing tank, and the dilute preparing tank passes through institute
State the second sanitary pump with second filter to be connected, second filter is connected with the 3rd filter, described
3rd filter is connected by the 3rd pipeline with the dilute preparing tank, and the 3rd filter passes through the 4th pipeline and the described 4th
Filter is connected, and the 4th filter is connected with the surge tank, the entrance of the dense preparing tank and the dilute preparing tank
Entrance is connected with the injection waterpipe.
On the basis of above-mentioned technical proposal, the utility model can also do following improvement：
Alternatively, in addition to waste pipe, the dense preparing tank, first sanitary pump, the first filter, described dilute
Given up with described the outlet of distribution tank, second sanitary pump, second filter, the 3rd filter and the surge tank
Waterpipe is connected.
Alternatively, in addition to pure steam pipeline, the entrance of the dense preparing tank, the dilute preparing tank and the 3rd filter are equal
It is connected with the pure steam pipeline.
Alternatively, in addition to condensing water conduit, the dense preparing tank, the first filter, the dilute preparing tank, described second
The outlet of filter, the 3rd filter and the surge tank is connected with the condensing water conduit.
Alternatively, the first filter is stud filter, second filter, the 3rd filter and described
4th filter is microporous membrane filters.
Alternatively, the filtering accuracy of the first filter is 4.0 μm, and the filtering accuracy of second filter is 0.45
μm, the filtering accuracy of the 3rd filter is 0.22 μm, and the filtering accuracy of the 4th filter is 0.22 μm.
Alternatively, respectively set respectively on first pipeline, the second pipe, the 3rd pipeline and the 4th pipeline
There is a glass tube visor.
Alternatively, capacitance level gauge is provided with the surge tank, is provided with the surge tank top entry into hydraulic pneumatic
Valve, interaction relation is formed between the capacitance level gauge and the feed liquor pneumatic operated valve, to be measured by the capacitance type liquid level
The level value obtained controls being turned on and off for the feed liquor pneumatic operated valve.
Alternatively, in addition to it is used for the first PLC for controlling concentrated compounding system, the first liquid level is provided with the dense preparing tank
Meter, is provided with the first electrical proportional ball valve at the dense preparing tank top entry, first PLC respectively with first liquid
Position meter and the first electrical proportional ball valve electrical connection.
Alternatively, in addition to it is used for the second PLC for controlling dilute match system, the second liquid level is provided with the dilute preparing tank
Meter, is provided with the second electrical proportional ball valve at the dilute preparing tank top entry, second PLC respectively with second liquid
Position meter and the second electrical proportional ball valve electrical connection.
The beneficial effects of the utility model：
The complete liquid mixing system of liquid drugs injection of the present utility model, is made up of concentrated compounding system, dilute match system and package system, in concentrated compounding
The material inhaled in system by first filter after carbon processing is entered in dilute preparing tank, and the material after dilute preparing tank is handled is successively
Filtered by the second filter and the 3rd filter twice, most enter surge tank after the 4th filter sterilised afterwards, completed canned.
The utility model can be realized online with liquid, on-line cleaning and online piecewising algorithms sterilizing, and passes through the first PLC and second
PLC controls with liquid precision.
Brief description of the drawings
Fig. 1 is the structural representation of the complete liquid mixing system of liquid drugs injection of the utility model embodiment.
Reference：
Inject waterpipe -11；Pure steam pipeline -12；Waste pipe -13；Condensing water conduit -14；
Concentrated compounding system -20；Dense preparing tank -21；First sanitary pump -22；First filter -23；
Dilute match system -30；Dilute preparing tank -31；Second sanitary pump -32；Second filter -33；
3rd filter -34；
Package system -40；4th filter -41；Surge tank -42；
First pipeline 51；Second pipe -52；3rd pipeline -53；4th pipeline -54；
Glass tube visor -61；Thermometer -62；Conductivity meter -63.
Embodiment
Principle of the present utility model and feature are described below in conjunction with accompanying drawing, example is served only for explaining this practicality
It is new, it is not intended to limit the scope of the utility model.
Fig. 1 is the structural representation of the complete liquid mixing system of liquid drugs injection of the utility model embodiment.It is new referring to Fig. 1, this practicality
Type embodiment provides a kind of complete liquid mixing system of liquid drugs injection, including：Injection waterpipe 11 and be sequentially connected with concentrated compounding system 20,
Dilute match system 30 and package system 40, the concentrated compounding system 20 include dense preparing tank 21, the first sanitary pump 22 and first filter 23,
Dilute match system 30 includes dilute preparing tank 31, the second sanitary pump 32, the second filter 33 and the 3rd filter 34, the encapsulation system
System 40 includes the 4th filter 41 and surge tank 42, and the dense preparing tank 21 passes through first sanitary pump 22 and the described first filtering
Device 23 is connected, and the first filter 23 is connected by the first pipeline 5151 with the dense preparing tank 21, first filtering
Device 23 is connected by second pipe 52 with the dilute preparing tank 31, the dilute preparing tank 31 by second sanitary pump 32 with it is described
Second filter 33 is connected, and second filter 33 is connected with the 3rd filter 34, the 3rd filter 34
It is connected by the 3rd pipeline 53 with the dilute preparing tank 31, the 3rd filter 34 passes through the 4th pipeline 54 and the 4th mistake
Filter 41 is connected, and the 4th filter 41 is connected with the surge tank 42, the entrance of the dense preparing tank 21 and described dilute
The entrance of distribution tank 31 is connected with the injection waterpipe 11.
The complete liquid mixing system of liquid drugs injection of the present utility model, is made up of concentrated compounding system 20, dilute match system 30 and package system 40,
The material inhaled in concentrated compounding system 20 by first filter 23 after carbon processing is entered in dilute preparing tank 31, at dilute preparing tank 31
Material after reason filters by the second filter 33 and the twice of the 3rd filter 34 successively, most afterwards after the sterilizing of the 4th filter 41
Into surge tank 42, complete canned.The utility model can be realized matches somebody with somebody liquid, on-line cleaning and online piecewising algorithms sterilizing online, and
Controlled by the first PLC and the second PLC with liquid precision.
It is as follows that process with liquid is carried out using the complete liquid mixing system of liquid drugs injection of the present utility model：Injection water from injection waterpipe
11 are entered in dense preparing tank 21 by the entrance of dense preparing tank 21, and other auxiliary materials enter concentrated compounding by the dog-house at the top of dense preparing tank 21
In tank 21, injection water and other auxiliary materials are mixed into dense material, and after the completion of dense material mixing, first is delivered to by the first sanitary pump 22
Filter 23 carries out carbonization treatment, opens the first pipeline 51 and closes second pipe 52, the dense material after carbonization treatment leads to
Cross the first pipeline 51 and be sent into dense preparing tank 21 and continue mixed processing, form a partial circulating.From going out for first filter 23
Whether sampling checking feed liquid is clarified in the dense material of mouthful outflow, if verifying feed clarification, opens second channel and closes the
One pipeline 51 so that dense material is entered in dilute preparing tank 31 by second pipe 52, and injection water is sent in dilute preparing tank 31 and dense thing
Material is mixed to form dilute material, and dilute material is delivered to the second filter 33 by the second sanitary pump 32 and the 3rd filter 34 is carried out successively
The filtration treatment of different filtering accuracies, open the 3rd pipeline 53 and close the 4th pipeline 54, the dilute material after filtered processing is led to
Cross the 3rd pipeline 53 and be sent into dilute preparing tank 31 and continue mixed processing, form a partial circulating.From going out for the 3rd filter 34
Whether sampling checking feed liquid is qualified in the dilute material of mouthful outflow, if checking out-feed liquid is qualified, opens fourth lane and closes the
Three pipelines 53 so that qualified dilute material is entered in the 4th filter 41 by the 4th pipeline 54 carries out bacteria removing, and qualified is dilute
Material, which enters, prepares encapsulation in surge tank 42, so far, that completes liquid drugs injection matches somebody with somebody liquid and encapsulation.
Referring to Fig. 1, in addition to waste pipe 13, the dense preparing tank 21, first sanitary pump 22, the first filter
23rd, the dilute preparing tank 31, second sanitary pump 32, second filter 33, the 3rd filter 34 and the buffering
The outlet of tank 42 is connected with the waste pipe 13.
The complete liquid mixing system of liquid drugs injection of the present utility model, in addition to the on-line cleaning system with function of on-line cleaning.Clearly
Need the filter core of four filters pulling down offline cleaning before washing.Function of on-line cleaning is carried out before liquid is matched somebody with somebody every time.Respectively to
Injection water is injected in dense preparing tank 21 and dilute preparing tank 31, keeps the water not less than 70% volume, carries out each part of whole system
And the cleaning of pipeline, the waste water through over cleaning flow out from the waste pipe 13 each exported respectively.Wherein, all waste pipes
Conductivity meter 63 is installed in road 13, detects whether the system reaches medical cleaning requirement by conductivity meter 63, and print
Go out to clean conductivity data report.
Referring to Fig. 1, in addition to pure steam pipeline 12, the dense preparing tank 21, the dilute preparing tank 31 and the 3rd filter
34 entrance is connected with the pure steam pipeline 12.Also include condensing water conduit 14, the dense preparing tank 21, first filtering
Device 23, the dilute preparing tank 31, second filter 33, the 3rd filter 34 and the surge tank 42 outlet and institute
Condensing water conduit 14 is stated to be connected.
The complete liquid mixing system of liquid drugs injection of the present utility model, in addition to the system of the fractional sterilization with online piecewising algorithms sterilizing function
System.Online piecewising algorithms sterilize and carried out after on-line cleaning.Respectively pure steam, pure steam are passed through into dense preparing tank 21 and dilute preparing tank 31
Flowed according to the trend with liquid material, the high temperature of pure steam can sterilize to each part and pipeline of whole system
Processing, when the temperature of pure steam reaches 121 DEG C, sterilizing can be reached and required.Pure steam temperature after the second filter 33
It has been declined that, its temperature is reached 121 DEG C again, it is necessary to the regular hour to the sterilizing of the 3rd filter 34 of back segment, therefore, directly
Connect and pure steam is passed into the 3rd filter 34 so that the second filter 33 and the 3rd filter 34 are passed through pure steam simultaneously and entered
Row sterilizing, can save sterilization time.In addition, pure steam from the top of dense preparing tank 21 by the first pipeline 51, approach second pipe 52,
Condensing water conduit 14 is finally reached, completes the sterilization process of concentrated compounding system 20.
Pure steam, by the 3rd pipeline 53, the pipeline 54 of approach the 4th, is passed through in the 4th filter 41, arrived from the top of dilute preparing tank 31
Up to surge tank 42, condensing water conduit 14 is finally reached, completes the sterilization process of dilute match system 30.High temperature pure steam is by whole system
Each part and pipeline of system, cooling produces condensed water to the cold, and is flowed out respectively from the condensing water conduit 14 each exported.Its
In, it is mounted on leading PT100 thermometers 62 in all condensing water conduits 14, the system is detected by leading PT100 thermometers 62
Whether reach medicine sterilizing to require, and print sterilising temp and Time Data Report.
Wherein, the first filter 23 is stud filter, second filter 33, the and of the 3rd filter 34
4th filter 41 is microporous membrane filters.
Wherein, the filtering accuracy of the first filter 23 is 4.0 μm, and the filtering accuracy of second filter 33 is
0.45 μm, the filtering accuracy of the 3rd filter 34 is 0.22 μm, and the filtering accuracy of the 4th filter 41 is 0.22 μm.
Referring to Fig. 1, first pipeline 51, the second pipe 52, the 3rd pipeline 53 and the 4th pipeline 54
It is upper to be respectively provided with a glass tube visor 61 respectively.In addition, can also on respective waste pipe 13 and condensing water conduit 14
Glass tube visor 61 is installed.
By glass tube visor 61, the whereabouts of liquid drugs injection decoction can be conveniently observed, it is particularly installed above in blow-off line
Glass tube visor 61, can be visually seen liquid drugs injection decoction can or can not be lost in.
Referring to Fig. 1, capacitance level gauge is provided with the surge tank 42, feed liquor is provided with the top entry of surge tank 42
Pneumatic operated valve, interaction relation is formed between the capacitance level gauge and the feed liquor pneumatic operated valve, to pass through the capacitance type liquid level
The level value measured controls being turned on and off for the feed liquor pneumatic operated valve.
Before canned, need to set a standard level value first.Capacitance level gauge is used to detect in surge tank 42
Level value, if level value is less than standard level value, feed liquor pneumatic operated valve can automatically open up feed liquor, if level value is higher than titer
Place value, feed liquor pneumatic operated valve can close feed liquor automatically.So package system 40 does not need manual operation, fully achieves auto-filling.
Referring to Fig. 1, in addition to for controlling the first PLC of concentrated compounding system 20, the is provided with the dense preparing tank 21
One liquid level gauge, is provided with the first electrical proportional ball valve at the top entry of dense preparing tank 21, first PLC respectively with institute
State first liquid level gauge and the first electrical proportional ball valve electrical connection.
Injection water required for being set first by the first PLC, then the first PLC is to the first electronics
Proportional ball valve sends open command, and the first electrical proportional ball valve is opened, and injection water is entered in dense preparing tank 21, and first liquid level gauge is real
When detect water level value in dense preparing tank 21, and the water level value is sent to the first PLC in real time, the first PLC will
Water level value is contrasted with injection water set in advance, and when water level value reaches injection water set in advance, then the first PLC is controlled
Device processed sends out code to the first electrical proportional ball valve, and the first electrical proportional ball valve is closed, and completes the injection water of dense preparing tank 21
Injection.
Referring to Fig. 1, in addition to for controlling the second PLC of dilute match system 30, the is provided with the dilute preparing tank 31
Two liquid level gauges, are provided with the second electrical proportional ball valve at the top entry of dilute preparing tank 31, second PLC respectively with institute
State second liquid level gauge and the second electrical proportional ball valve electrical connection.
Injection water required for being set first by the second PLC, then the second PLC is to the second electronics
Proportional ball valve sends open command, and the second electrical proportional ball valve is opened, and injection water is entered in dilute preparing tank 31, and second liquid level gauge is real
When detect water level value in dilute preparing tank 31, and the water level value is sent to the second PLC in real time, the second PLC will
Water level value is contrasted with injection water set in advance, and when water level value reaches injection water set in advance, then the 2nd PLC is controlled
Device processed sends out code to the second electrical proportional ball valve, and the second electrical proportional ball valve is closed, and completes the injection water of dilute preparing tank 31
Injection.
It should be noted that the first PLC of the present utility model or the second PLC also respectively with on-line cleaning
System and online piecewising algorithms disinfection system are connected, and are realized by the first PLC or the second PLC to on-line cleaning
The control of system and online piecewising algorithms disinfection system.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modification, equivalent substitution and improvements made etc., guarantor of the present utility model should be included in
Within the scope of shield.
Claims (10)
- A kind of 1. complete liquid mixing system of liquid drugs injection, it is characterised in that including：Injection waterpipe and be sequentially connected with concentrated compounding system, Dilute match system and package system, the concentrated compounding system include dense preparing tank, the first sanitary pump and first filter, dilute match system Including dilute preparing tank, the second sanitary pump, the second filter and the 3rd filter, the package system includes the 4th filter and buffering Tank, the dense preparing tank are connected by first sanitary pump with the first filter, and the first filter passes through first Pipeline is connected with the dense preparing tank, and the first filter is connected by second pipe with the dilute preparing tank, described dilute to match somebody with somebody Tank is connected by second sanitary pump with second filter, and second filter is connected with the 3rd filter Connect, the 3rd filter is connected by the 3rd pipeline with the dilute preparing tank, the 3rd filter by the 4th pipeline with 4th filter is connected, and the 4th filter is connected with the surge tank, the entrance of the dense preparing tank and described The entrance of dilute preparing tank is connected with the injection waterpipe.
- 2. the complete liquid mixing system of liquid drugs injection according to claim 1, it is characterised in that also including waste pipe, the concentrated compounding Tank, first sanitary pump, the first filter, the dilute preparing tank, second sanitary pump, second filter, institute The outlet for stating the 3rd filter and the surge tank is connected with the waste pipe.
- 3. the complete liquid mixing system of liquid drugs injection according to claim 2, it is characterised in that described dense also including pure steam pipeline The entrance of distribution tank, the dilute preparing tank and the 3rd filter is connected with the pure steam pipeline.
- 4. the complete liquid mixing system of liquid drugs injection according to claim 3, it is characterised in that described dense also including condensing water conduit Distribution tank, the first filter, the dilute preparing tank, second filter, the 3rd filter and the surge tank go out Mouth is connected with the condensing water conduit.
- 5. the complete liquid mixing system of liquid drugs injection according to claim 1, it is characterised in that the first filter filters for stud Device, second filter, the 3rd filter and the 4th filter are microporous membrane filters.
- 6. the complete liquid mixing system of liquid drugs injection according to claim 5, it is characterised in that the filtering accuracy of the first filter For 4.0 μm, the filtering accuracy of second filter is 0.45 μm, and the filtering accuracy of the 3rd filter is 0.22 μm, the The filtering accuracy of four filters is 0.22 μm.
- 7. the complete liquid mixing system of liquid drugs injection according to claim 1, it is characterised in that first pipeline, second pipe A glass tube visor is respectively provided with respectively on road, the 3rd pipeline and the 4th pipeline.
- 8. the complete liquid mixing system of liquid drugs injection according to claim 1, it is characterised in that be provided with condenser type liquid in the surge tank Position is counted, and feed liquor pneumatic operated valve is provided with the surge tank top entry, between the capacitance level gauge and the feed liquor pneumatic operated valve Interaction relation is formed, unlatching or the pass of the feed liquor pneumatic operated valve are controlled with the level value measured by the capacitance level gauge Close.
- 9. the complete liquid mixing system of liquid drugs injection according to any one of claim 1-8, it is characterised in that also include being used to control First PLC of concentrated compounding system, is provided with first liquid level gauge in the dense preparing tank, provided with the at the dense preparing tank top entry One electrical proportional ball valve, first PLC are electric with the first liquid level gauge and the first electrical proportional ball valve respectively Connection.
- 10. the complete liquid mixing system of liquid drugs injection according to any one of claim 1-8, it is characterised in that also include being used to control The second PLC of dilute match system is made, second liquid level gauge is provided with the dilute preparing tank, is provided with the dilute preparing tank top entry Second electrical proportional ball valve, second PLC respectively with the second liquid level gauge and the second electrical proportional ball valve Electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720665598.5U CN206868040U (en) | 2017-06-08 | 2017-06-08 | A kind of complete liquid mixing system of liquid drugs injection |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720665598.5U CN206868040U (en) | 2017-06-08 | 2017-06-08 | A kind of complete liquid mixing system of liquid drugs injection |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206868040U true CN206868040U (en) | 2018-01-12 |
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ID=61338248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720665598.5U Expired - Fee Related CN206868040U (en) | 2017-06-08 | 2017-06-08 | A kind of complete liquid mixing system of liquid drugs injection |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206868040U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051251A (en) * | 2017-06-08 | 2017-08-18 | 江苏鑫东方环保设备科技有限公司 | A kind of complete liquid mixing system of liquid drugs injection |
| CN112755884A (en) * | 2021-01-15 | 2021-05-07 | 韩俊红 | A even agitating unit for powder injection medicine detects |
-
2017
- 2017-06-08 CN CN201720665598.5U patent/CN206868040U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051251A (en) * | 2017-06-08 | 2017-08-18 | 江苏鑫东方环保设备科技有限公司 | A kind of complete liquid mixing system of liquid drugs injection |
| CN112755884A (en) * | 2021-01-15 | 2021-05-07 | 韩俊红 | A even agitating unit for powder injection medicine detects |
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|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180112 Termination date: 20210608 |