CN205760859U - A kind of liquid mixing system - Google Patents
A kind of liquid mixing system Download PDFInfo
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- CN205760859U CN205760859U CN201620612258.1U CN201620612258U CN205760859U CN 205760859 U CN205760859 U CN 205760859U CN 201620612258 U CN201620612258 U CN 201620612258U CN 205760859 U CN205760859 U CN 205760859U
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Abstract
A kind of liquid mixing system, has Agitation Tank, and Agitation Tank outer wall is provided with chuck, and Agitation Tank is provided with charging aperture, ingredients mouth, Butterworth Hatch, pure steam inlet, pure air intake and discharging opening, sets agitating device and clean device in Agitation Tank；The external proportioner of ingredients mouth；Cleaning device, external cleanout fluid device is connect in Butterworth Hatch；The external pure steam raising plant in pure steam inlet；The external pure air generator of pure air intake, and on pipeline, it has been sequentially connected in series ball valve D1, air filter and manual diaphragm valve J2, air filter arranges exhaustor A, exhaustor A is in series with pneumatic diaphragm valve F5, F6, the pipeline of air filter inlet end is provided with arm A and connects the exhaustor A between pneumatic diaphragm valve F5, F6, and the discharge outlet of air filter connects the exhaustor A of the pneumatic diaphragm valve F6 other end by ball valve D2 and arm B；This utility model is simple to operate, equipment cost is low, Disinfection Effect is good, it is achieved that manual/auto control.
Description
Technical field
This utility model is a kind of liquid mixing system, relates to the industries such as biological engineering, infusion solutions, oral liquid, fine chemistry
Material configures.
Background technology
Currently, liquid mixing system is widely used in the material configuration of the industries such as biological engineering, infusion solutions, oral liquid, fine chemistry,
Effectively eliminate cross-contamination and product microbiological contamination equivalent risk during configuration, improve production efficiency and the reliability of product.
Existing liquid mixing system has Agitation Tank, and Agitation Tank outer wall is provided with chuck, and chuck is for adding Agitation Tank
Heat or cooling, be provided with charging aperture, ingredients mouth, Butterworth Hatch, pure steam inlet, pure air intake and discharging opening on Agitation Tank, join
Being provided with agitating device in flow container and clean device, wherein agitating device has stirring motor, and the axle stretch end of stirring motor is equipped with turning
Axle, rotating shaft is positioned at Agitation Tank, turns the tip of the axis and installs the blade for stirring, and ingredients mouth is filled by pipeline docking dispensing
Putting (injection water device), Butterworth Hatch docks cleanout fluid device by pipeline, and pure steam generation is docked by pipeline in pure steam inlet
Device, pure air intake docks pure steam raising plant by pipeline, and equipped with air filter on pipeline.But, existing
Liquid mixing system there is problems in that (1) needs separately to set air vent on Agitation Tank, and install on the pipeline of air vent peripheral hardware
Air filter, in order to filtering discharging gas in Agitation Tank, this significantly increases equipment cost；(2) existing dosing
Cleaning systems, sterilization process are poor, it is impossible to accomplish each pipeline, especially to the sterilization of discharge nozzle, blow-off pipe and exhaustor, blow
Remaining water and dried, to reduce antibacterial residual to greatest extent；(3) existing liquid mixing system can only pass through each control knob
Valve event corresponding to Non-follow control is to complete to operate accordingly, it is impossible to accomplishes Automated condtrol, thus operates complexity, and work is strong
Degree is big, and production cost is high, and dispensing accuracy is low.
Summary of the invention
It is high that the purpose of this utility model seeks to solve current liquid mixing system equipment cost, clean, sterilization process poor, and
Can only Non-follow control, operation complexity, labor intensity is big, and production cost is high, and the problem that dispensing accuracy is low, for this kind of become
This is low, Disinfection Effect good, it is achieved the liquid mixing system of manual/auto control.
Concrete scheme of the present utility model is: a kind of liquid mixing system, has Agitation Tank, and Agitation Tank outer wall is provided with chuck,
Chuck for Agitation Tank is heated or cooled, Agitation Tank is provided with charging aperture, ingredients mouth, Butterworth Hatch, pure steam inlet,
Pure air intake and discharging opening, be provided with agitating device and clean device in Agitation Tank；It is characterized in that: at the pipeline that charging aperture is external
On equipped with manual diaphragm valve J1；Ingredients mouth connects proportioner by pneumatic diaphragm valve F1 and external pipeline；Connect clear in Butterworth Hatch
Cleaning device, and connect cleanout fluid device by pneumatic diaphragm valve F2 and external pipeline；Pure steam inlet by pneumatic diaphragm valve F3,
F4 and external pipeline connect pure steam raising plant；Pure air intake connects pure air generator by external pipeline, and
Being sequentially connected in series ball valve D1, air filter and manual diaphragm valve J2 on pipeline, wherein air filter arranges exhaustor A,
Be in series with pneumatic diaphragm valve F5, F6 on exhaustor A, the pipeline of air filter inlet end is provided with arm A connect pneumatic every
Exhaustor A between film valve F5, F6, it is another that the discharge outlet of air filter connects pneumatic diaphragm valve F6 by ball valve D2 and arm B
The exhaustor A of one end；At discharging opening equipped with manual diaphragm valve J3, and it is provided with external discharge nozzle, blow-off pipe and exhaustor B, its
Middle discharge nozzle, blow-off pipe are corresponding with on exhaustor B equipped with manual diaphragm valve J4, ball valve D3 and ball valve D4；Described pneumatic diaphragm valve
Unlatching/the closedown of F1, F2～F6 and the operation of agitating device are controlled by corresponding control knob respectively.
Chuck described in this utility model is provided with upper and lower fairlead, and upper fairlead is connected to steam and goes out pipe, commonly sky
Gas enters pipe and cooling water outlet tube, and goes out on pipe, normal air entrance pipe and cooling water outlet tube corresponding equipped with pneumatic section at steam
Only valve X1, X2, X3；Lower fairlead connects that steam enters pipe, drain pipe and cooling water enter pipe respectively, and wherein drain pipe connects exhaustor
A, drain pipe has been sequentially connected in series pneumatic stopping valve X4 and steam trap；Steam enters pipe and connects blow-off pipe, and enters dress on pipe at steam
There is pneumatic stopping valve X5；Enter on pipe equipped with pneumatic stopping valve X6 at cooling water；Described pneumatic stopping valve X1, X2～X6 are respectively by phase
The control knob answered controls it and opens/cut out.
This utility model is provided with bypass branch A, in bypass branch A on pipeline between pneumatic diaphragm valve F3, F4
Equipped with manual diaphragm valve J5；The pipeline of air filter outlet side is provided with bypass branch B, equipped with hands in bypass branch B
Dynamic diaphragm valve J6；It is equipped with air bleeding valve J7 in the side of manual diaphragm valve J3；Another of described bypass branch A and bypass branch B
End communicates, and connects air bleeding valve J7 by pipeline.
Equipped with relief valve S1 and pressure transducer P2 on the upper fairlead of chuck in this utility model；Occur at pure air
Device on the external pipeline at ball valve D1 place equipped with pressure transducer P3；Equipped with temperature sensor T2 on exhaustor A；Joining
Flow container is built with pressure transducer P1, temperature sensor T1 and liquid level sensor L1；Equipped with angle speed in the rotating shaft of agitating device
Degree sensor W1；Described pressure transducer P1～P3, temperature sensor T1～T2, liquid level sensor L1 and angular-rate sensor W1
Respectively communication connects PLC, and PLC communication connects touch screen, and realize pneumatic diaphragm valve F1, F2～F6 gentle
The real-time control that the unlatching/closedown of dynamic stop valve X1, X2～X6 and agitating device work run.
This utility model has the advantage that
(1) this utility model simple in construction, design ingenious, by use an air filter be simultaneously achieved dosing
The filtration of the pure air that tank is passed through when discharging and Agitation Tank discharge the filtration of gas after completing dispensing in tank, be substantially reduced
Equipment cost.
(2) this utility model is by design bypass branch A, B and air bleeding valve J7, it is achieved that to discharge nozzle, blow-off pipe and row
The sterilization of trachea, blow remaining water and dried, to decrease pipe Endophytic bacteria residual to greatest extent, effectively prevent intersection dirt
Dye.
(3) this utility model can not only realize the Non-follow control to liquid mixing system, and achieve and join liquid mixing system
Material, discharging, clean and the real-time monitoring of parameters in the Automated condtrol of these operations of sterilizing and blending process, so operate
Simple and convenient, greatly reduce operating cost, improve the accuracy of dispensing.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is control structure block diagram of the present utility model.
In figure: 1 Agitation Tank, 2 chucks, 3 charging apertures, 4 ingredients mouths, 5 Butterworth Hatch, 6 pure steam inlets,
7 pure air intakes, 8 discharging openings, 9 agitating devices, 10 cleaning devices, 11 proportioners, 12 cleanout fluid devices,
13 pure steam raising plants, 14 pure air generators, 15 air filters, 16 exhaustor A, 17 arm A,
18 arm B, 19 discharge nozzles, 20 blow-off pipes, 21 exhaustor B, fairlead on 22,23 times fairleads, 24 steam
Vapour goes out pipe, and 25 normal air enter pipe, 26 cooling water outlet tubes, and 27 steam enter pipe, 28 drain pipies, and 29 cooling water enter
Pipe, 30 steam traps, 31 bypass branch A, 32 bypass branch B, 33 PLC, 34 touch screens, 35 weigh mould
Block.
Detailed description of the invention
Seeing Fig. 1, this utility model has Agitation Tank 1, and Agitation Tank 1 outer wall is provided with chuck 2, and chuck 2 is for dosing
Tank 1 is heated or cooled, and is provided with charging aperture 3, ingredients mouth 4, Butterworth Hatch 5, pure steam inlet 6, pure air enter on Agitation Tank 1
Mouth 7 and discharging opening 8, be provided with agitating device 9 and clean device 10 in Agitation Tank 1；Particularly: at the external pipeline of charging aperture 3
On equipped with manual diaphragm valve J1；Ingredients mouth 4 connects proportioner 11 by pneumatic diaphragm valve F1 and external pipeline；In Butterworth Hatch 5
Connect cleaning device 10, and connect cleanout fluid device 12 by pneumatic diaphragm valve F2 and external pipeline；Pure steam inlet 6 is by pneumatic
Diaphragm valve F3, F4 and external pipeline connect pure steam raising plant 13；Pure air intake 7 connects pure air by external pipeline and sends out
Generating apparatus 14, and on pipeline, it has been sequentially connected in series ball valve D1, air filter 15 and manual diaphragm valve J2, wherein air filter
15 arrange exhaustor A16, are in series with pneumatic diaphragm valve F5, F6, at the pipeline of air filter 15 inlet end on exhaustor A16
Being provided with arm A17 and connect the exhaustor A16 between pneumatic diaphragm valve F5, F6, the discharge outlet of air filter 15 passes through ball valve
D2 and arm B18 connects the exhaustor A16 of the pneumatic diaphragm valve F6 other end；At discharging opening 8 equipped with manual diaphragm valve J3, and it is provided with
External discharge nozzle 19, blow-off pipe 20 and exhaustor B21, wherein discharge nozzle 19, blow-off pipe 20 corresponding with on exhaustor B21 equipped with
Manual diaphragm valve J4, ball valve D3 and ball valve D4；Unlatching/the closedown of described pneumatic diaphragm valve F1, F2～F6 and the fortune of agitating device 9
Row is controlled by corresponding control knob respectively.
Chuck 2 described in the present embodiment is provided with upper and lower fairlead 22,23, and upper fairlead 22 is connected to steam and goes out pipe
24, normal air enters pipe 25 and cooling water outlet tube 26, and goes out pipe 24, normal air entrance pipe 25 and cooling water outlet tube at steam
On 26, correspondence is equipped with pneumatic stopping valve X1, X2, X3；Lower fairlead 23 connects steam respectively and enters pipe 27, drain pipe 28 and cooling water
Entering pipe 29, wherein drain pipe 28 connects exhaustor A16, and drain pipe 28 has been sequentially connected in series pneumatic stopping valve X4 and steam trap 30；
Steam enters pipe 27 and connects blow-off pipe 20, and enters on pipe 27 equipped with pneumatic stopping valve X5 at steam；Cooling water enter on pipe 29 equipped with
Pneumatic stopping valve X6；Described pneumatic stopping valve X1, X2～X6 are controlled it by corresponding control knob respectively and open/close.
The present embodiment is provided with bypass branch A31, in bypass branch A31 on pipeline between pneumatic diaphragm valve F3, F4
On equipped with manual diaphragm valve J5；The pipeline of the outlet side of air filter 15 is provided with bypass branch B32, in bypass branch
B32 is upper equipped with manual diaphragm valve J6；It is equipped with air bleeding valve J7 in the side of manual diaphragm valve J3；Described bypass branch A31 is with other
The other end of road arm B32 communicates, and connects air bleeding valve J7 by pipeline.
See Fig. 2, equipped with relief valve S1 and pressure transducer P2 on the upper fairlead 22 of chuck 2 in the present embodiment；?
Pure air generator 14 on the external pipeline at ball valve D1 place equipped with pressure transducer P3；Equipped with temperature on exhaustor A16
Degree sensor T2；At Agitation Tank 1 built with pressure transducer P1, temperature sensor T1 and liquid level sensor L1；At agitating device 9
Rotating shaft on equipped with angular-rate sensor W1；Described pressure transducer P1～P3, temperature sensor T1～T2, liquid level sensor L1
Connect PLC 33(pressure transducer P1～P3 with angular-rate sensor W1 communication respectively and be alternatively Pressure gauge, temperature sensing
Device T1～T2 is alternatively thermometer), PLC 33 communication connects touch screen 34, and realizes pneumatic diaphragm valve F1, F2～F6
Unlatching/closedown with pneumatic stopping valve X1, X2～X6 and the real-time control of agitating device 9 work operation.
Below as a example by PLC is to the control in real time of the unlatching/closedown of each pneumatic diaphragm valve and pneumatic stopping valve,
Specific works process of the present utility model is described:
(1) charging: manually opened manual diaphragm valve J1, adds materials in Agitation Tank 1 from charging aperture 3, now stirs dress
Putting 9 beginning startup optimization, pneumatic stopping valve X3, X6 open, and cooling water enters from the lower fairlead 23 of chuck 2, from upper fairlead
22 discharge, and lower the temperature Agitation Tank 1；
(2) dispensing: pneumatic diaphragm valve F1 opens, and the injection water in proportioner 11 enters to along pipeline from ingredients mouth 4
In Agitation Tank 1, now the pressure transducer P1 in Agitation Tank 1, temperature sensor T1, liquid level sensor L1 will monitor in real time
Air pressure, feed temperature in tank body are transferred to PLC 33 with liquid level data, and PLC 33 passes according to angular velocity in real time
Data Control agitating device 9 mixing speed of sensor W1 monitoring, when the Weighing module 35 of peripheral hardware detects the current weight of Agitation Tank 1
When amount reaches requirement, PLC 33 controls pneumatic diaphragm valve F1 and closes, and proportioner 11 stops adding note in Agitation Tank 1
Jetting；
(3) discharging: manual unlocking ball valve D1, manual diaphragm valve J2, J3, J4, pure air generator 14 leads to along pipeline
Crossing air filter 15 and pure air intake 7 and be passed through pure air in Agitation Tank 1, the liquid configured in Agitation Tank 1 is at gas
Discharge from discharge nozzle 19 under the effect of pressure；
(4) cleaning: pneumatic diaphragm valve F2 opens, the cleanout fluid that cleanout fluid device 12 produces enters along pipeline from Butterworth Hatch 5
Enter to Agitation Tank 1, and by cleaning device 10 Agitation Tank 1 carried out internal washing, to be cleaned complete after, manually opened manually
Diaphragm valve J3 and ball valve D3, in tank, sewage is discharged from blow-off pipe 20；
(5) blowing Yu Shui: (a) and open ball valve D2, the condensed water in air filter 15 passes sequentially through ball valve D2, arm B18
Discharge with exhaustor A16；Manually opened ball valve D1, pneumatic diaphragm valve F6 open, and it is pure that the conveying of pure air generator 14 comes
Air passes sequentially through ball valve D1, arm A17 and pneumatic diaphragm valve F6 and purges the remaining water in exhaustor A16；B () manually opens
Opening ball valve D1, manual diaphragm valve J6, J7, and select successively to open manual diaphragm valve J4, ball valve D3, ball valve D4, pure air occurs
The pure air that device 14 conveying comes, after air filter 15 filters, realizes successively to discharge nozzle 19, blow-off pipe 20 and row
Remaining water in trachea B21 purges；
(6) sterilization: tank body is sterilized by (a): pneumatic diaphragm valve F3, F4 open, the conveying of pure steam raising plant 13 comes
Pure steam passes sequentially through pneumatic diaphragm valve F3, F4 along pipeline and pure air intake 6 enters to, in Agitation Tank 1, utilize high temperature pair
Antibacterial in tank body carries out disinfection；B the filter element of air filter 15 is carried out disinfection by (): manually opened manual diaphragm valve J2, gas
Dynamic diaphragm valve F5 opens, and the pure steam in tank body passes sequentially through manual diaphragm valve J2, the filter element of air filter 15 along pipeline
With arm A17, and by pneumatic diaphragm valve F5, finally discharge from exhaustor A16, thus reach the filter element to air filter 15
The purpose carried out disinfection；C discharge nozzle 19, blow-off pipe 20 are carried out disinfection by () with exhaustor B21: manually opened manual diaphragm valve
J2, J6, J7, and select successively to open manual diaphragm valve J4, ball valve D3, ball valve D4, the pure steam in tank body is along pipeline successively
Realize discharge nozzle 19, the high-temperature sterilization of blow-off pipe 20 and exhaustor B21；
(7) Agitation Tank 1 being dried process: (a) pneumatic stopping valve X3, X6 close, pneumatic stopping valve X2, X4 open,
Entering 25 by normal air and be passed through air in chuck 2, the cooling water in chuck 2 is under the influence of air pressure along lower fairlead
23 and drain pipe 28 discharge；B () pneumatic diaphragm valve F3 and pneumatic stopping valve X1, X5 open, and manually opened manual diaphragm valve J5,
J7 and ball valve D3, in the pure steam that the conveying of pure steam raising plant 13 comes is along Pipeline transport to chuck 2, and by upper extraction
Pipe 22 and steam go out pipe 24 and discharge, it is achieved thereby that heat the tank skin of Agitation Tank 1, and are issued in the effect of conduction of heat
Purpose withering to tank interior；C () manual unlocking manual diaphragm valve J3 and ball valve D3, in venting Agitation Tank 1
The condensed water condensed.
Claims (4)
1. a liquid mixing system, has Agitation Tank, and Agitation Tank outer wall is provided with chuck, chuck for Agitation Tank heated or
Cooling, is provided with charging aperture, ingredients mouth, Butterworth Hatch, pure steam inlet, pure air intake and discharging opening, Agitation Tank on Agitation Tank
Inside it is provided with agitating device and cleans device；It is characterized in that: equipped with manual diaphragm valve J1 on the pipeline that charging aperture is external；Ingredients mouth
Proportioner is connected by pneumatic diaphragm valve F1 and external pipeline；Cleaning device is connect in Butterworth Hatch, and by pneumatic diaphragm valve F2
Cleanout fluid device is connected with external pipeline；Pure steam inlet connects pure steam by pneumatic diaphragm valve F3, F4 and external pipeline and sends out
Generating apparatus；Pure air intake connects pure air generator by external pipeline, and has been sequentially connected in series ball valve D1, sky on pipeline
Air filter and manual diaphragm valve J2, wherein air filter arranges exhaustor A, is in series with pneumatic diaphragm valve on exhaustor A
F5, F6, be provided with arm A on the pipeline of air filter inlet end and connect the exhaustor A between pneumatic diaphragm valve F5, F6, empty
The discharge outlet of air filter connects the exhaustor A of the pneumatic diaphragm valve F6 other end by ball valve D2 and arm B；Discharging opening equipped with
Manual diaphragm valve J3, and it is provided with external discharge nozzle, blow-off pipe and exhaustor B, wherein on discharge nozzle, blow-off pipe and exhaustor B
Correspondence is equipped with manual diaphragm valve J4, ball valve D3 and ball valve D4；The unlatching of described pneumatic diaphragm valve F1, F2～F6/close and stir
The operation of device is controlled by corresponding control knob respectively.
A kind of liquid mixing system the most according to claim 1, is characterized in that: described chuck is provided with upper and lower fairlead, upper extraction
Pipe be connected to steam go out pipe, normal air enter pipe and cooling water outlet tube, and steam go out pipe, normal air enter pipe and
On cooling water outlet tube, correspondence is equipped with pneumatic stopping valve X1, X2, X3；Lower fairlead connects steam respectively and enters pipe, drain pipe and cooling
Water enters pipe, and wherein drain pipe connects exhaustor A, and drain pipe has been sequentially connected in series pneumatic stopping valve X4 and steam trap；Steam enters pipe
Connect blow-off pipe, and enter on pipe equipped with pneumatic stopping valve X5 at steam；Enter on pipe equipped with pneumatic stopping valve X6 at cooling water；Described
Pneumatic stopping valve X1, X2～X6 are controlled it by corresponding control knob respectively and open/close.
A kind of liquid mixing system the most according to claim 1, is characterized in that: on the pipeline between pneumatic diaphragm valve F3, F4
It is provided with bypass branch A, equipped with manual diaphragm valve J5 in bypass branch A；The pipeline of air filter outlet side is provided with side
Road arm B, equipped with manual diaphragm valve J6 in bypass branch B；It is equipped with air bleeding valve J7 in the side of manual diaphragm valve J3；Described
Bypass branch A communicates with the other end of bypass branch B, and connects air bleeding valve J7 by pipeline.
A kind of liquid mixing system the most according to claim 2, is characterized in that: equipped with relief valve S1 on the upper fairlead of chuck
With pressure transducer P2；Equipped with pressure transducer P3 on pure air generator to the external pipeline at ball valve D1 place；Row
Equipped with temperature sensor T2 on trachea A；At Agitation Tank built with pressure transducer P1, temperature sensor T1 and liquid level sensor
L1；Equipped with angular-rate sensor W1 in the rotating shaft of agitating device；Described pressure transducer P1～P3, temperature sensor T1～
T2, liquid level sensor L1 and angular-rate sensor W1 communication respectively connects PLC, and PLC communication connects touch screen,
And realize pneumatic diaphragm valve F1, F2～F6 and the unlatching/closedown of pneumatic stopping valve X1, X2～X6 and agitating device work are run
Real-time control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620612258.1U CN205760859U (en) | 2016-06-21 | 2016-06-21 | A kind of liquid mixing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620612258.1U CN205760859U (en) | 2016-06-21 | 2016-06-21 | A kind of liquid mixing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205760859U true CN205760859U (en) | 2016-12-07 |
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ID=58131997
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| CN201620612258.1U Active CN205760859U (en) | 2016-06-21 | 2016-06-21 | A kind of liquid mixing system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621990A (en) * | 2016-12-24 | 2017-05-10 | 无锡海达安全玻璃有限公司 | Solution mixing system |
| CN106726576A (en) * | 2016-12-27 | 2017-05-31 | 上海创洁科技股份有限公司 | A kind of supensoid agent prepares induction system |
| CN106881058A (en) * | 2017-04-06 | 2017-06-23 | 山东泰邦生物制品有限公司 | A kind of full-automatic solid-liquid separation system and preparation method thereof |
| CN109304128A (en) * | 2017-07-26 | 2019-02-05 | 上海至纯洁净系统科技股份有限公司 | If the liquid medicine dosing system and its cleaning method of T-type liquid filter |
-
2016
- 2016-06-21 CN CN201620612258.1U patent/CN205760859U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621990A (en) * | 2016-12-24 | 2017-05-10 | 无锡海达安全玻璃有限公司 | Solution mixing system |
| CN106726576A (en) * | 2016-12-27 | 2017-05-31 | 上海创洁科技股份有限公司 | A kind of supensoid agent prepares induction system |
| CN106726576B (en) * | 2016-12-27 | 2023-01-31 | 上海创洁科技有限公司 | Suspension preparation and conveying system |
| CN106881058A (en) * | 2017-04-06 | 2017-06-23 | 山东泰邦生物制品有限公司 | A kind of full-automatic solid-liquid separation system and preparation method thereof |
| CN106881058B (en) * | 2017-04-06 | 2023-02-03 | 山东泰邦生物制品有限公司 | Full-automatic solid-liquid separation and filtration system and cleaning method thereof |
| CN109304128A (en) * | 2017-07-26 | 2019-02-05 | 上海至纯洁净系统科技股份有限公司 | If the liquid medicine dosing system and its cleaning method of T-type liquid filter |
| CN109304128B (en) * | 2017-07-26 | 2024-01-23 | 上海至纯洁净系统科技股份有限公司 | Liquid medicine preparation system with T-shaped liquid filter and cleaning method thereof |
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