CN205762817U - A kind of CIP on-line cleaning system - Google Patents
A kind of CIP on-line cleaning system Download PDFInfo
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- CN205762817U CN205762817U CN201620612307.1U CN201620612307U CN205762817U CN 205762817 U CN205762817 U CN 205762817U CN 201620612307 U CN201620612307 U CN 201620612307U CN 205762817 U CN205762817 U CN 205762817U
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Abstract
A kind of CIP on-line cleaning system, include water storing tank and purge tank, and be furnished with pipeline purging system, water storing tank and purge tank are equipped with purified water entrance, recirculated water entrance, air vent and sewage draining exit, it is additionally provided with injection water entrance on water storing tank, purge tank is additionally provided with alkali liquor inlet;The sewage draining exit of water storing tank and purge tank is respectively by pipeline and the delivery pump connecting line purging system of docking;Pipeline purging system has additional electric heater;Alkali liquor inlet is by the liquid distribution pipe of the docking pipeline that connect dosing pump and delivery pump discharge end corresponding with alkali liquor circulation pipe;Each pipeline is respectively arranged with Pneumatic/electric control valve;Water storing tank and purge tank and corresponding pipeline are configured with sensor and communication connects PLC, to realize delivery pump and the start and stop of dosing pump and the real-time control of each Pneumatic/electric control valve on off state;This utility model automaticity is high, easy and simple to handle, and cleaning performance is good, it is achieved that to detergent line or the dried of equipment.
Description
Technical field
This utility model relates to a kind of purging system, especially a kind of CIP on-line cleaning system.
Background technology
CIP on-line cleaning system (Cleaning in place) refers to equipment (tank body, pipeline, pump, filter etc.) and whole
The cleaning solution of uniform temperature, without artificial unloading or on the premise of opening, within a scheduled time, is passed through by individual production line
Airtight pipeline carries out Sprayer Circulation to equipment inner surface and reaches the purpose cleaned.
But, the problem that existing CIP on-line cleaning system exists is as follows: (1) operation complexity, automaticity is low, no
Possesses automatic formulation function, when external equipment is carried out, it is impossible to parameters, inefficiency are set quickly and accurately
Under;(2) current CIP on-line cleaning system does not possess pipeline drying function so that have cleanout fluid residual to affect product in pipeline
Quality;(3) current CIP on-line cleaning system is not provided with insulation and heater, to there being paste drug residue
When tank skin is carried out, owing to this quasi drugs has, adhesive force is strong, more sensitive to temperature, the not feature such as easy cleaning, particularly
Just program jelly when temperature is less than certain value, be less susceptible to clean, if thus cleaning temperature can not be controlled, may result in clear
Wash the most thorough;(4) it is not provided with tank insulating structure and corresponding pipeline heating function, causes cleanout fluid thermal loss big, special
It is not when cleaning at a distance, causes cleaning performance poor owing to cleanout fluid heat waste is serious.
Summary of the invention
The purpose of this utility model seeks to solve current the problems referred to above existing for CIP on-line cleaning system, for this
One is easy and simple to handle, automaticity is high, cleaning is thorough, and possesses the CIP on-line cleaning system of pipeline heating function.
Concrete scheme of the present utility model is: a kind of CIP on-line cleaning system, includes water storing tank and purge tank, and joins
There is pipeline purging system, the external equipment to be cleaned of pipeline purging system, water storing tank and purge tank are equipped with purified water and enter
Mouth, recirculated water entrance, air vent and sewage draining exit, and on water storing tank, it is additionally provided with injection water entrance, purge tank is additionally provided with alkali
Liquid entrance, the sewage draining exit of water storing tank is to being connected to blow-off pipe A and water-supply-pipe, and the sewage draining exit of purge tank is to being connected to blow-off pipe B and defeated alkali
Liquid pipe, water-supply-pipe is connected with the other end of defeated alkali liquor pipe, and by tube for transfusion connecting line purging system, fills on tube for transfusion
There is delivery pump, it is characterized in that: described pipeline purging system includes blowing plant and appendix, equipped with pressure on appendix
Table, electric heater and air filter and some hand control valves and Pneumatic/electric control valve;The alkali liquor of described purge tank enters
Mouth is connected respectively the tube for transfusion of dosing pump and delivery pump discharge end by the liquid distribution pipe of docking and alkali liquor circulation pipe;Described row
It is respectively provided with Pneumatic/electric control on dirty pipe A, water-supply-pipe, blow-off pipe B, defeated alkali liquor pipe, tube for transfusion, liquid distribution pipe and alkali liquor circulation pipe
Valve processed;Equipped with liquid level sensor LC1 and temperature sensor TC1 on water storing tank, on purge tank equipped with liquid level sensor LC2 and
Temperature sensor TC2, equipped with conductivity sensor CC1, pressure transducer PC1 and temperature sensor TC3, liquid level on tube for transfusion
Sensor LC1~LC2, temperature sensor TC1~TC3, conductivity sensor CC1 and pressure transducer PC1 communication respectively connects
PLC, PLC communication connects touch screen, and realizes the start and stop to delivery pump and dosing pump and each Pneumatic/electric
The real-time control of control valve on off state.
Thermometer it is respectively arranged with on water storing tank described in this utility model and purge tank, and at water storing tank and the outer wall of purge tank
It is provided with heat-insulation layer.
Equipped with heat exchanger on tube for transfusion described in this utility model;The arrival end of the heat exchanger tube of heat exchanger is connected by pipeline
Industrial steam generating means, and equipped with Pneumatic/electric control valve on pipeline, and its switch shape is controlled in real time by PLC
State;Equipped with steam trap on the pipeline of the port of export docking of the heat exchanger tube of heat exchanger.
The recirculated water entrance docking backflow arm A of water storing tank described in this utility model, the recirculated water entrance pair of purge tank
Taking back stream arm B, the other end of backflow arm A, B is connected, and connects equipment to be cleaned by return main, main in backflow
Equipped with reflux pump and conductivity sensor CC2 on Guan, and peripheral hardware blow-off pipe C;Described blow-off pipe A, B, C and delivery pump and reflux pump
On blow-off pipe be all connected with blowdown supervisor, and at backflow arm A, backflow arm B, return main, blow-off pipe C and delivery pump and return
Being respectively arranged with Pneumatic/electric control valve on blow-off pipe on stream pump, described conductivity sensor CC2 communication connects PLC,
PLC realizes the start and stop to reflux pump and backflow arm A, backflow arm B, return main, blow-off pipe C and delivery pump and returns
The real-time control of the on off state of each Pneumatic/electric control valve on blow-off pipe on stream pump.
The injection water entrance of water storing tank described in this utility model connects injection water generating means by pipeline;Described water storage
The purified water entrance of tank and purge tank all connects purified water generating means by pipeline;Described water storing tank and the air vent of purge tank
It is respectively arranged with exhaust gas filter;On the pipeline of injection water entrance side and water storing tank and purge tank purified water entrance side pipeline on
It is respectively arranged with Pneumatic/electric control valve, and is controlled its on off state by PLC in real time.
This utility model has the advantage that
(1) this utility model automaticity is high, easy and simple to handle, it is achieved that to the automatic control of concentration of lye in purge tank
System, when being carried out a certain equipment or pipeline, it is possible to arranges parameters quickly and accurately, and controls to open accordingly
Water pump and valve, it is achieved that automatization is cleaned, cleaning efficiency is high;
(2) this utility model is by installing electric heater in pipeline purging system, enters pipeline to be cleaned or equipment
Row dried, effectively prevent and affect product quality because of pipeline cleaning liquid inside residual;
(3) this utility model is by arranging heat-insulation layer on water storing tank and purge tank outer wall, and configures on tube for transfusion and change
Hot device, it is ensured that the temperature of cleanout fluid in on-line cleaning system, and effectively prevent the thermal loss cleaned in course of conveying, really
Protect cleaning performance, be particularly suited for the cleaning to the tank skin having paste drug residue.
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 water storing tank, 2 purge tanks, 3 liquid dispensing devices, 4 purified water entrances, 5 recirculated water entrances, 6
Air vent, 7 sewage draining exits, 8 injection water entrances, 9 alkali liquor inlets, 10 blow-off pipe A, 11 water-supply-pipes, 12 blow-off pipes
B, 13 defeated alkali liquor pipes, 14 tube for transfusions, 15 delivery pumps, 16 blowing plants, 17 appendixs, 18 Pressure gauge A,
19 Pressure gauge B, 20 electric heaters, 21 air filters, 22 liquid distribution pipes, 23 alkali liquor circulation pipes, 24 dosing pumps,
25 PLC, 26 touch screens, 27 backflow arm A, 28 backflow arm B, 29 return mains, 30 reflux pumps,
31 blow-off pipe C, 32 blowdown supervisors, 33 heat exchangers, 34 industrial steam generating meanss, 35 steam traps, 36 injections
Water generating device, 37 purified water generating meanss, 38 exhaust gas filters, 39 thermometers, 40 heat-insulation layers, LC1, LC2
Liquid level sensor, TC1, TC2, TC3 temperature sensor, CC1, CC2 conductivity sensor, PC1 pressure transducer, D1,
D2 ball valve, P1 air relief valve, T1, T2 pneumatic stopping valve, S1 check-valves, F1, F2~F17 pneumatic diaphragm valve.
Detailed description of the invention
Below as a example by the cleaning to liquid dispensing device, this utility model is specifically described, wherein the present embodiment relates to
And to hand control valve be specially ball valve, check-valves, the Pneumatic/electric control valve related in the present embodiment is the most pneumatic
Stop valve, pneumatic diaphragm valve and pneumatic pressure-release valve.
Seeing Fig. 1-2, this utility model includes water storing tank 1 and purge tank 2, and is furnished with pipeline purging system, and pipeline blows
The external liquid dispensing device of system of sweeping 3, is equipped with purified water entrance 4, recirculated water entrance 5, air vent 6 on water storing tank 1 and purge tank 2
And sewage draining exit 7, and on water storing tank 1, it is additionally provided with injection water entrance 8, purge tank 2 is additionally provided with alkali liquor inlet 9, water storing tank 1
Sewage draining exit is to being connected to blow-off pipe A10 and water-supply-pipe 11, and the sewage draining exit of purge tank 2 is to being connected to blow-off pipe B12 and defeated alkali liquor pipe 13, defeated
Water pipe 11 is connected with the other end of defeated alkali liquor pipe 13, and by tube for transfusion 14 connecting line purging system, on tube for transfusion 14
Equipped with delivery pump 15;Described pipeline purging system includes blowing plant 16 and appendix 17, fills successively on appendix 17
There are Pressure gauge A18, ball valve D1, air relief valve P1, pneumatic stopping valve T1, electric heater 20, air filter 21, ball valve D2, non-return
Valve S1 and Pressure gauge B19 and pneumatic diaphragm valve F1;The alkali liquor inlet of described purge tank 2 is by the liquid distribution pipe 22 docked and alkali liquor
Circulation pipe 23 is connected respectively the tube for transfusion of dosing pump 24 and delivery pump 15 discharge end;Described blow-off pipe A10, water-supply-pipe 11,
On blow-off pipe B12, defeated alkali liquor pipe 13, tube for transfusion 14, liquid distribution pipe 22 and alkali liquor circulation pipe 23 corresponding equipped with pneumatic diaphragm valve F2,
F3, F4, F5, F6, F7, F8, wherein tube for transfusion 14 is connected to pneumatic diaphragm valve F1 to the appendix between liquid dispensing device 3;
The recirculated water entrance docking backflow arm A27 of described water storing tank 1, equipped with pneumatic diaphragm valve on backflow arm A27
F9;The recirculated water entrance docking backflow arm B28 of described purge tank 2, equipped with pneumatic diaphragm valve F10 on backflow arm B28;Institute
The other end stating backflow arm A27 and backflow arm B28 is connected, and connects liquid dispensing device 3 by return main 29, in backflow
Equipped with reflux pump 30 and pneumatic diaphragm valve F11 and conductivity sensor CC2 on supervisor 29, and return main 29 connects blow-off pipe
C31, equipped with pneumatic diaphragm valve F12 on blow-off pipe C31;Described blow-off pipe A10, blow-off pipe B12, blow-off pipe C31 and delivery pump
15 are all connected with blowdown supervisor 32 with the blow-off pipe on reflux pump 30, wherein equipped with pneumatic diaphragm valve on the blow-off pipe of delivery pump 15
F13, equipped with pneumatic diaphragm valve F14 on the blow-off pipe of reflux pump 30;
Equipped with liquid level sensor LC1 and temperature sensor TC1 on water storing tank 1, equipped with liquid level sensor on purge tank 2
LC2 and temperature sensor TC2, equipped with conductivity sensor CC1, pressure transducer PC1 and temperature sensor on tube for transfusion 14
TC3, liquid level sensor LC1~LC2, temperature sensor TC1~TC3, conductivity sensor CC1 and pressure transducer PC1 are respectively
Communication connects PLC 25, and PLC 25 communication connects touch screen 26, and realizes delivery pump 15, dosing pump 24 and return
The start and stop of stream pump 30 and the real-time control of the on off state of air relief valve P1, pneumatic stopping valve T1 and pneumatic diaphragm valve F1~F14.
Thermometer 39 it is respectively arranged with on water storing tank 1 described in the present embodiment and purge tank 2, and at water storing tank 1 and purge tank 2
Outer wall is provided with heat-insulation layer 40.
Equipped with heat exchanger 33 on tube for transfusion 14 described in the present embodiment;The arrival end of the heat exchanger tube of heat exchanger 33 passes through pipeline
Connect industrial steam generating means 34, and equipped with pneumatic stopping valve T2 on pipeline, the on off state of pneumatic stopping valve T2 is by PLC
Controller 25 controls in real time;Equipped with steam trap on the pipeline that pneumatic stopping valve T2 docks with the port of export of the heat exchanger tube of heat exchanger 33
35。
The injection water entrance 8 of water storing tank 1 described in the present embodiment connects injection water generating means 36 by pipeline, and at note
Equipped with pneumatic diaphragm valve F15 on the pipeline of jetting entrance side;The purified water entrance 4 of described water storing tank 1 and purge tank 2 is all by pipe
Road connects purified water generating means 37, and equipped with pneumatic diaphragm valve F16 on the pipeline of the purified water entrance side of water storing tank 1,
Equipped with pneumatic diaphragm valve F17 on the pipeline of the purified water entrance side of purge tank 2;The air vent of described water storing tank 1 and purge tank 2 is equal
Equipped with exhaust gas filter 38;The on off state of described pneumatic diaphragm valve F15, F16, F17 is controlled in real time by PLC 25.
When purging system is when being carried out paste medicine residual on tank skin, and the cleaning of employing is as follows: pure
Change water rinse blow remaining scale liquid circulation flushing blow the secondarily purified water of remaining liquid rinse blow remaining water injection water rinse
The remaining water hot-air dry of punching.
When being purified water and rinsing, first pneumatic diaphragm valve F16 opens, and purified water generating means passes through pipeline to water storage
Tank 1 injects a certain amount of purified water;Then, pneumatic diaphragm valve F3, F6, F11, F9 open, delivery pump 15 and reflux pump simultaneously
30 startup optimization, are rinsed liquid dispensing device constituting circle irrigation system, then during this in heat exchanger tube of heat exchanger 33
Being passed through industrial steam to heat the purified water for rinsing, after once flushing completes, pneumatic diaphragm valve F12 opens, will
Cleanout fluid is discharged from blow-off pipe C31, and then pneumatic diaphragm valve F2 opens, and the residual solution in water storing tank 1 is arranged from blow-off pipe A10
Go out, prepare for rinsing next time.
When carrying out alkali liquor circulation flushing, then before this, first configure certain density alkali liquor: pneumatic diaphragm valve F7 opens,
Dosing pump 24 startup optimization injects alkali liquor in purge tank 2, and pneumatic diaphragm valve F17 opens, and purified water generating means passes through pipeline
Injecting purified water in purge tank 2, pneumatic diaphragm valve F5, F8 opens simultaneously simultaneously, delivery pump 15 and heat exchanger 33 startup optimization,
To constitute alkali liquor automatic configuration system, by the conductivity sensor CC1, pressure transducer PC1 and the temperature sensor TC3 that arrange
The detection concentration of configured alkali liquor, hydraulic pressure and temperature in real time, when indices reaches requirement, alkali liquor automatic configuration system stops
Run;
Then, then start liquid dispensing device is carried out alkali liquor circulation flushing: pneumatic diaphragm valve F5, F6, F11, F10 open, with
Time delivery pump 15 and reflux pump 30 startup optimization, liquid dispensing device is carried out alkali cleaning, then this mistake constituting alkali liquor circle irrigation system
In journey, heat exchanger 33 remains on and heats the alkali liquor in conveying, when alkali liquor circulation flushing completes, and pneumatic diaphragm valve F12
Opening, discharged from blow-off pipe C31 by cleanout fluid, then pneumatic diaphragm valve F4 opens, and the residual solution in purge tank 2 is from blow-off pipe
B12 discharges.
When carrying out injection water and rinsing, first pneumatic diaphragm valve F15 opens, injection water generating means 36 by pipeline first to
Water storing tank 1 injects a certain amount of purified water;Then, pneumatic diaphragm valve F3, F6, F11, F12 open, simultaneously delivery pump 15 with return
Stream pump 30 startup optimization, to constitute injection water flushing line system, is rinsed liquid dispensing device, then heat exchanger 33 during this
Running work and the injection water in pipeline carries out heat treated, the cleanout fluid after flushing is discharged from blow-off pipe C31, the most pneumatic
Diaphragm valve F2 opens, and the residual solution in water storing tank 1 is discharged from blow-off pipe A10.
When carrying out blowing Yu Shuihuo and blowing remaining liquid, manually opened ball valve D1, D2 and check-valves S1, PLC 25 controls gas
Dynamic stop valve T1 opens with pneumatic diaphragm valve F1, F11, F12, and detect according to Pressure gauge A18 and Pressure gauge B19 in real time
Atmospheric pressure value controls the aperture of air relief valve P1, and blowing plant 16 is passed through compressed air in appendix 17, and realizes dosing
Remaining water in device and respective line thereof or the purging of remaining liquid.
When carrying out hot-air dry, open the electric heater 20 being arranged on pipeline purging system, in appendix 17
The compressed air of conveying heats, and then reaches purpose withering to liquid dispensing device and respective line thereof.
Claims (5)
1. a CIP on-line cleaning system, includes water storing tank and purge tank, and is furnished with pipeline purging system, and pipeline purging is
Unite external equipment to be cleaned, water storing tank and purge tank are equipped with purified water entrance, recirculated water entrance, air vent and blowdown
Mouthful, and on water storing tank, it is additionally provided with injection water entrance, and purge tank is additionally provided with alkali liquor inlet, the sewage draining exit of water storing tank is to being connected to
Blow-off pipe A and water-supply-pipe, the sewage draining exit of purge tank to being connected to blow-off pipe B and defeated alkali liquor pipe, another of water-supply-pipe and defeated alkali liquor pipe
End is connected, and by tube for transfusion connecting line purging system, equipped with delivery pump on tube for transfusion, it is characterized in that: described pipeline
Purging system includes blowing plant and appendix, on appendix equipped with Pressure gauge, electric heater and air filter with
And some hand control valves and Pneumatic/electric control valve;The alkali liquor inlet of described purge tank is by the liquid distribution pipe docked and alkali liquor
Circulation pipe is connected respectively the tube for transfusion of dosing pump and delivery pump discharge end;Described blow-off pipe A, water-supply-pipe, blow-off pipe B, defeated
It is respectively provided with Pneumatic/electric control valve on alkali liquor pipe, tube for transfusion, liquid distribution pipe and alkali liquor circulation pipe;Equipped with liquid level on water storing tank
Sensor LC1 and temperature sensor TC1, equipped with liquid level sensor LC2 and temperature sensor TC2 on purge tank, at tube for transfusion
On equipped with conductivity sensor CC1, pressure transducer PC1 and temperature sensor TC3, liquid level sensor LC1~LC2, temperature pass
Sensor TC1~TC3, conductivity sensor CC1 and pressure transducer PC1 communication respectively connects PLC, and PLC is led to
News connect touch screen, and realize delivery pump and the start and stop of dosing pump and each Pneumatic/electric control valve on off state real-time
Control.
A kind of CIP on-line cleaning system the most according to claim 1, is characterized in that: on described water storing tank and purge tank all
Equipped with thermometer, and it is provided with heat-insulation layer on the outer wall of water storing tank and purge tank.
A kind of CIP on-line cleaning system the most according to claim 1, is characterized in that: equipped with heat exchanger on described tube for transfusion;
The arrival end of the heat exchanger tube of heat exchanger connects industrial steam generating means by pipeline, and equipped with Pneumatic/electric control on pipeline
Valve processed, and its on off state is controlled in real time by PLC;Equipped with dredging on the pipeline of the port of export docking of the heat exchanger tube of heat exchanger
Hydrophone.
A kind of CIP on-line cleaning system the most according to claim 1, is characterized in that: the recirculated water entrance of described water storing tank
Docking backflow arm A, the recirculated water entrance docking backflow arm B of purge tank, the other end of backflow arm A, B is connected, and leads to
Cross return main and connect equipment to be cleaned, equipped with reflux pump and conductivity sensor CC2 on return main, and peripheral hardware blowdown
Pipe C;Described blow-off pipe A, B, C and delivery pump and the blow-off pipe on reflux pump are all connected with blowdown supervisor, and at backflow arm A, return
Stream arm B, return main, blow-off pipe C and delivery pump are respectively arranged with Pneumatic/electric control valve, institute on the blow-off pipe on reflux pump
Stating conductivity sensor CC2 communication and connect PLC, PLC realizes the start and stop to reflux pump and backflow arm A, returns
Stream arm B, return main, blow-off pipe C and delivery pump are opened with each Pneumatic/electric control valve on the blow-off pipe on reflux pump
The real-time control of off status.
5., according to a kind of CIP on-line cleaning system described in claim 1 or 2 or 3 or 4, it is characterized in that: the note of described water storing tank
Jetting entrance connects injection water generating means by pipeline;The purified water entrance of described water storing tank and purge tank is all by pipeline even
Connect purified water generating means;The air vent of described water storing tank and purge tank is respectively arranged with exhaust gas filter;At injection water entrance side
On pipeline and water storing tank and purge tank purified water entrance side pipeline on be respectively arranged with Pneumatic/electric control valve, and by PLC control
Device controls its on off state in real time.
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CN201620612307.1U CN205762817U (en) | 2016-06-21 | 2016-06-21 | A kind of CIP on-line cleaning system |
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CN201620612307.1U CN205762817U (en) | 2016-06-21 | 2016-06-21 | A kind of CIP on-line cleaning system |
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Cited By (6)
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CN106881029A (en) * | 2017-03-10 | 2017-06-23 | 大连大特气体有限公司 | Manual-automatic integral gaseous mixture configures system |
CN107297350A (en) * | 2017-08-09 | 2017-10-27 | 上海电气燃气轮机有限公司 | The leaf cleaning system of gas turbine blower |
CN108097657A (en) * | 2017-12-22 | 2018-06-01 | 江苏信息职业技术学院 | A kind of CIP cleaning devices and cleaning method |
CN109365442A (en) * | 2018-10-09 | 2019-02-22 | 广州铖兴进出口贸易有限公司 | Utilize the clean system of clean steam low consumption and its technique |
CN110327801A (en) * | 2019-08-08 | 2019-10-15 | 上海青赛生物科技有限公司 | A kind of station CIP is automatic to mend alkali system and its alkali supplement method |
CN110614249A (en) * | 2019-09-24 | 2019-12-27 | 华润三九(雅安)药业有限公司 | Online cleaning method for traditional Chinese medicine production equipment |
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2016
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106881029A (en) * | 2017-03-10 | 2017-06-23 | 大连大特气体有限公司 | Manual-automatic integral gaseous mixture configures system |
CN106881029B (en) * | 2017-03-10 | 2022-10-18 | 大连大特气体有限公司 | Manual-automatic integrated mixed gas configuration system |
CN107297350A (en) * | 2017-08-09 | 2017-10-27 | 上海电气燃气轮机有限公司 | The leaf cleaning system of gas turbine blower |
CN108097657A (en) * | 2017-12-22 | 2018-06-01 | 江苏信息职业技术学院 | A kind of CIP cleaning devices and cleaning method |
CN108097657B (en) * | 2017-12-22 | 2023-12-26 | 江苏信息职业技术学院 | CIP cleaning device and cleaning method |
CN109365442A (en) * | 2018-10-09 | 2019-02-22 | 广州铖兴进出口贸易有限公司 | Utilize the clean system of clean steam low consumption and its technique |
CN110327801A (en) * | 2019-08-08 | 2019-10-15 | 上海青赛生物科技有限公司 | A kind of station CIP is automatic to mend alkali system and its alkali supplement method |
CN110327801B (en) * | 2019-08-08 | 2021-09-03 | 上海青赛生物科技有限公司 | Automatic alkali supplementing system and method for CIP station |
CN110614249A (en) * | 2019-09-24 | 2019-12-27 | 华润三九(雅安)药业有限公司 | Online cleaning method for traditional Chinese medicine production equipment |
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