CN201762083U - Small-capacity injection material conveying system - Google Patents
Small-capacity injection material conveying system Download PDFInfo
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- CN201762083U CN201762083U CN2010205043922U CN201020504392U CN201762083U CN 201762083 U CN201762083 U CN 201762083U CN 2010205043922 U CN2010205043922 U CN 2010205043922U CN 201020504392 U CN201020504392 U CN 201020504392U CN 201762083 U CN201762083 U CN 201762083U
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Abstract
The utility model relates to a small-capacity injection material conveying system comprising a thick mixing tank, a thin mixing tank, a filter and respirators, wherein the respirators are respectively positioned at the tops of the thick mixing tank and the thin mixing tank; the tank bottom of the thick mixing tank and/or thin mixing tank are/is provided with a waste water discharge port or a discharge channel; the waste water discharge port or the discharge channel is provided with an electric conductivity meter for testing the electric conductivity of discharged waste water; and alternatively, each of the respirators is provided with a disinfection hydrophobic filter with the function of electric heating. The small-capacity injection material conveying system tests the electric conductivity of liquid discharged through the electric conductivity meter arranged at the waste liquid discharge channel or the discharge port, thus making judgment of cleaning effect, and being beneficial to on-line cleaning; and the accident hidden troubles can be greatly reduced through the electric heating type respirators.
Description
Technical field
The utility model relates to a kind of material pipe delivery system of small-volume injection in the pharmaceutical industry, this pipe-line transportation system specifically be used for realizing soup be delivered to the bottle placer encapsulation as before the finished product the sequence of operations such as stirring, dilution of process.
Background technology
The principle of work of small-capacity injection material transport system mainly is that bulk drug is entered dense preparing tank by charge door, and adding injection water dilution, through after the magnetic stirrer soup is delivered to dilute preparing tank by health level water pump, and add corresponding injection water and finish accurate dosing process by Weighing module, and feed liquid is delivered to bottle placer encapsulation by sterilizing filter, become a delivery system of finished product.
In the existing small-capacity injection material transport system, general to adopt 1 filtering accuracy be 0.45 μ m and 2 filter series connection that filtering accuracy is 0.22 μ m to dilute preparing tank to the bottle placer filter, and material is about to feed liquid after by these two filters and is delivered to bottle placer.Simultaneously also be provided with respirator at tank deck, the main effect of respirator is to make air and external air pressure balance in the jar in pharmaceutical industry, and outside air is carried out aseptic filtration, be unlikely to make jar internal pressure excessive or too small, cause tank body blast or flatly fall; But because delivery system need use pure steam when sterilization or cleaning, and pure steam is easy to generate condensed water, and the condensed water that is produced can stop up the filter core in the respirator, thereby causes intrasystem pressure change to cause potential safety hazard.
Along with the development of current medical technology, the checking for material system among the new edition GMP is also more and more stricter simultaneously, and this cleaning and sterilization comprising equipment, pipe section is verified, and required also more and more stricter for the filter of material-transporting system.For example require among the new edition GMP: sterilising temp need be controlled at and be not less than 121 ℃, sterilization time 〉=30min; And traditional small-volume injection delivery system can't be carried out on-line monitoring to temperature and water quality, and then has influenced its serviceability and work efficiency.
Summary of the invention
Technical problem to be solved in the utility model is to provide a kind of small-capacity injection material transport system of performance safety, and its technical matters to be solved can be implemented by the following technical programs.
A kind of small-capacity injection material transport system, comprise dense preparing tank, dilute preparing tank, filter and lay respectively at dense preparing tank and the respirator of dilute preparing tank tank deck, the jar end of described dense preparing tank and/or dilute preparing tank, be provided with discharge of wastewater mouth or discharge-channel, and described discharge of wastewater mouth or discharge-channel place are provided with the conductivity meter that is used for testing institute's waste discharge conductivity.
As the further improvement of the technical program, described respirator is the electrical heating type filter that has electric heating function.
As the further improvement of the technical program, described respirator can be the degerming hydrophobic filter.
Wherein, the filtering accuracy of described degerming hydrophobic filter can be 0.22 μ m.
In addition, be provided with discharge of wastewater mouth (or discharge of wastewater passage) and condensed water discharge-channel at the bottom of described dense preparing tank jar, described discharge of wastewater mouth (or discharge of wastewater passage) and/or condensed water discharge-channel place can be provided with the temperature sensor that is used for testing online pure steam sterilizing (SIP) thermometry.
Equally, be provided with discharge of wastewater mouth or discharge-channel at the bottom of described dilute preparing tank jar, described discharge of wastewater mouth or discharge-channel place can be provided with the temperature sensor that is used for testing institute's waste discharge temperature.
Also as the further improvement of the technical program, described filter can comprise that filtering accuracy is that the decarburization filter of 3 μ m, the filter that filtering accuracy is 1 μ m, filter and the filtering accuracy that filtering accuracy is 0.45 μ m are the sterilizing filter of 0.22 μ m.
As the further improvement of the technical program, described filtering accuracy is that the sterilizing filter of 0.22 μ m has two.
As the further improvement of the technical program, be provided with water for injection water entry and purified water water entry again at described dense preparing tank tank deck; Described water for injection water entry and purified water water entry be equipped with at least one by the set spray ball of dense preparing tank tank deck with described water for injection or/and purified water is sent into the liquor charging passage in the dense preparing tank jar, and also be equipped with at least one not by described spray ball with described water for injection or/and purified water is sent into the liquor charging passage in the dense preparing tank jar.
In like manner, be provided with water for injection water entry and purified water water entry at described dilute preparing tank tank deck; Described water for injection water entry and purified water water entry be equipped with at least one by the set spray ball of dilute preparing tank tank deck with described water for injection or/and purified water is sent into the liquor charging passage in the dilute preparing tank jar, and also be equipped with at least one not by described spray ball with described water for injection or/and purified water is sent into the liquor charging passage in the dilute preparing tank jar.
Adopt the small-capacity injection material transport system of technique scheme, can reduce accident potential greatly by adopting the electrical heating type respirator.And can measure the conductivity value of the liquid that discharged, and then cleaning performance is judged by conductivity instrument is set at discharging of waste liquid passage or discharge side.Help realizing on-line cleaning.
Description of drawings
Below in conjunction with accompanying drawing the specific embodiment of the present utility model being done one describes in detail.
Fig. 1 is integral structure of the present utility model and schematic flow sheet;
Fig. 2 a is the enlarged diagram at A frame place among Fig. 1;
Fig. 2 b is the enlarged diagram at B frame place among Fig. 1;
Fig. 2 c is the enlarged diagram at C frame place among Fig. 1;
Fig. 2 d is the enlarged diagram at D frame place among Fig. 1.
Among the figure each label the theing contents are as follows of corresponding or expression:
V1001, V1002, V1003, V1004, V1005, V1007, V1008, V1009, V1014, V1015, V1016, V1017, V1018, V1019, V1020, V1022, V1023, V1024, V1025, V1028, V1030, V1031, V1032, V1033, V1034, V1035, V1036, V1037, V1038, V1039, V1040, V1041, V1042, V1044, V1045, V1046, V1047, V1050, V1051, V1053, V1054, V1055, V1056, V1057, V1058, V1059, V1060, V1061, V1064, V1066, V1067, V1068, V1071, V1072, V1073, V1074, V1075, V1076, V1078, V1079, V1080, V1083, V1085, V1086, V1087, V1088, V1089, V1090, V1091, V1092, V1093, V1094, V1095, V1096, V1097, V1101, V1103, V1106, V1107, V1111, V1113, V1114, V1115, V1116, V1117, V1118---valve
V1006, V1013, V1043, V1048, V1052, V1062, V1065, V1098, V1112---sample valve
V1010, V1021, V1069, V1077---drain valve
V1011, V1012, V1027, V1029, V1063, V1070, V1082, V1084---percentum control cock
V1026---safety valve
V1049, V1100, V1102, V1105, V1108, V1110---discharge side
V1081---blowdown valve
V1099, V1104, V1109---integrity test mouth
E101, E102---electro heat respirator
F101---3 μ m decarburization filter F 102---1 μ m filter F 103---0.45 μ m filter F 104, F105---, 0.22 μ m sterilizing filter
I101, I103, I105, I108, I109, I115, I117, I120, I121, I122, I129---temperature sensor
I102, I106, I112, I113, I119, I125, I126, I127, I128---compression indicator
I104, I111, I116, I118, I124---pressure sensor
I107---pressure type level sensor
I110, I114, I123, I130---conductivity meter
P101, P102---material-handling pump
R101---100L dense preparing tank R102---250L dilute preparing tank
101,102---pure steam inlet
111,113---purified water water inlet 112,114---purified water water outlet
121,123---water for injection water inlet 122,124---water for injection water outlet
131,132---nitrogen free air diffuser 133,134---nitrogen admission port
141,143,145,147---cooling water intake 142,144,146,148---cooling water outlet
151,152,153,154,155---the condensed water water outlet
161,162,163---wastewater effluent mouth 166,167,168,169---discharge side
171,172---the industrial steam admission port
181,182---the integrity tester interface
191---go bottle placer to connect the position
201,202---heat exchanger
211,212---pressure regulating valve
221,222---filter
231,232---the rupture disk position
241,242---visor lamp position
251,252,253---the spray ball
261,262---weigh a little
The specific embodiment
Small-capacity injection material transport system as depicted in figs. 1 and 2, system forms and mainly comprises: 100L dense preparing tank R101,250L dilute preparing tank R102(tank body volume can be determined according to the needs of each various processes), material-handling pump P101 and P102, filtering accuracy is the decarburization filter F 101 of 3 μ m, filtering accuracy is the filter F 102 of 1 μ m, filtering accuracy is the filter F 103 of 0.45 μ m, filtering accuracy is sterilizing filter F104 and the F105 of 0.22 μ m, and jar last each accessory, wherein accessory comprises respirator, the diaphragm valve of safety valve and various sizes, ball valve, drain valve and pipe fitting etc. (the concrete indication of the related accessory that is indicated among the figure sees in the description of drawings enumerating of corresponding component title behind each label for details).
Small-volume injection delivery system dense preparing tank R101 tank deck of the present utility model is furnished with water for injection (comprising water for injection water inlet 121 and water for injection water outlet 122) and purified water interface (comprising purified water water inlet 111 and purified water water outlet 112) inserts tank deck spray ball 251 jointly, increasing a pipeline does not in addition more directly enter in the jar by tank deck spray ball 251, in the blending process of routine, the operation that sprays by abhiseca is can be satisfactory.But in emerging field of biological pharmacy, some special material is very strict for the proportioning process conditional request, if (injection water directly enters by spray when promptly preparing burden to adopt conventional way, directly do not enter in the jar and increase inlet in addition), then in blending process, cause foam easily, be not easy to mass transport, feed liquid is splashed, for these materials, this may cause that material characteristic changes.This point can determine whether needs according to concrete pharmaceutical field.
Same also is equipped with similar injection water and purified water interface at dilute preparing tank R102 tank deck.
The utility model discharge side at the bottom of jar increases the real-time monitoring that temp probe and conductivity probe are realized temperature and water quality conductive, it is common respirator that the respirator of tank deck adopts what adopt in electrical heating type respirator E101 and the E102(conventional delivery systems respectively), the main effect of respirator is in pharmaceutical industry, because strictness control requirement to bacterium, and make total system can not be subjected to the pollution of bacterium in the outside air, thereby the technical program is selected one 0.22 μ m degerming hydrophobic filter respectively to be set as above-mentioned respirator respectively on the material-compound tank top of dense preparing tank and dilute preparing tank, in fact the respirator here is exactly a filter, it promptly is hydrophobic filter, it also is degerming level filter, also has heating function simultaneously, it can pass through gas, and liquid cannot pass through, and it mainly acts on exactly and keeps a jar inside and outside air pressure balance by the respirator that adopts electrical heating type.And owing to can produce condensed water in the process of tank body or pipeline being carried out the online sterilization of pure steam (SIP), partial condensation water can accumulate in the respirator top, causes clogging of filter element; For anti-problem here, then increased electric heating function, make condensate evaporation, thereby prevent that condensed water from stopping up filter core.It is not only bringing into play electric heating function, normally not have under the situation of sterilizing, and it is also serving as and filters atmosphere, keeps jar effect of inside and outside barometric pressure balance.
The main purpose of respirator is to make jar interior air and external air pressure balance, be unlikely to make jar internal pressure excessive or too small, cause jar blast or flatly fall, and the air in entering jar during by this respirator air reached the purpose of degerming, can not have any pollution to soup.
The utility model has increased a heating function in traditional respirator, main purpose need use pure steam when just being online sterilization, and pure steam is easy to generate condensed water, and condensed water can stop up the filter core in the respirator, so need to adopt the mode of heating this moment, add hot filter, make condensate evaporation, be unlikely to cause clogging of filter element.
Before the batching of carrying out each time batch, at first to clean completely and sterilize the feed liquid of last consignment of time.
Cleaning process is as follows:
Open V1003 and V1012 valve, wherein the V1003 valve is a common manual SUS316L diaphragm valve, and V1012 is pneumatic percentum control cock; Mainly the acting as of pneumatic percentum control cock be used for the preparing burden accuracy control of consumption of water, and can reach the purpose of Long-distance Control, after having opened these two valves, enter tank body by spray ball 251 and can reach the effect of washing tank body for the first time and passing through material-handling pump pipe blow-through pipe fitting; During cleaning, bottom valve V1034 and V1040, V1042, V1025, V1045, V1046, V1051, V1053, these valves of V1054 are all opened, after realizing self-loopa, open vent valves V1035, V1039 at the bottom of the material-compound tank of dense preparing tank R101, V1041, the conductivity meter I110 that be installed in discharge of wastewater porthole, dense preparing tank bottom this moment just can detect discharging water quality, by conductivity meter conductivity value is changed into the 4-20mA analog quantity and is sent to bonded assembly PLC system of institute further to make follow-up judgement and operating order; In medical system, verify that if desired pipeline and tank body have cleaned cleaning, then need conductivity meter to detect, thereby reach the needed data of cleaning checking by the record of conductivity value.
Clean for the second time and then open the water for injection valve, opening pure steam valve V1004 earlier sterilizes earlier to the pipeline below the V1005, because pipeline a period of time need not, in order to prevent long bacterium in the heat exchanger, then before entering the R101 material-compound tank, use pure steam sterilizing, the purpose of opening valve V1009 and drain valve V1010 simultaneously is for the condensed water of draining, sterilization time continues after 30 seconds, open water for injection valve V1005, V1011(percentum control cock) is ejected into the tank body various piece uniformly by spray ball 251, and then open bottom valve V1034, V1044, V1042, V1045, V1046, V1051, V1053, V0154, wash cycles for several times, at last by vent valves V1035 at the bottom of opening jar, blowoff valve V1041 at the bottom of V1039 and the pump, the water quality after cleaning by conductivity meter I110 mensuration again.Conductivity meter changes into the 4-20mA analog quantity with conductivity value and is sent to the PLC system.These data then can be used as cleans indispensable significant data in the checking.
In like manner the cleaning for dilute preparing tank R102 can adopt same control step, but in the general cleaning below the V1055 one section flexible pipe be one and clean cecum; As shown in the figure, equally, open valve V1064, V1068 earlier, pipeline is carried out pure steam sterilizing after 30 seconds, close V1064, V1068 valve, open V1057, V1055, V1056, V1070, close V1053, V1054, injection water then can reach the purpose of cleaning a segment pipe below the V1055 by valve V1057, V1056, V1055, at the bottom of rinse water is disposed to jar, measures the purpose that can reach the cleaning checking equally by conductivity meter I123 again.Dilute preparing tank R102 rear end pipeline adopts can carry out the on-line cleaning process with quadrat method, but because bottle placer is placed as the B level zone in the clean room of pharmaceutical factory, (B level zone is at dynamic ten thousand grades, static hundred grades of clean areas, and press the 14 regulation of 98 editions GMP standards of SDA, the air purity in pharmaceutical production clean room (district) is divided into four ranks, hundred grades of clean rooms are defined as: must not be more than 3500 in the cubic meter clean room greater than the grit number of 0.5 μ m, and must not be greater than the grit number of 5 μ m greater than 0; Ten thousand grades of clean rooms are defined as: the grit number greater than 0.5 μ m in the cubic meter clean room must not be more than 350000.Grit number greater than 5 μ m must not be more than 2000, and 100,000 grades of clean rooms are defined as: must not be more than 3500000 in the cubic meter clean room greater than the grit of 0.5 μ m, and must not be greater than the grit of 5 μ m more than 20000.) because B level zone is not allow floor drain, so when carrying out that valve V1113 rear end is cleaned and sterilizing, need connection hose will clean waste water and condensed water is disposed to the dilute preparing tank zone.
Cleaning later then is the online sterilization process of pure steam (SIP), and the SIP process comprises the sterilization to jar, tank deck respirator and total system pipeline valve filter.At first tank body is sterilized, open dense preparing tank (R101) valve V1002 by jar at the bottom of the set temperature sensor I108 of discharge side monitor (wherein the discharge-channel at the bottom of the dense preparing tank R101 jar is provided with condensed water water outlet 151 and wastewater effluent mouth 161), because the set point of sensor I108 of discharge side is the cold spot of temperature at the bottom of being positioned at jar, therefore just can pick up counting when temperature build-up to 121 ℃ or when above and sterilize, sterilization time is 30min, then can reach the purpose of online sterilization, open V1036 during sterilization simultaneously, V1037, the V1038 valve is discharged condensed water.Open V1042, V1045, V1040, V1051, V1053, V1054 simultaneously, in sterilization process, can produce a large amount of condensed waters, comprise on the respirator and also can produce condensed water, at this moment as long as adopt the respirator of electrical heating type, with the filter core heating, condensate evaporation can prevent that then condensed water from stopping up filter core and causing respirator to lose efficacy; On discharge-channel at the bottom of the jar, also be provided with temperature sensor I109 equally.
In like manner the sterilization process of dilute preparing tank is also with the sterilization process unanimity of dense preparing tank, the discharge-channel of holding under the dilute preparing tank R102 jar is provided with condensed water water outlet 152 and wastewater effluent mouth 162, also is provided with the temperature sensor I121 and the I122 that are used for testing online pure steam sterilizing thermometry on discharge-channel.
I110, I114, I123, I130 are conductivity meter among the figure, are used to monitor the conductivity value of water for cleaning, through to the mensuration of conductivity value, then can draw cleaning and verify actv. numerical value.
E101, E102 are the electrothermic type respirator among the figure, compare with traditional respirator, have increased heating function, the heating of the respirator inner filter core that passes through, make the time, make attached to the condensed water on the filter core and be able to heating evaporation, thereby prevent clogging of filter element and cause the tank body explosion or flatly fall the SIP of system.
I101, I103, I105, I108, I109, I115, I117, I120, I121, I122, I129 are temperature sensor among the figure, are used for monitoring and acquisition system temperature conditions everywhere, with decision sterilization control and the related data collection of run up time.
In addition, but the cooresponding big arrow indication in corresponding label place in the trend reference diagram of each gas and liquid among the figure, for example: to be 145 cooling water intake enter pipeline along the sensing of right side arrow among the figure to number in the figure, and number in the figure is 153 the condensed water water outlet sensing discharge line along the left side arrow; Be that the arrow of 101 pure steam inlet lower end indicates the path that pure steam enters system pipeline also as number in the figure; Be the water outlet position that the arrow of 112 purified water water outlet upper end indicates purified water also as label, and the water inlet direction of label to be 111 purified water water inlet lower end arrow represent purified water.The sign of other parts also is similar.
The utility model reaches the purpose of multistage degerming by increase by the sterilizing filter of one 0.22 μ m again on the basis of existing system, thereby more can guarantee the quality of soup.
The relative prior art of the utility model is discharge side increase conductivity probe and temp probe at the bottom of jar also, conductivity value is converted into 4-20 milliampere analog signals, be sent to and carry out data logging and storage in the PLC system, after a batch of production finishes for soup, when pipe blow-through and equipment and to the SIP of system (online sterilization), can on-line monitoring conductivity value and temperature value, reach the data that need in cleaning checking and the sterilization checking.Do not reach the needed data of checking and in traditional cleaning checking and sterilization process, have these two kinds of on-line monitoring instrument, because conductivity can be monitored the water quality after cleaning, and in GMP requires, sterilising temp then needs to be controlled at and is not less than 121 ℃, sterilization time needs 〉=30min, can know then that when temperature sensor being placed on discharge side and minimum temperature point position the minimum temperature point reaches 121 ℃ interdependent node, and then the sterilization that picks up counting; Related data can be indexed in cleaning and the sterilization authenticating documents thus.
The utility model has solved in traditional small-volume injection delivery system the deficiency that can't carry out on-line monitoring to temperature and water quality; And this system can also realize automatic on-line SIP, and the automatic on-line cleaning process.System has realized the monitoring to temperature and institute's discharge liquid conductivity, thereby and prevents that by the respirator heating function condensed water from stopping up fluid reservoir tank deck respirator and making the tank body explosion or flatly fall.
Claims (10)
1. small-capacity injection material transport system, comprise dense preparing tank, dilute preparing tank, filter and lay respectively at dense preparing tank and the respirator of dilute preparing tank tank deck, it is characterized in that, the jar end of described dense preparing tank and/or dilute preparing tank, be provided with discharge of wastewater mouth or discharge-channel, and described discharge of wastewater mouth or discharge-channel place are provided with the conductivity meter that is used for testing institute's waste discharge conductivity.
2. small-capacity injection material transport system according to claim 1 is characterized in that, described respirator is the electrical heating type respirator.
3. small-capacity injection material transport system according to claim 1 and 2 is characterized in that, described respirator is the degerming hydrophobic filter.
4. small-capacity injection material transport system according to claim 3 is characterized in that, the filtering accuracy of described degerming hydrophobic filter is 0.22 μ m.
5. small-capacity injection material transport system according to claim 1, it is characterized in that, be provided with discharge of wastewater mouth/discharge-channel and condensation water channel at the bottom of the described dense preparing tank jar, described discharge of wastewater mouth/discharge-channel and/or condensation water channel place are provided with the temperature sensor that is used for testing online pure steam sterilizing thermometry.
6. small-capacity injection material transport system according to claim 1, it is characterized in that, be provided with discharge of wastewater mouth/discharge-channel and condensation water channel at the bottom of the described dilute preparing tank jar, described discharge of wastewater mouth/discharge-channel and/or condensation water channel place are provided with the temperature sensor that is used for testing online pure steam sterilizing thermometry.
7. small-capacity injection material transport system according to claim 1, it is characterized in that described filter comprises that filtering accuracy is that the decarburization filter of 3 μ m, the filter that filtering accuracy is 1 μ m, filter and the filtering accuracy that filtering accuracy is 0.45 μ m are the sterilizing filter of 0.22 μ m.
8. small-capacity injection material transport system according to claim 7 is characterized in that, described filtering accuracy is that the sterilizing filter of 0.22 μ m has two.
9. small-capacity injection material transport system according to claim 1 is characterized in that, described dense preparing tank tank deck is provided with water for injection water entry and purified water water entry; Described water for injection water entry and purified water water entry be equipped with at least one by the set spray ball of dense preparing tank tank deck with described water for injection or/and purified water is sent into the liquor charging passage in the dense preparing tank jar, and also be equipped with at least one not by described spray ball with described water for injection or/and purified water is sent into the liquor charging passage in the dense preparing tank jar.
10. small-capacity injection material transport system according to claim 1 is characterized in that, described dilute preparing tank tank deck is provided with water for injection water entry and purified water water entry; Described water for injection water entry and purified water water entry be equipped with at least one by the set spray ball of dilute preparing tank tank deck with described water for injection or/and purified water is sent into the liquor charging passage in the dilute preparing tank jar, and also be equipped with at least one not by described spray ball with described water for injection or/and purified water is sent into the liquor charging passage in the dilute preparing tank jar.
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| CN2010205043922U CN201762083U (en) | 2010-08-26 | 2010-08-26 | Small-capacity injection material conveying system |
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| CN2010205043922U CN201762083U (en) | 2010-08-26 | 2010-08-26 | Small-capacity injection material conveying system |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101915362A (en) * | 2010-08-26 | 2010-12-15 | 上海创洁科技有限公司 | Small-capacity injection material transport 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 |
| 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 |
| CN107649060A (en) * | 2017-10-18 | 2018-02-02 | 嘉兴尚能光伏材料科技有限公司 | A kind of efficient automatic filling machine |
| CN117443251A (en) * | 2023-11-01 | 2024-01-26 | 安徽宏业药业有限公司 | Production process of oxytocin injection and liquid preparation production system thereof |
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2010
- 2010-08-26 CN CN2010205043922U patent/CN201762083U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101915362A (en) * | 2010-08-26 | 2010-12-15 | 上海创洁科技有限公司 | Small-capacity injection material transport 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 |
| 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 |
| CN107649060A (en) * | 2017-10-18 | 2018-02-02 | 嘉兴尚能光伏材料科技有限公司 | A kind of efficient automatic filling machine |
| CN117443251A (en) * | 2023-11-01 | 2024-01-26 | 安徽宏业药业有限公司 | Production process of oxytocin injection and liquid preparation production system thereof |
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