CN205549646U - Medicinal alcohol distillation automatic control production system - Google Patents
Medicinal alcohol distillation automatic control production system Download PDFInfo
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- CN205549646U CN205549646U CN201620140624.8U CN201620140624U CN205549646U CN 205549646 U CN205549646 U CN 205549646U CN 201620140624 U CN201620140624 U CN 201620140624U CN 205549646 U CN205549646 U CN 205549646U
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Abstract
The utility model relates to a medicinal alcohol distillation automatic control production system, including rare alcohol storage device, alcohol distillation plant and qualified alcohol storage device three. Carry the gravity tank to keep in through a liquid pump the rare alcohol in rare alcohol storage tank, the gravity tank liquid level variation in according to the tower cauldron supply in real time, and alcohol distillation plant carries out air distillation, and the back is reachd to concentration, carries qualified alcohol storage tank to store after the cooling qualified alcohol. In whole production process, can look over the state that the valve was located in setting up present in real time and carry out real time control. The utility model discloses an automatic distillation control obtains high concentration alcohol to satisfy follow -up production requirement.
Description
Technical field
The utility model relates to alcohol distillation production field, particularly a kind of medicinal alcohol distillation automatic control production system.
Background technology
In prior art, obtaining alcohol in high concentration as raw material, needs by distillation using the Diluted Alcohol that Workshop Production reclaims, tradition alcohol still-process cannot realize Automated condtrol, it is impossible to meets subsequent production requirement.
Summary of the invention
In view of this, the purpose of this utility model is to provide a kind of medicinal alcohol distillation automatic control production system, obtains alcohol in high concentration, to meet subsequent production requirement by automation distillation.
The utility model uses below scheme to realize: a kind of medicinal alcohol distillation automatic control production system, including a Diluted Alcohol storage device, an alcohol distillation device and qualified alcohol storage device；
Described Diluted Alcohol storage device includes one first Diluted Alcohol storage tank and one second Diluted Alcohol storage tank；The inlet of the inlet of described first Diluted Alcohol storage tank and described second Diluted Alcohol storage tank all one end with a feed liquor main valve are connected, the liquid outlet of described first Diluted Alcohol storage tank and one end of one first Diluted Alcohol storage tank liquid valve are connected, the liquid outlet of described second Diluted Alcohol storage tank and one end of one second Diluted Alcohol storage tank liquid valve are connected, the other end of described first Diluted Alcohol storage tank liquid valve is all connected with one end of one first Diluted Alcohol transfer pump and one end of one second Diluted Alcohol transfer pump with the other end of described second Diluted Alcohol storage tank liquid valve, the inlet of the gravity tank that the other end of described first Diluted Alcohol transfer pump and the other end of the second Diluted Alcohol transfer pump are also arranged at a high position with is connected, a full level alarm switch and a low alarm switch it is provided with on the tank body of described gravity tank；The liquid outlet of described gravity tank and a gravity tank go out one end of liquid regulation valve and are connected；Described first Diluted Alcohol tank inside is provided with a liquid level gauge with the inside of one second Diluted Alcohol storage tank；
Described alcohol distillation device includes one in order to the destilling tower of alcohol distillation, one end of heating cylinder steam first air inlet of described destilling tower and destilling tower heating cylinder jacket steam regulation valve is connected, heating cylinder steam second air inlet of described destilling tower and one end of a destilling tower heating cylinder coil pipe steam control valve are connected, the heating cylinder of described destilling tower offers one and is connected in order to the liquid outlet of waste discharge alcohol, one end of the liquid outlet of described heating cylinder and waste discharge alcohol regulation valve；Described heating cylinder also vaporization chamber with described destilling tower is connected, described vaporization chamber top is communicated with the extension tower portion of described destilling tower, the lower openings in described extension tower portion goes out the other end of liquid regulation valve and is connected with described gravity tank, the upper opening in described extension tower portion and one end of a return valve are connected, and the other end of described return valve and one end of a qualified alcohol liquid valve are connected；The tower top opening extending tower portion of described destilling tower and a sheet frame condenser are connected, described sheet frame condenser offers a cooling water intake, one cold water intaking water return outlet and a condensation alcohol liquid outlet, one end of described cooling water intake and cooling circulating water water inlet main valve is connected, the inlet of described alcohol liquid outlet and a surge tank is connected, a liquid-level switch it is provided with on the tank body of described surge tank, the liquid outlet of described surge tank and one end of a reflow of alcohol pump are connected, the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
It is provided with a thermometer in the inside of described heating cylinder, the inside of described vaporization chamber, the inside of described tower top and the return main being connected with described cooling water water return outlet；It is provided with a pressure sensor in the jet chimney that first air inlet of the inside of described vaporization chamber and the heating cylinder of described destilling tower is connected with one end of described destilling tower heating cylinder jacket steam regulation valve；The inside of described vaporization chamber is additionally provided with a liquid level gauge；One it is provided with in order to detect the alcohol concentration meter of alcohol concentration and flow simultaneously in the pipeline that the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
Described qualified alcohol storage device includes one first qualified alcohol storage tank, one second qualified alcohol storage tank and a cooler, the other end of described qualified alcohol liquid valve is connected with one end of described cooler, one end of the other end of described cooler and one end of one first qualified alcohol storage tank liquid feed valve and one the two the first qualified alcohol storage tank liquid feed valve is connected, the other end of described first qualified alcohol storage tank liquid feed valve is connected with the inlet of described first qualified alcohol storage tank, the other end of one end of described second qualified alcohol storage tank liquid feed valve is connected with the inlet of described second qualified alcohol storage tank；The liquid outlet of described first qualified alcohol storage tank is all connected with a qualified alcohol Pump for giving-out with the liquid outlet of described second qualified alcohol storage tank；The inside of described first qualified alcohol storage tank is provided with a liquid level gauge with the inside of described second qualified alcohol storage tank.
In the utility model, alcohol distillation be using Workshop Production reclaim Diluted Alcohol as raw material, obtain alcohol in high concentration by distillation, to meet subsequent production requirement.Complete equipment includes Diluted Alcohol storage device, alcohol distillation device and qualified alcohol storage three parts of device.By Pump for giving-out, the Diluted Alcohol in Diluted Alcohol storage tank is transported to gravity tank keep in, gravity tank supplements in real time according to the liquid level change in tower reactor, alcohol distillation device carries out air-distillation, after concentration arrives, qualified alcohol is transported to after supercooling qualified alcohol storage tank and stores.In whole production process, can valve state in which controlling in real time in real time inspection current setting.
Especially, the using method of described medicinal alcohol distillation automatic control production system comprises the following steps:
I is standby
Stand-by state refers to that whole equipment does not produce, and equipment is only in stand-by state and just can produce.
II feed liquor
Unlatching equipment, equipment enters into feed liquor state.First by Diluted Alcohol storage tank to gravity tank feed liquor, until gravity tank high level；Then by gravity tank to tower reactor feed liquor, until tower reactor high level.During feed liquor, the liquid valve of two Diluted Alcohol storage tanks opens out liquid simultaneously, and selected Pump for giving-out starts running.In whole still-process, as long as tower reactor liquid level is less than setting working solution place value, gravity tank will be from trend tower reactor fluid infusion, until tower reactor high level.If the liquid level of gravity tank is reported to the police less than lower bound, Diluted Alcohol storage tank is just as gravity tank fluid infusion, until liquid level height is only limited to.
III heating
Tower reactor liquid level reaches work liquid level, begins to warm up, and cools down water water intaking valve and open.Heating cylinder temperature is less than setting operating temperature, and coil pipe steam valve is opened, and bottom temperature is less than setting operating temperature, and jacket steam valve is opened.The two steam valve is all regulation valve, and system can be automatically adjusted valve aperture according to set temperature value by PID, temperature be controlled near design temperature, it is ensured that stablizing of still-process.
IV refluxes/goes out liquid
Along with bottom temperature raises, the alcohol amount evaporated is gradually increased, when reaching surge tank high level, reflow of alcohol pump is opened, flowmeter detects in real time, and alcohol concentration reaches the qualified alcohol concentration set, and opens out qualified alcohol valve and qualified alcohol storage tank liquid feed valve.First select the first qualified alcohol storage tank feed liquor, if the first qualified alcohol storage tank arrives high level, automatically switch to the second qualified alcohol storage tank and continue feed liquor.If alcohol concentration not up to sets concentration value, open return valve, continue distillation.
V waste discharge alcohol/stopping heating
The basis for estimation of equipment aneroid: two Diluted Alcohol storage tanks and gravity tank aneroid simultaneously.The condition of waste discharge alcohol: the first, equipment state is in reflux state；The second, the waste discharge alcohol temperature value of tower top temperature, bottom temperature, heating cylinder temperature above correspondence.
When production status meets waste discharge alcohol condition, and equipment is judged as aneroid simultaneously, then system is first shut off steam valve, stops heating, start timing, after reaching to stop heat set points, open waste discharge alcohol valve, starting waste discharge alcohol, drained rear equipment state jumps to standby, and production terminates.
When production status meets waste discharge alcohol condition, but equipment also has Diluted Alcohol, at this moment stops feed liquor, steam off valve, opens waste discharge alcohol valve, drained after, restart feed liquor, heating, continue distillation.
When tower reactor liquid level is less than work liquid level, and equipment is judged as aneroid, then system steam off valve, stopping heating, start timing, and after reaching to stop heat set points, equipment redirects as standby, and production terminates.
Wherein, the amount of a waste discharge alcohol artificially can be revised according to actual conditions.
Compared with prior art, the utility model obtains alcohol in high concentration, to meet subsequent production requirement by automation distillation.
Accompanying drawing explanation
Fig. 1 is that Diluted Alcohol of the present utility model stores device schematic diagram.
Fig. 2 is alcohol distillation device schematic diagram of the present utility model
Fig. 3 is qualified alcohol storage device schematic diagram of the present utility model.
Label declaration: 1 regulates valve for heating cylinder jacket steam；2 is heating cylinder coil pipe steam control valve；3 regulate valve for waste discharge alcohol；4 go out liquid regulation valve for gravity tank；5 is the first Diluted Alcohol storage tank liquid valve；6 is the second Diluted Alcohol storage tank liquid valve；7 is return valve；8 is qualified alcohol liquid valve；9 is the first qualified alcohol storage tank liquid feed valve；10 is the second qualified alcohol storage tank liquid feed valve；11 is cooling circulating water water inlet main valve；12 is Diluted Alcohol storage tank feed liquor main valve；13 is the first Diluted Alcohol transfer pump；14 is the second Diluted Alcohol transfer pump；15 is reflow of alcohol pump；16 is qualified alcohol Pump for giving-out；17 is destilling tower heating cylinder；18 is destilling tower vaporization chamber；19 extend tower top for destilling tower；20 is CWR；21 is the jet chimney arranging pressure sensor；22 is the pressure sensor of vaporization chamber；23 is the first qualified alcohol storage tank；24 is the second qualified alcohol storage tank；25 is the first Diluted Alcohol storage tank；26 is the first Diluted Alcohol storage tank；27 is vaporization chamber liquid level gauge；28 switch for gravity tank full level alarm；29 switch for gravity tank low alarm；30 is surge tank liquid-level switch；31 is alcohol concentration meter.
Detailed description of the invention
Below in conjunction with the accompanying drawings and the utility model is described further by embodiment.
This enforcement provides a kind of medicinal alcohol distillation automatic control production system, including a Diluted Alcohol storage device, an alcohol distillation device and qualified alcohol storage device；
As it is shown in figure 1, described Diluted Alcohol storage device includes one first Diluted Alcohol storage tank 25 and one second Diluted Alcohol storage tank 26；The inlet of the inlet of described first Diluted Alcohol storage tank and described second Diluted Alcohol storage tank all one end with a feed liquor main valve 12 are connected, the liquid outlet of described first Diluted Alcohol storage tank and one end of one first Diluted Alcohol storage tank liquid valve 5 are connected, the liquid outlet of described second Diluted Alcohol storage tank and one end of one second Diluted Alcohol storage tank liquid valve 6 are connected, the other end of described first Diluted Alcohol storage tank liquid valve is all connected with one end of one first Diluted Alcohol transfer pump 13 and one end of one second Diluted Alcohol transfer pump 14 with the other end of described second Diluted Alcohol storage tank liquid valve, the inlet of the gravity tank that the other end of described first Diluted Alcohol transfer pump and the other end of the second Diluted Alcohol transfer pump are also arranged at a high position with is connected, a full level alarm switch 28 and low alarm switch 29 it is provided with on the tank body of described gravity tank；The liquid outlet of described gravity tank and a gravity tank go out one end of liquid regulation valve 4 and are connected；Described first Diluted Alcohol tank inside is provided with a liquid level gauge with the inside of one second Diluted Alcohol storage tank；
As shown in Figure 2, described alcohol distillation device includes one in order to the destilling tower of alcohol distillation, one end of heating cylinder 17 steam first air inlet of described destilling tower and destilling tower heating cylinder jacket steam regulation valve 1 is connected, heating cylinder steam second air inlet of described destilling tower and one end of a destilling tower heating cylinder coil pipe steam control valve 2 are connected, the heating cylinder of described destilling tower offers one and is connected in order to the liquid outlet of waste discharge alcohol, one end of the liquid outlet of described heating cylinder and waste discharge alcohol regulation valve 3；Described heating cylinder is also connected with the vaporization chamber 18 of described destilling tower, described vaporization chamber top is communicated with the extension tower portion 19 of described destilling tower, the lower openings in described extension tower portion goes out the other end of liquid regulation valve and is connected with described gravity tank, the upper opening in described extension tower portion and one end of a return valve 7 are connected, and the other end of described return valve and one end of a qualified alcohol liquid valve 8 are connected；The tower top opening extending tower portion of described destilling tower and a sheet frame condenser are connected, described sheet frame condenser offers a cooling water intake, one cold water intaking water return outlet and a condensation alcohol liquid outlet, one end of described cooling water intake and cooling circulating water water inlet main valve 11 is connected, the inlet of described alcohol liquid outlet and a surge tank is connected, a liquid-level switch 30 it is provided with on the tank body of described surge tank, the liquid outlet of described surge tank and one end of a reflow of alcohol pump 15 are connected, the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
It is provided with a thermometer in the inside of described heating cylinder, the inside of described vaporization chamber, the inside of described tower top and the return main 20 being connected with described cooling water water return outlet；It is provided with a pressure sensor 21 in the jet chimney that first air inlet of the inside of described vaporization chamber and the heating cylinder of described destilling tower is connected with one end of described destilling tower heating cylinder jacket steam regulation valve；The inside of described vaporization chamber is additionally provided with a liquid level gauge 27 and pressure sensor 22；One it is provided with in order to detect the alcohol concentration meter 31 of alcohol concentration and flow simultaneously in the pipeline that the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
As shown in Figure 3, described qualified alcohol storage device includes one first qualified alcohol storage tank 23, one second qualified alcohol storage tank 24 and a cooler, the other end of described qualified alcohol liquid valve is connected with one end of described cooler, one end of the other end of described cooler and one end of one first qualified alcohol storage tank liquid feed valve 9 and one the two the first qualified alcohol storage tank liquid feed valve 10 is connected, the other end of described first qualified alcohol storage tank liquid feed valve is connected with the inlet of described first qualified alcohol storage tank, the other end of one end of described second qualified alcohol storage tank liquid feed valve is connected with the inlet of described second qualified alcohol storage tank；The liquid outlet of described first qualified alcohol storage tank is all connected with a qualified alcohol Pump for giving-out 16 with the liquid outlet of described second qualified alcohol storage tank；The inside of described first qualified alcohol storage tank is provided with a liquid level gauge with the inside of described second qualified alcohol storage tank.
In the present embodiment, alcohol distillation be using Workshop Production reclaim Diluted Alcohol as raw material, obtain alcohol in high concentration by distillation, to meet subsequent production requirement.Complete equipment includes Diluted Alcohol storage device, alcohol distillation device and qualified alcohol storage three parts of device.By Pump for giving-out, the Diluted Alcohol in Diluted Alcohol storage tank is transported to gravity tank keep in, gravity tank supplements in real time according to the liquid level change in tower reactor, alcohol distillation device carries out air-distillation, after concentration arrives, qualified alcohol is transported to after supercooling qualified alcohol storage tank and stores.In whole production process, can valve state in which controlling in real time in real time inspection current setting.
Especially, the using method of described medicinal alcohol distillation automatic control production system comprises the following steps:
I is standby
Stand-by state refers to that whole equipment does not produce, and equipment is only in stand-by state and just can produce.
II feed liquor
Unlatching equipment, equipment enters into feed liquor state.First by Diluted Alcohol storage tank to gravity tank feed liquor, until gravity tank high level；Then by gravity tank to tower reactor feed liquor, until tower reactor high level.During feed liquor, the liquid valve of two Diluted Alcohol storage tanks opens out liquid simultaneously, and selected Pump for giving-out starts running.In whole still-process, as long as tower reactor liquid level is less than setting working solution place value, gravity tank will be from trend tower reactor fluid infusion, until tower reactor high level.If the liquid level of gravity tank is reported to the police less than lower bound, Diluted Alcohol storage tank is just as gravity tank fluid infusion, until liquid level height is only limited to.
III heating
Tower reactor liquid level reaches work liquid level, begins to warm up, and cools down water water intaking valve and open.Heating cylinder temperature is less than setting operating temperature, and coil pipe steam valve is opened, and bottom temperature is less than setting operating temperature, and jacket steam valve is opened.The two steam valve is all regulation valve, and system can be automatically adjusted valve aperture according to set temperature value by PID, temperature be controlled near design temperature, it is ensured that stablizing of still-process.
IV refluxes/goes out liquid
Along with bottom temperature raises, the alcohol amount evaporated is gradually increased, when reaching surge tank high level, reflow of alcohol pump is opened, flowmeter detects in real time, and alcohol concentration reaches the qualified alcohol concentration set, and opens out qualified alcohol valve and qualified alcohol storage tank liquid feed valve.First select the first qualified alcohol storage tank feed liquor, if the first qualified alcohol storage tank arrives high level, automatically switch to the second qualified alcohol storage tank and continue feed liquor.If alcohol concentration not up to sets concentration value, open return valve, continue distillation.
V waste discharge alcohol/stopping heating
The basis for estimation of equipment aneroid: two Diluted Alcohol storage tanks and gravity tank aneroid simultaneously.The condition of waste discharge alcohol: the first, equipment state is in reflux state；The second, the waste discharge alcohol temperature value of tower top temperature, bottom temperature, heating cylinder temperature above correspondence.
When production status meets waste discharge alcohol condition, and equipment is judged as aneroid simultaneously, then system is first shut off steam valve, stops heating, start timing, after reaching to stop heat set points, open waste discharge alcohol valve, starting waste discharge alcohol, drained rear equipment state jumps to standby, and production terminates.
When production status meets waste discharge alcohol condition, but equipment also has Diluted Alcohol, at this moment stops feed liquor, steam off valve, opens waste discharge alcohol valve, drained after, restart feed liquor, heating, continue distillation.
When tower reactor liquid level is less than work liquid level, and equipment is judged as aneroid, then system steam off valve, stopping heating, start timing, and after reaching to stop heat set points, equipment redirects as standby, and production terminates.
Wherein, the amount of a waste discharge alcohol artificially can be revised according to actual conditions.
The foregoing is only preferred embodiment of the present utility model, all impartial changes done according to the utility model claim and modification, all should belong to covering scope of the present utility model.
Claims (1)
1. a medicinal alcohol distillation automatic control production system, it is characterised in that: include a Diluted Alcohol storage device, an alcohol distillation device and qualified alcohol storage device；
Described Diluted Alcohol storage device includes one first Diluted Alcohol storage tank and one second Diluted Alcohol storage tank；The inlet of the inlet of described first Diluted Alcohol storage tank and described second Diluted Alcohol storage tank all one end with a feed liquor main valve are connected, the liquid outlet of described first Diluted Alcohol storage tank and one end of one first Diluted Alcohol storage tank liquid valve are connected, the liquid outlet of described second Diluted Alcohol storage tank and one end of one second Diluted Alcohol storage tank liquid valve are connected, the other end of described first Diluted Alcohol storage tank liquid valve is all connected with one end of one first Diluted Alcohol transfer pump and one end of one second Diluted Alcohol transfer pump with the other end of described second Diluted Alcohol storage tank liquid valve, the inlet of the gravity tank that the other end of described first Diluted Alcohol transfer pump and the other end of the second Diluted Alcohol transfer pump are also arranged at a high position with is connected, a full level alarm switch and a low alarm switch it is provided with on the tank body of described gravity tank；The liquid outlet of described gravity tank and a gravity tank go out one end of liquid regulation valve and are connected；Described first Diluted Alcohol tank inside is provided with a liquid level gauge with the inside of one second Diluted Alcohol storage tank；
Described alcohol distillation device includes one in order to the destilling tower of alcohol distillation, one end of heating cylinder steam first air inlet of described destilling tower and destilling tower heating cylinder jacket steam regulation valve is connected, heating cylinder steam second air inlet of described destilling tower and one end of a destilling tower heating cylinder coil pipe steam control valve are connected, the heating cylinder of described destilling tower offers one and is connected in order to the liquid outlet of waste discharge alcohol, one end of the liquid outlet of described heating cylinder and waste discharge alcohol regulation valve；Described heating cylinder also vaporization chamber with described destilling tower is connected, described vaporization chamber top is communicated with the extension tower portion of described destilling tower, the lower openings in described extension tower portion goes out the other end of liquid regulation valve and is connected with described gravity tank, the upper opening in described extension tower portion and one end of a return valve are connected, and the other end of described return valve and one end of a qualified alcohol liquid valve are connected；The tower top opening extending tower portion of described destilling tower and a sheet frame condenser are connected, described sheet frame condenser offers a cooling water intake, one cold water intaking water return outlet and a condensation alcohol liquid outlet, one end of described cooling water intake and cooling circulating water water inlet main valve is connected, the inlet of described alcohol liquid outlet and a surge tank is connected, a liquid-level switch it is provided with on the tank body of described surge tank, the liquid outlet of described surge tank and one end of a reflow of alcohol pump are connected, the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
It is provided with a thermometer in the inside of described heating cylinder, the inside of described vaporization chamber, the inside of described tower top and the return main being connected with described cooling water water return outlet；It is provided with a pressure sensor in the jet chimney that first air inlet of the inside of described vaporization chamber and the heating cylinder of described destilling tower is connected with one end of described destilling tower heating cylinder jacket steam regulation valve；The inside of described vaporization chamber is additionally provided with a liquid level gauge；One it is provided with in order to detect the alcohol concentration meter of alcohol concentration and flow simultaneously in the pipeline that the other end of described reflow of alcohol pump is connected with one end of the other end of described return valve and described qualified alcohol liquid valve；
Described qualified alcohol storage device includes one first qualified alcohol storage tank, one second qualified alcohol storage tank and a cooler, the other end of described qualified alcohol liquid valve is connected with one end of described cooler, the other end of described cooler and one end of one end of one first qualified alcohol storage tank liquid feed valve and one second qualified alcohol storage tank liquid feed valve are connected, the other end of described first qualified alcohol storage tank liquid feed valve is connected with the inlet of described first qualified alcohol storage tank, the other end of one end of described second qualified alcohol storage tank liquid feed valve is connected with the inlet of described second qualified alcohol storage tank；The liquid outlet of described first qualified alcohol storage tank is all connected with a qualified alcohol Pump for giving-out with the liquid outlet of described second qualified alcohol storage tank；The inside of described first qualified alcohol storage tank is provided with a liquid level gauge with the inside of described second qualified alcohol storage tank.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620140624.8U CN205549646U (en) | 2016-02-25 | 2016-02-25 | Medicinal alcohol distillation automatic control production system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620140624.8U CN205549646U (en) | 2016-02-25 | 2016-02-25 | Medicinal alcohol distillation automatic control production system |
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| CN205549646U true CN205549646U (en) | 2016-09-07 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110479181A (en) * | 2019-08-12 | 2019-11-22 | 江苏新美星包装机械股份有限公司 | A kind of online deployment device |
-
2016
- 2016-02-25 CN CN201620140624.8U patent/CN205549646U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110479181A (en) * | 2019-08-12 | 2019-11-22 | 江苏新美星包装机械股份有限公司 | A kind of online deployment device |
| CN110479181B (en) * | 2019-08-12 | 2024-04-09 | 江苏新美星包装机械股份有限公司 | Online allocation device |
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| CP02 | Change in the address of a patent holder |
Address after: 363000 No. 1, Amber Road, Xiangcheng District, Zhangzhou City, Fujian Province Patentee after: ZHANGZHOU PIEN TZE HUANG PHARMACEUTICAL Co.,Ltd. Address before: Xiangcheng District 363000 in Fujian province Zhangzhou City Street No. 1 Patentee before: ZHANGZHOU PIEN TZE HUANG PHARMACEUTICAL Co.,Ltd. |
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| CP02 | Change in the address of a patent holder |