CN103536446B - Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup - Google Patents
Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup Download PDFInfo
- Publication number
- CN103536446B CN103536446B CN201310510103.8A CN201310510103A CN103536446B CN 103536446 B CN103536446 B CN 103536446B CN 201310510103 A CN201310510103 A CN 201310510103A CN 103536446 B CN103536446 B CN 103536446B
- Authority
- CN
- China
- Prior art keywords
- storage tank
- benefits
- economic benefits
- social benefits
- connecting pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
The invention relates to an automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and an automatic control production method of the syrup. The device comprises an extraction device, a dual-purpose concentration device and an online sterilization device. The extraction device, the dual-purpose concentration device and the online sterilization device are respectively provided with single-unit automatic control systems, automatic control valves are arranged on connecting pipelines between the devices, and the single-unit automatic control system and control lines of the automatic control valves are all connected with a monitoring and operating system. The automatic control production method of the bulbus fritillariae cirrhosae lung-heat-clearing syrup using the automatic control production device includes that according to production process of the bulbus fritillariae cirrhosae lung-heat-clearing syrup, the monitoring and operating system controls working of selected devices through corresponding single-unit automatic control systems with operation processes of extraction, dual-purpose concentration and sterilization in sequence, and meanwhile, during the working, the monitoring and operating system controls on-and-off of corresponding automatic control valves so as to complete various processes and conveying of liquid medicine among different devices. The device and the method are high in automation level, and automatic control production can be carried out according to the production process of the bulbus fritillariae cirrhosae lung-heat-clearing syrup.
Description
Technical field
The present invention relates to Chinese medicine production technical field, particularly a kind of Fritillary lung heat clearing syrup automatic control process units and method thereof.
Background technology
Chinese medicine is divided into Chinese patent medicine and Chinese crude drug by processing technique, and Chinese patent medicine is wherein the Chinese medicine product of making various different dosage forms taking Chinese herbal medicine as raw material through preparation processing.Fritillary lung heat clearing syrup is the Chinese patent medicine of a kind of clearing away lung-heat and moistening for dryness, relieving cough and resolving phlegm.In the production process of Fritillary lung heat clearing syrup, generally need to extract medical material, concentrate, the manufacturing procedure such as sterilizing, therefore, be necessary to design a set of automaticity automatic control process units high, that produce applicable to Fritillary lung heat clearing syrup.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, a kind of Fritillary lung heat clearing syrup automatic control process units and method thereof are provided, this device and method automaticity is high, can carry out automatic control production according to the production technology of Fritillary lung heat clearing syrup.
For achieving the above object, technical scheme of the present invention is: a kind of Fritillary lung heat clearing syrup automatic control process units, comprise extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, the liquid outlet of described extraction element is connected to economic benefits and social benefits enrichment facility through connecting pipe, the liquid outlet of described economic benefits and social benefits enrichment facility is connected to online bactericidal unit through connecting pipe, and the liquid outlet of described online bactericidal unit is connected to next production process through connecting pipe; Described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit are respectively equipped with unit robot control system(RCS), described unit robot control system(RCS) is all connected to monitor operating system, in connecting pipe between described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, be respectively equipped with Self controlling valve, the control line of described Self controlling valve is all connected to monitor operating system.
Further, described extraction element comprises some extraction pot and some extracting solution storage tanks, and described economic benefits and social benefits enrichment facility comprises some economic benefits and social benefits concentration tanks and some economic benefits and social benefits concentrated solution storage tanks, and described online bactericidal unit comprises storage tank after sterilizing installation and some sterilizings.
Further, described extraction element comprises the first extraction pot, the second extraction pot, the 3rd extraction pot, the 4th extraction pot, the first extracting solution storage tank and the second extracting solution storage tank, described economic benefits and social benefits enrichment facility comprises the first economic benefits and social benefits concentration tank, the second economic benefits and social benefits concentration tank, the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank, and described online bactericidal unit comprises after sterilizing installation, the first sterilizing storage tank after storage tank and the second sterilizing;
The liquid outlet of described the first extraction pot and the second extraction pot is connected to the first extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the 3rd extraction pot and the 4th extraction pot is connected to the second extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the first extracting solution storage tank is connected to the first economic benefits and social benefits concentration tank through connecting pipe, and the liquid outlet of described the second extracting solution storage tank is connected to the second economic benefits and social benefits concentration tank through connecting pipe;
The liquid outlet of described the first economic benefits and social benefits concentration tank is connected to the first economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described the second economic benefits and social benefits concentration tank is connected to the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, and the liquid outlet of described the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank is connected to sterilizing installation through connecting pipe respectively;
The refluxing opening of described sterilizing installation is connected to respectively the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described sterilizing installation storage tank after storage tank and the second sterilizing after connecting pipe is connected to respectively the first sterilizing, after described the first sterilizing, after storage tank and the second sterilizing, the liquid outlet of storage tank is connected to next production process through connecting pipe respectively.
The present invention also provides the Fritillary lung heat clearing syrup automatic control production method of utilizing described device, monitor operating system is according to the production technology of Fritillary lung heat clearing syrup, concentrate and sterilization process operation through extraction, economic benefits and social benefits successively, by the corresponding selected device work of unit robot control system(RCS) control, control in the course of the work corresponding Self controlling valve and open and close, to complete the conveying between different device of each operation and medicinal liquid simultaneously.
Further, while carrying out abstraction process, in corresponding extraction pot, add relevant medical material, then extraction element is worked as follows:
Step 1.1: according to the extraction process of Fritillary lung heat clearing syrup, judgement is alcohol extraction or water extraction is then accordingly added ethanol or drinking water in extraction pot;
Step 1.2: immersion medical material reaches the soak time of setting, then decocts;
Step 1.3: reach after the decocting time of setting, stop decocting, then open the Self controlling valve in the connecting pipe between extraction pot and corresponding extracting solution storage tank, export extracting solution to extracting solution storage tank;
Step 1.4: repeat above-mentioned steps 1.1 ~ 1.3, until reach the decoction number of times of setting, decoct and finish;
Step 1.5: extraction pot automatic discharge, abstraction process finishes.
Further, while carrying out economic benefits and social benefits enrichment process, economic benefits and social benefits enrichment facility carries out as follows:
Step 2.1: open the Self controlling valve in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank, enter extracting solution to certain liquid level and close Self controlling valve, start to concentrate;
Step 2.2: in the time that concentrated concentration arrives target zone, open the Self controlling valve in the connecting pipe between economic benefits and social benefits concentration tank and corresponding economic benefits and social benefits concentrated solution storage tank, start fluid; When the liquid level in economic benefits and social benefits concentration tank lower than set minimum work liquid level time, the Self controlling valve of closing in the connecting pipe between economic benefits and social benefits concentration tank and corresponding economic benefits and social benefits concentrated solution storage tank stops fluid, and the Self controlling valve of opening in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank supplements extracting solution, then continue concentrated, until all extracting solution are concentrated and fluid completes, economic benefits and social benefits enrichment process finishes.
Further, while carrying out sterilization process, online bactericidal unit carries out as follows:
Step 3.1: the concentrated solution in pre-thermal agitation economic benefits and social benefits concentrated solution storage tank, then open the Self controlling valve in the connecting pipe between economic benefits and social benefits concentrated solution storage tank and sterilizing installation, export concentrated solution to sterilizing installation;
Step 3.2: be heated in sterilizing installation until medicinal liquid after design temperature high temperature sterilize, open the Self controlling valve in the connecting pipe between storage tank after sterilizing installation and accordingly sterilizing, export medicinal liquid to after sterilizing storage tank, sterilization process finishes.
Compared to prior art, the invention has the beneficial effects as follows: this device and method highly versatile, automaticity is high, can be according to the production technology of Fritillary lung heat clearing syrup, the operation that selection need to complete, and the operation completing is as required selected, is combined corresponding work equipment, by the corresponding selected work equipment work of unit robot control system(RCS) control, realize the automatic controlization of Fritillary lung heat clearing syrup and produced, there is very strong practicality and wide application prospect.
Below in conjunction with drawings and the specific embodiments, the present invention is described in further detail.
Brief description of the drawings
Fig. 1 is the syndeton schematic diagram of the Fritillary lung heat clearing syrup automatic control process units of the embodiment of the present invention.
Fig. 2 is the workflow diagram of abstraction process in the embodiment of the present invention.
Fig. 3 is the workflow diagram of enrichment process in the embodiment of the present invention.
Detailed description of the invention
Fritillary lung heat clearing syrup automatic control process units of the present invention, comprise extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, the liquid outlet of described extraction element is connected to economic benefits and social benefits enrichment facility through connecting pipe, the liquid outlet of described economic benefits and social benefits enrichment facility is connected to online bactericidal unit through connecting pipe, and the liquid outlet of described online bactericidal unit is connected to next production process through connecting pipe; Described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit are respectively equipped with unit robot control system(RCS), described unit robot control system(RCS) is all connected to monitor operating system, in connecting pipe between described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, be respectively equipped with Self controlling valve, the control line of described Self controlling valve is all connected to monitor operating system.
As shown in Figure 1, described extraction element comprises some extraction pot and some extracting solution storage tanks, and described economic benefits and social benefits enrichment facility comprises some economic benefits and social benefits concentration tanks and some economic benefits and social benefits concentrated solution storage tanks, and described online bactericidal unit comprises storage tank after sterilizing installation and some sterilizings.
Described extraction element comprises the first extraction pot, the second extraction pot, the 3rd extraction pot, the 4th extraction pot, the first extracting solution storage tank and the second extracting solution storage tank, described economic benefits and social benefits enrichment facility comprises the first economic benefits and social benefits concentration tank, the second economic benefits and social benefits concentration tank, the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank, and described online bactericidal unit comprises after sterilizing installation, the first sterilizing storage tank after storage tank and the second sterilizing;
The liquid outlet of described the first extraction pot and the second extraction pot is connected to the first extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the 3rd extraction pot and the 4th extraction pot is connected to the second extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the first extracting solution storage tank is connected to the first economic benefits and social benefits concentration tank through connecting pipe, and the liquid outlet of described the second extracting solution storage tank is connected to the second economic benefits and social benefits concentration tank through connecting pipe;
The liquid outlet of described the first economic benefits and social benefits concentration tank is connected to the first economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described the second economic benefits and social benefits concentration tank is connected to the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, and the liquid outlet of described the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank is connected to sterilizing installation through connecting pipe respectively;
The refluxing opening of described sterilizing installation is connected to respectively the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described sterilizing installation storage tank after storage tank and the second sterilizing after connecting pipe is connected to respectively the first sterilizing, after described the first sterilizing, after storage tank and the second sterilizing, the liquid outlet of storage tank is connected to next production process through connecting pipe respectively.
The present invention also provides the Fritillary lung heat clearing syrup automatic control production method of utilizing described device, monitor operating system is according to the production technology of Fritillary lung heat clearing syrup, concentrate and sterilization process operation through extraction, economic benefits and social benefits successively, by the corresponding selected device work of unit robot control system(RCS) control, control in the course of the work corresponding Self controlling valve and open and close, to complete the conveying between different device of each operation and medicinal liquid simultaneously.
In the present embodiment, while carrying out abstraction process, in corresponding extraction pot, add relevant medical material, then extraction element is worked as follows:
Step 1.1: according to the extraction process of Fritillary lung heat clearing syrup, judgement is alcohol extraction or water extraction is then accordingly added ethanol or drinking water in extraction pot;
Step 1.2: immersion medical material reaches the soak time of setting, then decocts;
Step 1.3: reach after the decocting time of setting, stop decocting, then open the Self controlling valve in the connecting pipe between extraction pot and corresponding extracting solution storage tank, export extracting solution to extracting solution storage tank;
Step 1.4: repeat above-mentioned steps 1.1 ~ 1.3, until reach the decoction number of times of setting, decoct and finish;
Step 1.5: extraction pot automatic discharge, abstraction process finishes.
As shown in Figure 2, abstraction process specific works flow process is as follows: prepare to produce, add medical material, after having fed intake, first judge whether to extract volatile oil; If do not extract volatile oil, judge whether again alcohol extraction, if alcohol extraction is added ethanol and carried out successively medical material immersion, decoction, fluid; If not alcohol extraction, adds decoction drinking water and carries out successively medical material immersion, decoction, fluid; If extraction volatile oil add and extract volatilization drinking water, and heated and boiled is to extract volatile oil, after volatile oil has extracted, adds other medical materials, after having fed intake, add that decoction drinking water soaks successively, decoction, fluid.Wherein, immersion and the number of times, the time that decoct can be set according to Fritillary lung heat clearing syrup, and now extraction pot is interior in intermittent cyclic state, and circulation time and off time are also set according to Fritillary lung heat clearing syrup.In the time of fluid putty, unit robot control system(RCS) control steam control valve by putty steam blast to continue fluid.In the time that fluid completes, also do not reach setting value if decoct number of times, return and continue to judge whether to extract; Reach while setting value if decoct number of times, now fluid completes, decocts end, opens the bottom of extraction pot and discharges medicinal residues; After having removed the gred, close bottom, now abstraction process finishes.After shutdown, can carry out alkali liquor cleaning and hot water cleaning to extraction element, so that produce the Fritillary lung heat clearing syrup of next batch.
In the present embodiment, while carrying out economic benefits and social benefits enrichment process, economic benefits and social benefits enrichment facility carries out as follows:
Step 2.1: open the Self controlling valve in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank, enter extracting solution to certain liquid level and close Self controlling valve, start to concentrate;
Step 2.2: in the time that concentrated concentration arrives target zone, open the Self controlling valve in the connecting pipe between economic benefits and social benefits concentration tank and corresponding economic benefits and social benefits concentrated solution storage tank, start fluid; When the liquid level in economic benefits and social benefits concentration tank lower than set minimum work liquid level time, the Self controlling valve of closing in the connecting pipe between economic benefits and social benefits concentration tank and corresponding economic benefits and social benefits concentrated solution storage tank stops fluid, and the Self controlling valve of opening in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank supplements extracting solution, then continue concentrated, until all extracting solution are concentrated and fluid completes, economic benefits and social benefits enrichment process finishes.
As shown in Figure 3, enrichment process specific works flow process is as follows: prepare to produce, concentration tank is carried out after evacuation, start feed liquor, concentrated.If not tailing, in the time that concentrated concentration arrives target zone, start fluid, if the liquid level after fluid is lower than work liquid level, enter extracting solution reconcentration, if the liquid level after fluid is higher than work liquid level, continue fluid; In the time that concentrated concentration does not arrive target zone, continue concentrated.If tailing starts tailing concentration, in the time that concentrated concentration arrives target zone or while there is low liquid level, carry out tailing fluid, tailing carries out heat water-spraying, and fluid completes, concentrated end; In the time that concentrated concentration does not arrive target zone, continue tailing concentration.After shutdown, can carry out alkali liquor cleaning and hot water cleaning to enrichment facility.
In the present embodiment, while carrying out sterilization process, online bactericidal unit carries out as follows:
Step 3.1: the concentrated solution in pre-thermal agitation economic benefits and social benefits concentrated solution storage tank, then open the Self controlling valve in the connecting pipe between economic benefits and social benefits concentrated solution storage tank and sterilizing installation, export concentrated solution to sterilizing installation;
Step 3.2: be heated in sterilizing installation until medicinal liquid after design temperature high temperature sterilize, open the Self controlling valve in the connecting pipe between storage tank after sterilizing installation and accordingly sterilizing, export medicinal liquid to after sterilizing storage tank, sterilization process finishes.
Below in conjunction with the production technology of Fritillary lung heat clearing syrup, the invention will be further described.
The production technology of Fritillary lung heat clearing syrup comprises two kinds of flow processs, and one is the distillation extraction of Semen Armeniacae Amarum, Herba Menthae, and another is that other medical materials concentrate to obtain water extraction condensed cream through water extraction, obtains finished product finally by high-temperature sterilization unit sterilizing.
As shown in Figure 2, the water extraction flow process of Fritillary lung heat clearing syrup is: by monitor operating system, enter " combination operation " of " extraction-single-action " option, select Fritillary lung heat clearing syrup water extraction operation, after typing product batch number, start and produce automatic program.Medical material is dropped into extraction pot, produce and start.First pass, robot control system(RCS) is added the drinking water of 6.5 times of medical material amounts by opening drinking water pipeline pneumatic operated valve, starts decoction program.In decoction process, temperature control system, by automatic steam regulation valve opening, makes extracting solution keep slight boiling condition, and tubing pump and related valve are opened simultaneously, extract in flow container in intermittent cyclic state.Time timer will record decocting time, reach the decocting time of setting after 2 hours, system, by automatic steam off valve, is opened outlet valve, medicinal liquid is evacuated to extracting solution basin stand-by, extraction pot robot control system(RCS) continues to add 2 hours processes of second time decoction of drinking water startup of 6 times of medical material amounts.After 2 decoctions reach, discharging completes, and decocts and finishes.
The concentration flow path of Fritillary lung heat clearing syrup as shown in Figure 3, taking water extraction concentration flow path as example: pass through monitor operating system, enter " combination operation " of " economic benefits and social benefits " option, confirm the extracting solution trade mark to be concentrated, batch correct after, in robot control system(RCS), set discharge concentration, start concentrated automatic program, concentration systems evacuation, feed liquid is sent into respectively that economic benefits and social benefits enrichment facility one is imitated, in the concentrated cylinder of two effects, is finished to the high limit of the liquid level of setting feed liquor by vacuum.Start and concentrate, in concentration process, system detects liquid level in evaporation tank, and during lower than work liquid level, constantly feed supplement enters enrichment facility.Treat that basin inner liquid medicine all enters enrichment facility, system starts tailing concentration, and solution to be concentrated is in the time that the detection of pressure reduction density tester reaches setting density, and system start-up discharging program, concentrates and finish.
The sterilizing flow process of Fritillary lung heat clearing syrup is: pass through monitor operating system, enter " combination operation " of " sterilizing " option, confirm the basin trade mark, batch correct of syrup extracting solution subject to sterilization, before sterilizing, pass into steam to economic benefits and social benefits concentrated solution basin chuck, open stirring, preheating basin inner liquid medicine simultaneously.Treat that tank inner liquid medicine is preheated to 70 DEG C, start mateiral pump, medicinal liquid is delivered to bactericidal unit, after medicine liquid heating to 121 DEG C high temperature sterilize, through cooling enter sterilizing after basin.Robot control system(RCS) is by the temperature information providing according to the temperature sensor on pipeline, and the direction of three-way diverter valve in control piper, makes medicinal liquid not meeting before 121 DEG C of sterilising temps, cannot enter subsequent processing operation by this operation.
Each flow process possesses unit robot control system(RCS) above, and between flow process, adopts line automatic program, has realized the process of Fritillary lung heat clearing syrup from raw material to sterilizing ointment.
Be more than preferred embodiment of the present invention, all changes of doing according to technical solution of the present invention, when the function producing does not exceed the scope of technical solution of the present invention, all belong to protection scope of the present invention.
Claims (5)
1. a Fritillary lung heat clearing syrup automatic control process units, it is characterized in that: comprise extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, the liquid outlet of described extraction element is connected to respectively economic benefits and social benefits enrichment facility through connecting pipe, the liquid outlet of described economic benefits and social benefits enrichment facility is connected to online bactericidal unit through connecting pipe, and the liquid outlet of described online bactericidal unit is connected to next production process through connecting pipe; Described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit are respectively equipped with unit robot control system(RCS), described unit robot control system(RCS) is all connected to monitor operating system, in connecting pipe between described extraction element, economic benefits and social benefits enrichment facility and online bactericidal unit, be respectively equipped with Self controlling valve, the control line of described Self controlling valve is all connected to monitor operating system;
Described extraction element comprises the first extraction pot, the second extraction pot, the 3rd extraction pot, the 4th extraction pot, the first extracting solution storage tank and the second extracting solution storage tank, described economic benefits and social benefits enrichment facility comprises the first economic benefits and social benefits concentration tank, the second economic benefits and social benefits concentration tank, the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank, and described online bactericidal unit comprises after sterilizing installation, the first sterilizing storage tank after storage tank and the second sterilizing;
The liquid outlet of described the first extraction pot and the second extraction pot is connected to the first extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the 3rd extraction pot and the 4th extraction pot is connected to the second extracting solution storage tank through connecting pipe respectively, the liquid outlet of described the first extracting solution storage tank is connected to the first economic benefits and social benefits concentration tank through connecting pipe, and the liquid outlet of described the second extracting solution storage tank is connected to the second economic benefits and social benefits concentration tank through connecting pipe;
The liquid outlet of described the first economic benefits and social benefits concentration tank is connected to the first economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described the second economic benefits and social benefits concentration tank is connected to the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, and the liquid outlet of described the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank is connected to sterilizing installation through connecting pipe respectively;
The refluxing opening of described sterilizing installation is connected to respectively the first economic benefits and social benefits concentrated solution storage tank and the second economic benefits and social benefits concentrated solution storage tank through connecting pipe, the liquid outlet of described sterilizing installation storage tank after storage tank and the second sterilizing after connecting pipe is connected to respectively the first sterilizing, after described the first sterilizing, after storage tank and the second sterilizing, the liquid outlet of storage tank is connected to next production process through connecting pipe respectively.
2. the Fritillary lung heat clearing syrup automatic control production method that utilization is installed as claimed in claim 1, it is characterized in that: monitor operating system is according to the production technology of Fritillary lung heat clearing syrup, concentrate and sterilization process operation through extraction, economic benefits and social benefits successively, by the corresponding selected device work of unit robot control system(RCS) control, control in the course of the work corresponding Self controlling valve and open and close, to complete the conveying between different device of each operation and medicinal liquid simultaneously.
3. Fritillary lung heat clearing syrup automatic control production method according to claim 2, is characterized in that: while carrying out abstraction process, in corresponding extraction pot, add relevant medical material, then extraction element is worked as follows:
Step 1.1: according to the extraction process of Fritillary lung heat clearing syrup, judgement is alcohol extraction or water extraction is then accordingly added quantitative ethanol or drinking water in extraction pot;
Step 1.2: immersion medical material reaches the soak time of setting, then decocts;
Step 1.3: reach after the decocting time of setting, stop decocting, then open the Self controlling valve in the connecting pipe between extraction pot and corresponding extracting solution storage tank, start mateiral pump, export extracting solution to extracting solution storage tank;
Step 1.4: repeat above-mentioned steps 1.1 ~ 1.3, until reach the decoction number of times of setting, decoct and finish;
Step 1.5: extraction pot automatic discharge, abstraction process finishes.
4. Fritillary lung heat clearing syrup automatic control production method according to claim 2, is characterized in that: while carrying out economic benefits and social benefits enrichment process, economic benefits and social benefits enrichment facility carries out as follows:
Step 2.1: open the Self controlling valve in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank, utilize vacuum, extracting solution is evacuated to economic benefits and social benefits enrichment facility, when extracting solution reaches setting level value, close Self controlling valve, start to concentrate;
Step 2.2: when the liquid level in economic benefits and social benefits concentration tank lower than set minimum work liquid level time, and the Self controlling valve of opening in the connecting pipe between extracting solution storage tank and corresponding economic benefits and social benefits concentration tank supplements extracting solution, then continue concentrated, until all extracting solution are concentrated and fluid completes, economic benefits and social benefits enrichment process finishes.
5. Fritillary lung heat clearing syrup automatic control production method according to claim 2, is characterized in that: while carrying out sterilization process, online bactericidal unit carries out as follows:
Step 3.1: the concentrated solution in pre-thermal agitation economic benefits and social benefits concentrated solution storage tank, then open the Self controlling valve in the connecting pipe between economic benefits and social benefits concentrated solution storage tank and sterilizing installation, export concentrated solution to sterilizing installation;
Step 3.2: in sterilization process, when medicine liquid heating is during to set temperature value, medicinal liquid directly passes through condensing unit, be transported to storage tank after sterilizing, in the time that fluid temperature does not also reach set temperature value, medicinal liquid is got back to economic benefits and social benefits concentrated solution storage tank the inside by reflux pipe, reheats sterilizing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310510103.8A CN103536446B (en) | 2013-10-25 | 2013-10-25 | Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310510103.8A CN103536446B (en) | 2013-10-25 | 2013-10-25 | Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103536446A CN103536446A (en) | 2014-01-29 |
CN103536446B true CN103536446B (en) | 2014-11-19 |
Family
ID=49960565
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310510103.8A Active CN103536446B (en) | 2013-10-25 | 2013-10-25 | Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103536446B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112221191A (en) * | 2020-10-13 | 2021-01-15 | 杭州师范大学钱江学院 | Medicament extraction method and system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1679729A (en) * | 2005-01-28 | 2005-10-12 | 云南昆船设计研究院 | Chinese medicine preparation and set of apparatuses thereof |
CN2762804Y (en) * | 2005-01-28 | 2006-03-08 | 云南昆船设计研究院 | Traditional Chinese medicine liquid sterilizing device |
CN101757802A (en) * | 2010-02-04 | 2010-06-30 | 陈晓东 | Energy-saving device for low-temperature reduced-pressure extracting and concentrating traditional Chinese medicine |
CN201625192U (en) * | 2009-11-24 | 2010-11-10 | 株洲千金药业股份有限公司 | Integrated control system for preparing traditional Chinese medicine extracts |
CN202715042U (en) * | 2012-06-15 | 2013-02-06 | 浙江远力健药业有限责任公司 | Traditional Chinese medicine extraction and concentration equipment |
-
2013
- 2013-10-25 CN CN201310510103.8A patent/CN103536446B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1679729A (en) * | 2005-01-28 | 2005-10-12 | 云南昆船设计研究院 | Chinese medicine preparation and set of apparatuses thereof |
CN2762804Y (en) * | 2005-01-28 | 2006-03-08 | 云南昆船设计研究院 | Traditional Chinese medicine liquid sterilizing device |
CN201625192U (en) * | 2009-11-24 | 2010-11-10 | 株洲千金药业股份有限公司 | Integrated control system for preparing traditional Chinese medicine extracts |
CN101757802A (en) * | 2010-02-04 | 2010-06-30 | 陈晓东 | Energy-saving device for low-temperature reduced-pressure extracting and concentrating traditional Chinese medicine |
CN202715042U (en) * | 2012-06-15 | 2013-02-06 | 浙江远力健药业有限责任公司 | Traditional Chinese medicine extraction and concentration equipment |
Also Published As
Publication number | Publication date |
---|---|
CN103536446A (en) | 2014-01-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102952629B (en) | Technological method for extracting natural cinnamon oil | |
CN103893991A (en) | Heat cycle extraction concentration method for traditional Chinese medicine | |
CN204824121U (en) | It washs and online sterilization system to blow integrative equipment on -line of embedment | |
CN203763899U (en) | Chinese medicinal herb thermal circulating extracting and concentrating system | |
CN206980170U (en) | A kind of Chinese medicine ethanol extracts rapid concentration equipment integrating | |
CN103301640B (en) | Concentration method and device for traditional Chinese medicine extracting solution | |
CN103536446B (en) | Automatic control production device of bulbus fritillariae cirrhosae lung-heat-clearing syrup and production method of syrup | |
CN202315405U (en) | Automatic liquid medicine extracting control system based on proportion integration differentiation (PID) control | |
CN105126383B (en) | The integrated extraction concentration technique of the energy-efficient automation of Chinese medicine and technological equipment | |
CN103519995B (en) | Huoxiang Zhengqi liquid automatic control production device and method thereof | |
CN203525348U (en) | Self-control production system of traditional Chinese medicines | |
CN2778277Y (en) | Chinese medicinal liquor vacuum condensation equipment | |
CN207384868U (en) | Plant extraction liquid enrichment facility | |
CN102419548B (en) | The medicinal liquid that waste water residual heat recycles extracts concentration automatic control system and method | |
CN105903218A (en) | Continuous concentrating device for jasmine extracting solution and control method thereof | |
CN103690364B (en) | Automatic control production device and automatic control production method of medicine for treating traumatic injury and rheumatic bone pain | |
CN206337058U (en) | A kind of injection stage medicine equipment process water system | |
CN206666169U (en) | A kind of sewage-treatment plant | |
CN206342933U (en) | The MVR vaporising devices that normal temperature starts | |
CN106902530A (en) | A kind of evaporation concentration system of low steam loss | |
CN201085015Y (en) | Full-automatic milk high-order vacuum circulation flash evaporation plate-type condensing unit | |
CN207861928U (en) | A kind of heating of extraction processing procedure water and stand-by provision | |
CN211153611U (en) | Whey liquid forced circulation falling film thickener | |
CN103550682B (en) | Cardiovascular compound recipe tablet automatic control production method and production system thereof | |
CN211734304U (en) | Traditional chinese medicine volatile components draws collecting device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP02 | Change in the address of a patent holder | ||
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: 363000 1 Street, Zhangzhou, Fujian Patentee before: ZHANGZHOU PIEN TZE HUANG PHARMACEUTICAL Co.,Ltd. |