CN202740408U - Capsule production workshop - Google Patents
Capsule production workshop Download PDFInfo
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- CN202740408U CN202740408U CN 201220439471 CN201220439471U CN202740408U CN 202740408 U CN202740408 U CN 202740408U CN 201220439471 CN201220439471 CN 201220439471 CN 201220439471 U CN201220439471 U CN 201220439471U CN 202740408 U CN202740408 U CN 202740408U
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Abstract
The utility model discloses a capsule production workshop, which comprises a drying region and an operating region, wherein the drying region is used for drying capsule green embryos to obtain capsules; the operating region and the drying region are mutually independent and separated; a colloid dipping machine is placed in the operating region; the outside of the colloid dipping machine is preferably provided with a laminar flow cover; the capsule green embryos prepared by the colloid dipping machine are sent to the drying region to be dried; and the operating region is adjacent to a colloid melting region. The capsule production workshop provided by the utility model can ensure the cleanliness required in each region, improves the colloid dipping quality, saves the energy consumption and provides a comfortable working environment for operators.
Description
Technical field
This utility model relates to medical material processing and manufacturing field, is specifically related to a kind of capsule manufacture workshop.
Background technology
Capsule (Capsule) preparation is dosage form the most general in the pharmaceutical preparation, accounts for more than 60% of oral formulations total amount.In 200,000,000,000 of China's Capsules consumption figure years, global total quantity consumed is more than 800,000,000,000.
At present, to be the gelatin that extracts take materials such as the animal bone such as cattle, pig or skins make as raw material the film of Capsules agent.Although gelatin has good characteristic when the preparation Capsules, originate limited, can produce reaction with some drugs, the compatibility is poor, and gelatin may have antigenicity as heterologous protein.For example, the cattle source property gelatin materials of import may contain Protein virus, uses its capsule that makes as raw material may cause the diffusion of bovine spongiform encephalopathy.For avoiding the infection of the human diseases that the animal proteinum protein may cause, market begins to develop the vegetalitas Capsules of alternative gelatin.Replacing animal raw materials with vegetable raw material and make capsule, allow oral drugs bring into play better curative effect, is development trend and the direction of from now on capsule for medicine industry, is great, the revolutionary change of pharmacy industry, has great medical value and economic worth.
At present, the workshop of vegetalitas Capsules comprises colloid solution preparation workshop and dips in the glue workshop.Raw material is put into storage glue tank after colloid solution preparation workshop is formulated into colloid solution.Dip in glue dipping machine and drying equipment etc. are set in the glue workshop, what the colloid solution in the storage glue tank entered into glue dipping machine dips in the glue groove, and capsule die dips colloid solution and forms capsule and give birth to embryo, carries out subsequently drying in drying equipment, forms Capsules.
The present glue workshop of dipping in, glue dipping machine, operating space and dry section are arranged on dips in without obviously separation in glue the workshop in, can't protect cleanliness factor, the temperature and humidity of levying the operating space and dipping in Jiao Qu.Dip in glue groove top without special shield facility, be difficult to guarantee to dip in the stable of the performance such as glue temperature and rheological characteristic in the glue groove as one at whole production process, thereby affect quality and the qualification rate of capsule, and dry section makes the operating space temperature very high with the high temperature that dips in Jiao Qu, easily impact dipping in the required temperature humidity of glue work, energy consumption is high and cause waste, hot and humid gas that operator are done not feel like oneself.
Therefore, this area is in the urgent need to improving the capsule manufacture workshop.
The utility model content
The purpose of this utility model provides a kind of novel capsule manufacture system.
Plant capsule production system of the present utility model comprises:
Dry section is used for that the living embryo of capsule is carried out drying and obtains capsule;
The operating space, the separate mutual separation setting of described operating space and described dry section, and place glue dipping machine in the described operating space, the capsule that is made by glue dipping machine is given birth to embryo and is delivered to dry section and carry out drying.
In another preference, described dry section and operating space are in the same Factory Building, separate by cutting off mutually each other.
In another preference, the cleanliness factor of described operating space is 300,000 grades, and temperature is 20 ~ 30 ℃.
In another preference, described glue dipping machine comprises:
Dip in the glue groove, the described in-built colloid solution that is useful on the preparation plant capsule of glue groove that dips in, the described glue groove periphery of dipping in arranges the laminar flow hood that can open;
Capsule die, described capsule die dip the described colloid solution that dips in the glue groove and form plant gum Tibetan household slave embryo.
In another preference, describedly to dip in glue groove top, be 300,000 grades by the regional cleanliness factor of sealing that described laminar flow hood is shrouded, temperature is 60-80 ℃, humidity is 60-80%.
In another preference, described operating space also is provided with storage glue tank, in the described storage glue tank colloid solution is housed, during use, described storage glue tank places to dip in above the glue groove and by pipeline liquid injecting device and is connected with the described glue groove that dips in, and described colloid solution enters into described dipping in the glue groove by described closing pipe line;
The described preparation of storage glue tank water replanishing device, agitating device and attemperator remain on 55-80 ℃ with the temperature of storing up the colloid solution in the glue tank.
In another preference, described capsule manufacture system also comprises the colloidal sol district, places glue pot in the described colloidal sol district, is used for the colloid solution of preparation preparation plant capsule; Described glue pot comprises tank body and the cover that covers on described tank body, on the described cover charge door is set, and described tank body lower part arranges discharging opening, and described tank interior is provided with homogenizer.
In another preference, the cleanliness factor in described colloidal sol district is 300,000 grades, and temperature is 20-30 ℃, and humidity is 45-55%.
In another preference, the area of described operating space accounts for the 15-25% of described plant capsule production system area; The area of described dry section accounts for the 50-60% of described plant capsule production system area; Described colloidal sol district accounts for the 25-35% of described plant capsule production system area.
In another preference, the discharging opening of described glue pot is connected with storage glue tank by pipeline.
In another preference, described glue pot also disposes vacuum extractor, attemperating unit and water replanishing device.
Plant capsule production system of the present utility model, dry section and operating space isolate setting mutually, can guarantee each required cleanliness factor in zone, and improve and dip in the colloid amount, energy efficient, and provide comfortable working environment for operator.
In should be understood that in this utility model scope, above-mentioned each technical characterictic of the present utility model and can making up mutually between specifically described each technical characterictic in below (eg embodiment), thus consist of new or preferred technical scheme.As space is limited, this tired stating no longer one by one.
Description of drawings
Fig. 1 is the structural representation in capsule manufacture of the present utility model workshop.
Fig. 2 is the structural representation of another optimal way in capsule manufacture of the present utility model workshop.
Fig. 3 is the structural representation of glue pot of the present utility model.
Fig. 4 is the structural representation of storage glue tank of the present utility model.
Specific implementation method
Inventor of the present utility model advanced further investigation, designed a kind of novel capsule manufacture workshop, and operating space and dry section are isolated setting mutually, can guarantee the cleanliness factor that each zone is required, improve and to dip in the colloid amount, energy efficient, and provide comfortable working environment for operator.
Below in conjunction with specific embodiment, further set forth this utility model.Should be understood that these embodiment only are used for explanation this utility model and are not used in the scope of the present utility model that limits.The experimental technique of unreceipted actual conditions in the following example is usually according to normal condition or the condition of advising according to manufacturer.
Unless otherwise defined, the same meaning that employed all specialties and scientific words and one skilled in the art are familiar with in the literary composition.In addition, any method similar or impartial to described content and material all can be applicable in this utility model method.The usefulness that better implementation method described in the literary composition and material only present a demonstration.
As used herein, " capsule manufacture system " has identical implication with " capsule manufacture workshop ", for the production of capsule, and plant capsule particularly.
As shown in Figure 1, capsule manufacture of the present utility model system comprises:
Dry section 3 is used for that the living embryo of capsule is carried out drying and obtains capsule;
Operating space 4, described operating space 4 and described dry section 3 separate mutual separation settings, and described operating space 3 interior placement glue dipping machines 5, the capsule that is made by glue dipping machine 5 are given birth to embryo and are delivered to dry section 3 and carry out drying.
The cleanliness factor of described operating space 4 is 300,000 grades, and temperature is 20 ~ 30 ℃.
The temperature of described dry section 3, humidity, cleanliness factor be significantly restriction not, adopts this area habitual temperature, humidity, cleanliness factor to get final product.
Dry section of the present utility model 3 keeps separating with operating space 4, and the wet steam of the dry heat that produces is without the operating space 4, directly discharge by dry section 3, and the retaining zone cleaning is when satisfying job requirement, for operator provide comfortable working environment.
Dry section 3 of the present utility model and operating space 4 separate mutual separation settings, isolation arranges mutually, does not refer to that dry section 3 does not communicate fully with operating space 4.For example, described dry section 3 and operating space 4 are in the same Factory Building, separate mutually by cutting off 10 each other, cut off the 10 door (not shown) that are provided with for personnel's turnover.For another example, described dry section 3 is with in operating space 4 is in different adjacent Factory Buildings, and dry section 3 and operating space 4 are separated mutually by the wall between two Factory Buildings, and door is set on the wall.Door is when closing, and dry section 3 is mutually separated with operating space 4 and arranged, and when door was opened, the staff can be from the operating space 4 enters dry section 3 and carries out equipment inspection or observation etc.
Be provided with drying equipment 7 in the dry section 3; 4 entrances that are provided with drying equipment 7 in the operating space; give birth to embryo is delivered to dry section 3 by conveyer belt 6 together with capsule die drying equipment 7 by the capsule that glue dipping machine 5 makes; after the living embryo of capsule is dried in drying equipment 7; return to operating space 4 by conveyer belt 6; thereby send into and carry out stripping operation in the capsule withdrawing pattern machine 20 and make finished capsule product, centrally do not need the workman manually to transport and arrange etc.Preferably, conveyer belt 6 is arranged in the casing of sealing, guarantees that capsule is given birth to embryo, finished capsule product can not be exposed in the external environment in course of conveying.
Further, adopting the method such as pipeline suction that finished capsule product is delivered to the check district tests.
The preferred drying equipment 7 of this utility model is dry kiln.The living embryo of capsule enters on the conveyer belt of drying equipment 7 from entrance automatically together with capsule die after dipping in glue, and the process up and down back and forth conveying of 4-6 layer is dried.
In a preferred implementation of the present utility model, glue dipping machine 5 comprises:
Dip in the glue groove, described dipping in the glue groove is equipped with colloid solution, and the described glue groove periphery of dipping in arranges the laminar flow hood that can open, is used for keeping dipping in the required temperature of glue, humidity and cleanliness factor, to satisfy the demand of dipping in glue work, ensures the colloid amount of dipping in;
Capsule die, described capsule die dip the described colloid solution that dips in the glue groove and form the living embryo of capsule.
Glue dipping machine 5 of the present utility model also comprises control system, and the colloid solution that dips in the glue groove by control system regulation and control capsule die forms the living embryo of capsule.
Describedly dip in glue groove top, can be become by the zone of sealing that described laminar flow hood is shrouded and dip in Jiao Qu, cleanliness factor is 300,000 grades, and temperature is 60-80 ℃, and humidity is 60-80%.The technical staff can dip in according to the big or small corresponding adjustment of dipping in the glue groove area of Jiao Qu.
In addition, because the space in the laminar flow hood is less, be conducive to energy-conservation and control environmental index.
Operator can observe and control operation across laminar flow hood, also can open in case of necessity laminar flow hood or enter work in the space that laminar flow hood seals.
Capsule manufacture of the present utility model system; the placement location of capsule withdrawing pattern machine 20 in operating space 4 do not have special requirement; preferably; in operating space 4; capsule withdrawing pattern machine 20 is placed on and dips in glue district below, is convenient to the capsule die that removes and sends into through the conveying runner of glue dipping machine 5 preparations and dip in the circulation of glue groove and dip in glue from capsule withdrawing pattern machine 20.
As shown in Figure 2, described capsule manufacture system also comprises colloidal sol district 9, with described operating space 4, dry section 3 separate settings, described colloidal sol district 9 interior placement glue pots 1, is used for preparation colloid solution; Described glue pot 1 comprises tank body and the cover that covers on described tank body, on the described cover charge door is set, and described tank body lower part arranges discharging opening, and described tank interior is provided with homogenizer.
The cleanliness factor in described colloidal sol district 9 is 300,000 grades, and temperature is 20-30 ℃, and humidity is 45-55%.
Also arrange by Material Staging Area 8 in the described colloidal sol district 9, be used for preparing, depositing the raw material that the preparation capsule is used.
In another preference, as shown in Figure 3, glue pot 1 comprises tank body 15, and is arranged on the cover 11 of tank body 15 upper ends.Charging aperture 13 is set on the described cover, and raw material enters into the inside of described tank body 15 through charging aperture 13.Described tank body 15 inner preparation homogenizer 17 and stirring paddles 16, described homogenizer 17 and stirring paddle 16 drive running by the motor 14 that described cover 11 upper ends arrange.In addition, described glue pot 1 is also prepared vacuum extractor, by carrying out evacuation in the logical pressure mouthful 12 pairs of tank bodies 15 that arrange on the described cover 11.Discharging opening 19 is arranged on the lower end of described tank body 15.
Further, also are furnished with intervalometer, online viscosity determinator, sight glass etc. on the described glue pot 1.
Homogenizer 17 is the high speed homogenization device, and maximum speed reaches 8000rpm, through 20-120 minute stirring, can make the abundant homogenize of raw material, refinement under 30-90 ℃ of temperature, and is fused to single structure with water in extremely trickle pearl base structure.
In another preference, described homogenizer rotating speed is 500-8000rpm.
Described vacuum extractor can be got rid of the bubble in the colloid solution to carrying out evacuation in the tank body 15, and pressure is 0.7 ~ 1 normal atmosphere.
Described glue pot 1 is also prepared automatic feeding device, and raw material joins the inside of described tank body 15 automatically by charging aperture 13, and the charging rate scalable.
Described glue pot 1 is also prepared the supercharging drawing mechanism, and by carrying out supercharging in the logical pressure mouthful 12 pairs of tank bodies 15 that arrange on the described cover 11, colloid solution flows out through discharging opening 19 and enters into described storage glue tank 2.
Described glue pot 1 is also prepared attemperating unit, and the periphery of described tank body 15 arranges temperature control layer 18, and the temperature in the tank body 15 is controlled at 0-100 ℃.
Described glue pot 1 also can be prepared water replanishing device, by carrying out moisturizing in 13 pairs of tank bodies 15 of charge door.
In another preference, described capsule manufacture system also is provided with storage glue tank, in the described storage glue tank colloid solution is housed.
As shown in Figure 4, described storage glue tank 2 comprises tank body 25, and is arranged on the cover 21 of tank body 25 upper ends.Water supplement port 13 is set on the described cover.Described tank body 15 inner preparation stirring paddles 26, the blade of stirring paddle 26 is positioned at the bottom of described tank body 25, motor 24 driven rotary that described stirring paddle 26 arranges by described cover 21 upper ends.Discharging opening 29 is arranged on the lower end of described tank body 25.
Colloid solution is delivered to the described glue groove that dips in by the sebific duct that goes out that is arranged on discharging opening 29 and dip between the glue groove.
Described storage glue tank 2 is also prepared attemperating unit, and the periphery of described tank body 25 arranges temperature control layer 28, and the temperature of tank body 25 interior materials is controlled at 55-80 ℃, is preferably 60-75 ℃.
Described storage glue tank 2 can be prepared water replanishing device, by carrying out moisturizing in 23 pairs of tank bodies 25 of water supplement port.
Go out sebific duct and also can be used for prison and detect the flow of regulating colloid solution with the sensor of measuring flow and moisture, the moisture in the monitoring colloid solution when moisture reduces, starts water replanishing device, by the 25 interior moisturizings of water supplement port 23 phase tank bodies.
In another preference, described storage glue tank 2 inside are provided with the defoamer Drop-adding device.
When storage glue tank 2 is placed on colloidal sol district 9, after colloid solution is prepared in glue pot 1 and is finished, from discharging opening 19 by the closed conduit storage glue tank 2 of packing into, the storage glue tank 2 that colloid solution is housed betransported sends into operating space 4, place the top of dipping in the glue groove, be preferably oblique upper, colloid solution is delivered to the described glue groove that dips in by the sebific duct that goes out that is arranged on storage glue tank 2 discharging openings 29 and dip between the glue groove, dips in glue and forms the living embryo of capsule.
In another preference, colloidal sol district 9, operating space 4 are arranged in the Factory Building, consist of intensive system, glue pot 1 discharging opening 19 is connected by the storage glue tank 2 that utilidor and operating space 4 are built in the top of dipping in the glue groove, the realization channelization is produced, and can save colloid solution is preserved transportation through storage glue tank 2 step.
The area of described operating space 4 accounts for the 15-25% of described capsule manufacture system area; The area of described dry section 3 accounts for the 50-60% of described capsule manufacture system area; Described colloidal sol district 9 accounts for the 25-35% of described capsule manufacture system area.
Capsule manufacture of the present utility model system in use, at Material Staging Area 8 the gellan gum raw material is mixed and to reach evenly, charging aperture 13 by glue pot 1 slowly joins in the deionized water of inside of described tank body 15, intensification, stirring are carried out high speed homogenization after reaching 80 ℃ to 100 ℃, rotating speed 2000-6000rpm continues 10-30 minute.Middling speed stirs, and speed 500-1500rpm continues 10-30 minute.Keep mixing speed, hydroxypropyl emthylcellulose HPMC is slowly added continuously by the charging aperture 13 of glue pot 1, stirring at low speed after HPMC all adds, speed 20-60rpm, temperature is down to about 70 ℃, keeps 20-60 minute.
Adopt vacuum extractor, by carrying out evacuation in the logical pressure mouthful 12 pairs of tank bodies 15 that arrange on the described cover 11.After removing the bubble in the tank body 15 internal sizes liquid solutions, colloid solution enters storage glue tank 2 by discharging opening 19, in the operating space 4, storage glue tank 2 is in 65-75 ℃ of insulation, colloid solution is put into by the discharging opening 29 of storage glue tank 2 and is dipped in the glue groove, dips in glue, makes hollow plant gum Tibetan household slave embryo, be conveyed into subsequently dry section 3 and carry out dried, form hollow plant capsule.
Above embodiment has exemplified the preferred capsule manufacture of this utility model system.Capsule manufacture of the present utility model system can have several (being preferably 1-4) operating spaces, dry section and colloidal sol district, operating space and dry section can be arranged in the same delivery room, in same or different colloidal sol districts, configure colloid solution, carry to the storage glue tank of operating space.
Usefulness of the present utility model is:
(1) zone isolates mutually, has guaranteed the different demands of each zone to cleanliness factor, temperature and humidity;
(2) operating space is separated mutually with dry section, and the wet steam of the dry heat that produces directly discharges without the operating space;
(3) reduce temperature, the humidity of operating space, improved workman's operational comfort;
(4) reduce the temperature in operating space and colloidal sol district, saved energy consumption;
(5) guarantee to dip in glue district scope interior temperature, humidity, improve the colloid amount of dipping in;
(6) intensive workshop provides possibility for producing channelization;
(7) dip in glue groove periphery laminar flow hood is set, keep required temperature, humidity and cleanliness factor, to satisfy the demand of dipping in glue work.
The above-mentioned feature that this utility model is mentioned, or the feature that embodiment mentions can combination in any.All features that this case description discloses can with any composition forms and usefulness, each feature that discloses in the description can be replaced by any alternative characteristics of identical, impartial or similar purpose that provides.Therefore except special instruction is arranged, the feature that discloses only is the general example of equalization or similar features.
All quote in this application as a reference at all documents that this utility model is mentioned, just as each piece document is quoted separately as a reference.Should be understood that in addition those skilled in the art can make various changes or modifications this utility model after having read above-mentioned teachings of the present utility model, these equivalent form of values fall within the application's appended claims limited range equally.
Claims (10)
1. a plant capsule production system is characterized in that, comprising:
Dry section is used for that the living embryo of capsule is carried out drying and obtains capsule;
The operating space, the separate mutual separation setting of described operating space and described dry section, and place glue dipping machine in the described operating space, the capsule that is made by glue dipping machine is given birth to embryo and is delivered to dry section and carry out drying.
2. plant capsule production system as claimed in claim 1 is characterized in that, the cleanliness factor of described operating space is 300,000 grades, and temperature is 20 ~ 30 ℃.
3. plant capsule production system as claimed in claim 1 is characterized in that, described glue dipping machine comprises:
Dip in the glue groove, the described in-built colloid solution that is useful on the preparation plant capsule of glue groove that dips in, the described glue groove periphery of dipping in arranges the laminar flow hood that can open;
Capsule die, described capsule die dip the described colloid solution that dips in the glue groove and form plant gum Tibetan household slave embryo.
4. plant capsule production system as claimed in claim 3 is characterized in that, describedly dips in glue groove top, is 300,000 grades by the regional cleanliness factor of sealing that described laminar flow hood is shrouded, and temperature is 60-80 ℃, and humidity is 60-80%.
5. plant capsule production system as claimed in claim 3, it is characterized in that, described operating space also is provided with storage glue tank, in the described storage glue tank colloid solution is housed, during use, described storage glue tank places to dip in above the glue groove and by pipeline liquid injecting device and is connected with the described glue groove that dips in, and described colloid solution enters into described dipping in the glue groove by described closing pipe line;
The described preparation of storage glue tank water replanishing device, agitating device and attemperator remain on 55-80 ℃ with the temperature of storing up the colloid solution in the glue tank.
6. such as each described plant capsule production system of claim 1 ~ 5, it is characterized in that, described capsule manufacture system also comprises the colloidal sol district, places glue pot in the described colloidal sol district, is used for the colloid solution of preparation preparation plant capsule; Described glue pot comprises tank body and the cover that covers on described tank body, on the described cover charge door is set, and described tank body lower part arranges discharging opening, and described tank interior is provided with homogenizer.
7. plant capsule production system as claimed in claim 6 is characterized in that, the cleanliness factor in described colloidal sol district is 300,000 grades, and temperature is 20-30 ℃, and humidity is 45-55%.
8. plant capsule production system as claimed in claim 6 is characterized in that, the area of described operating space accounts for the 15-25% of described plant capsule production system area; The area of described dry section accounts for the 50-60% of described plant capsule production system area; Described colloidal sol district accounts for the 25-35% of described plant capsule production system area.
9. plant capsule production system as claimed in claim 6 is characterized in that, the discharging opening of described glue pot is connected with storage glue tank by pipeline.
10. plant capsule production system as claimed in claim 6 is characterized in that, described glue pot also disposes vacuum extractor, attemperating unit and water replanishing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220439471 CN202740408U (en) | 2012-08-30 | 2012-08-30 | Capsule production workshop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220439471 CN202740408U (en) | 2012-08-30 | 2012-08-30 | Capsule production workshop |
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| Publication Number | Publication Date |
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| CN202740408U true CN202740408U (en) | 2013-02-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220439471 Expired - Fee Related CN202740408U (en) | 2012-08-30 | 2012-08-30 | Capsule production workshop |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103735416A (en) * | 2013-10-28 | 2014-04-23 | 山东永春堂集团有限公司 | Capsule low-temperature filling method and special capsule filling chamber |
| CN109159312A (en) * | 2018-09-03 | 2019-01-08 | 昆山市石智电子科技有限公司 | It is a kind of for producing the solf device and sol gel process of plant capsule |
| CN117111664A (en) * | 2023-10-25 | 2023-11-24 | 江苏辰星药业股份有限公司 | Environment control method and system for storing plant empty capsules |
-
2012
- 2012-08-30 CN CN 201220439471 patent/CN202740408U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103735416A (en) * | 2013-10-28 | 2014-04-23 | 山东永春堂集团有限公司 | Capsule low-temperature filling method and special capsule filling chamber |
| CN103735416B (en) * | 2013-10-28 | 2017-02-01 | 山东永春堂集团有限公司 | Capsule low-temperature filling method and special capsule filling chamber |
| CN109159312A (en) * | 2018-09-03 | 2019-01-08 | 昆山市石智电子科技有限公司 | It is a kind of for producing the solf device and sol gel process of plant capsule |
| CN109159312B (en) * | 2018-09-03 | 2021-05-18 | 昆山市石智电子科技有限公司 | Sol device and sol method for producing plant capsules |
| CN117111664A (en) * | 2023-10-25 | 2023-11-24 | 江苏辰星药业股份有限公司 | Environment control method and system for storing plant empty capsules |
| CN117111664B (en) * | 2023-10-25 | 2023-12-26 | 江苏辰星药业股份有限公司 | Environment control method and system for storing plant empty capsules |
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Granted publication date: 20130220 Termination date: 20200830 |