CN103182196A - High pressure drug extraction system - Google Patents
High pressure drug extraction system Download PDFInfo
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- CN103182196A CN103182196A CN201110458221XA CN201110458221A CN103182196A CN 103182196 A CN103182196 A CN 103182196A CN 201110458221X A CN201110458221X A CN 201110458221XA CN 201110458221 A CN201110458221 A CN 201110458221A CN 103182196 A CN103182196 A CN 103182196A
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Abstract
The invention relates to the field of pharmaceutical equipment, and relates to an extraction system. A high pressure drug extraction system comprises a support, a tank body disposed on the support, a mist eliminator, a condenser, a cooler, a reduced pressure refluxing tank and a high pressure air pump, wherein the tank body is divided into an upper tank body and a lower tank body; a filter device is disposed between the upper tank body and the lower tank body; the high pressure air pump is communicated with the upper tank body; and the upper tank body is provided with a mashing device. Due to the adoption of the above technical solution, drugs are mashed in advance and effective components in the drugs can be dissolved in a solvent faster by a high pressure and low temperature heating mode, thereby shortening immersion time of the drugs.
Description
Technical field
The present invention relates to a kind of pharmaceutical equipment field, be specifically related to a kind of extraction system.
Background technology
In pharmacy procedure, the raw-material extraction of Chinese medicine is one of Chinese medicine pretreatment procedure of producing most critical, operations such as the extraction precision of its treatment process will directly have influence on and follow-uply concentrate, separation and purification.
Present most of producer all adopts the constant-pressure and high-temperature extraction process, this extraction process not only needs to soak medicinal material early stage, prolong the pretreatment procedure time, and under this constant-pressure and high-temperature state, thermal sensitivity active ingredient is destroyed many, invalid macromolecular substances easier with bring in the extract, this makes that follow-up separation and purification is long in time limit, the solvent consume is big, not only reduced virtually extract quality and also improved the raw-material wastage of Chinese medicine, so cause the medicinal material cost of manufacture to rise, the drainage of the Chinese medicine of waste also can affect to environment, can not satisfy people to economic benefit, the double requirements of environmental protection.
Summary of the invention
The objective of the invention is to, provide a kind of high pressure medicine extraction system, to address the above problem.
Technical problem solved by the invention can realize by the following technical solutions:
A kind of high pressure medicine extraction system comprises that a support, is positioned at the tank body on the described support, it is characterized in that described tank body is divided into a upper tank body, a lower tank, is provided with a filter between described upper tank body and the described lower tank;
Also comprise a high-pressure pump, described high-pressure pump is communicated with described upper tank body, is provided with a crushing apparatus in the described upper tank body.
The present invention mixes device by described the blending of high-speed rotation, medicinal material in the described upper tank body is blended into concoction with solvent, described high-pressure pump pressurizes to the air in the described upper tank body subsequently, forces the concoction of active ingredient to flow in the lower tank by described filter.
Described crushing apparatus comprises a dynamical system, at least two blades, a turning cylinder, and described vanes fixed is connected on the described turning cylinder, and described turning cylinder connects described dynamical system, and described dynamical system connects a microprocessor system.
Be provided with a heater in the described upper tank body, described heater connects described crushing apparatus, and described heater is the blade heating of described crushing apparatus, when making described crushing apparatus blend medicinal material, heat for solvent together, the active ingredient of being convenient to medicinal material fully is dissolved in the solvent.
Described heater connects described microprocessor system, the heating maximum temperature scope of described heater is 45-80 ℃, in order to be dissolved in solvent by accelerating medicament active ingredient to the method for medicinal material heating, reduce extraction time, in addition in this temperature range, because the active ingredient of temperature survivable thermal sensitivity on the low side highland medicinal material.
Described filter comprises a valve, a filter core excessively, described filter core excessively is positioned at the below of described valve, described valve connects described upper tank body lower end, is provided with a sealing ring between described valve and the described upper tank body, and the control end of described valve connects described microprocessor system.
The described filter core of crossing comprises a screen pack group, at least one filter membrane, is provided with described filter membrane below the reverse osmosis membrane, described screen pack, and described filter membrane lower end is provided with described reverse osmosis membrane.
Described screen pack group comprises at least one high efficiency particulate air, and the aperture of described high efficiency particulate air is the 0.1-0.25 micron, the screen pack that described screen pack can adopt glass fibre to make.
Described high-pressure pump is positioned at the top of described upper tank body, described high-pressure pump connects described microprocessor system, described high-pressure pump and described upper tank body junction are provided with a photocatalyst device, and described photocatalyst device comprises a photocatalyst filtering net, at least one light source for the described photocatalyst filtering net of irradiation.Described light source adopts the ultraviolet ultraviolet lamp of emission.
Described upper tank body top is provided with a charging aperture, described charging aperture is provided with a seal cover, the top of described seal cover is provided with a drain tap, the control end of described seal cover, described drain tap connects described microprocessor system, when described upper tank body internal gas pressure was too high, described microprocessor system regulated the air pressure in the described upper tank body by described drain tap.
Described seal cover issues and is provided with a ultraviolet ray generating apparatus, and described ultraviolet ray generating apparatus connects described microprocessor system; Described ultraviolet ray generating apparatus in the form of a ring, the transmitting terminal that takes place of described ultraviolet ray towards described charging aperture.
Also comprise a temperature sensor, baroceptor, described temperature sensor, baroceptor connect described microprocessor system, and described temperature sensor is positioned at the inwall bottom of described upper tank body, and described baroceptor is positioned at the upper inside wall of described upper tank body.
Described microprocessor system links a wireless communication module, described microprocessor system connects a calculator by described wireless communication module, described calculator carries out control operation in the help of described wireless communication module to described microprocessor system, temperature to described heater arranges, and according to described temperature sensor, the measured data of baroceptor described high-pressure pump is regulated and control.
Beneficial effect: owing to adopt technique scheme, the present invention formerly blends medicinal material, and by the mode that high pressure low temperature heats, the active ingredient in the medicinal material is dissolved in the solvent faster, has reduced the time that medicinal material soaks.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present invention;
Fig. 2 is partial structurtes schematic diagram of the present invention.
The specific embodiment
For technological means, creation characteristic that the present invention is realized, reach purpose and effect is easy to understand, further set forth the present invention below in conjunction with concrete diagram.
With reference to Fig. 1, Fig. 2, a kind of high pressure medicine extraction system comprises that a support, is positioned at the tank body 1 on the support, and tank body 1 is divided into a upper tank body 11, a lower tank 12, is provided with a filter 51 between upper tank body 11 and the lower tank 12; Also comprise a high-pressure pump 7, high-pressure pump 7 is communicated with upper tank body 11, is provided with a crushing apparatus 51 in the upper tank body 11.The present invention blends by high-speed rotation and mixes device, and the medicinal material in the upper tank body is blended into concoction with solvent, and high-pressure pump pressurizes to the air in the upper tank body subsequently, forces the concoction of active ingredient to flow in the lower tank by filter.
Crushing apparatus 52 comprises a dynamical system, at least two blades, a turning cylinder, and vanes fixed is connected on the turning cylinder, and turning cylinder connects dynamical system, and dynamical system connects a microprocessor system.Be provided with a heater in the upper tank body 11, heater 53 connects crushing apparatus, and heater 53 is the blade heating of crushing apparatus 52, when making crushing apparatus 53 blend medicinal material, heat for solvent together, the active ingredient of being convenient to medicinal material fully is dissolved in the solvent.In addition, heater 53 connects the microprocessor system, the heating maximum temperature scope of heater 53 is 45-80 ℃, in order to be dissolved in solvent by accelerating medicament active ingredient to the method for medicinal material heating, reduce extraction time, in addition in this temperature range, because the active ingredient of temperature survivable thermal sensitivity on the low side highland medicinal material.
High-pressure pump 7 is positioned at the top of upper tank body 11, high-pressure pump 7 connects the microprocessor system, high-pressure pump 7 is provided with a photocatalyst device with upper tank body 11 junctions, and photocatalyst device comprises a photocatalyst filtering net, at least one light source for the irradiates light catalyst filter screen.Light source adopts the ultraviolet ultraviolet lamp of emission.
Filter 51 comprises a valve, a filter core excessively, crosses the below that filter core is positioned at valve, and valve connects the upper tank body lower end, is provided with a sealing ring between valve and the upper tank body, and the control end of valve connects the microprocessor system.Cross filter core and comprise a screen pack group, at least one filter membrane, be provided with filter membrane below the reverse osmosis membrane, screen pack, the filter membrane lower end is provided with reverse osmosis membrane.The screen pack group comprises at least one high efficiency particulate air, and the aperture of high efficiency particulate air is the 0.1-0.25 micron, the screen pack that screen pack can adopt glass fibre to make.
Upper tank body 11 tops are provided with a charging aperture, charging aperture is provided with a seal cover 13, the top of seal cover is provided with a drain tap 8, the control end of seal cover 13, drain tap 8 connects the microprocessor system, and when seal cover 13 was closed, drain tap 8 temporary transient maintenances were closed, after treating that upper tank body 11 interior gases begin to reach certain value, under the control of microprocessor system, open drain tap 8, by cooperating of drain tap 8 and high-pressure pump, the air pressure in the upper tank body 11 are remained in the certain value.Seal cover 13 issues and is provided with a ultraviolet ray generating apparatus 54, ultraviolet ray generating apparatus 54 in the form of a ring, ultraviolet ray 54 transmitting terminal takes place towards charging aperture, ultraviolet ray generating apparatus 54 connects the microprocessor systems.The moment that seal cover 13 is opened, ultraviolet ray generating apparatus 54 is opened under the control of microprocessor simultaneously, for dropping into the sterilization that carries out disinfection of medicinal materials in the upper tank body 11.
Also comprise a temperature sensor, baroceptor, temperature sensor, baroceptor connect the microprocessor system, and temperature sensor is positioned at the inwall bottom of upper tank body 12, and baroceptor is positioned at the upper inside wall of upper tank body 12.The microprocessor system records data by temperature sensor, baroceptor, regulates the switch of high-pressure pump 7, drain tap 8, and the heating power of control heater 53, avoids the air pressure in the mountain tank body 11 and temperature is too high or low excessively.
The microprocessor system links a wireless communication module, the microprocessor system connects a calculator by wireless communication module, calculator carries out control operation in the help of wireless communication module to the microprocessor system, realize the purpose that full-automatic wireless is controlled, also be convenient to monitor in real time extraction state in the tank body.
More than show and described basic principle of the present invention and principal character and advantage of the present invention.The technical staff of the industry should understand; the present invention is not restricted to the described embodiments; that describes in above-described embodiment and the specification just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.The claimed scope of the present invention is defined by appending claims and equivalent thereof.
Claims (10)
1. a high pressure medicine extraction system comprises that a support, is positioned at the tank body on the described support, it is characterized in that described tank body is divided into a upper tank body, a lower tank, is provided with a filter between described upper tank body and the described lower tank;
Also comprise a high-pressure pump, described high-pressure pump is communicated with described upper tank body, is provided with a crushing apparatus in the described upper tank body.
2. high pressure medicine extraction system according to claim 1, it is characterized in that: described crushing apparatus comprises a dynamical system, at least two blades, one turning cylinder, described vanes fixed is connected on the described turning cylinder, described turning cylinder connects described dynamical system, and described dynamical system connects a microprocessor system.
3. high pressure medicine extraction system according to claim 2, it is characterized in that: be provided with a heater in the described upper tank body, described heater connects described crushing apparatus, described heater is the blade heating of described crushing apparatus, when making described crushing apparatus blend medicinal material, heat for solvent together;
Described heater connects described microprocessor system, and the heating maximum temperature scope of described heater is 45-80 ℃.
4. high pressure medicine extraction system according to claim 3, it is characterized in that: described filter comprises a valve, a filter core excessively, described filter core excessively is positioned at the below of described valve, described valve connects described upper tank body lower end, be provided with a sealing ring between described valve and the described upper tank body, the control end of described valve connects described microprocessor system.
5. high pressure medicine extraction system according to claim 4, it is characterized in that: the described filter core of crossing comprises a screen pack group, at least one filter membrane, be provided with described filter membrane below one reverse osmosis membrane, described screen pack, described filter membrane lower end is provided with described reverse osmosis membrane.
Described screen pack group comprises at least one high efficiency particulate air, and the aperture of described high efficiency particulate air is the 0.1-0.25 micron, the screen pack that described screen pack is made with glass fibre.
6. high pressure medicine extraction system according to claim 5, it is characterized in that: described high-pressure pump is positioned at the top of described upper tank body, described high-pressure pump connects described microprocessor system, described high-pressure pump and described upper tank body junction are provided with a photocatalyst device, and described photocatalyst device comprises a photocatalyst filtering net, at least one light source for the described photocatalyst filtering net of irradiation;
Described light source adopts the ultraviolet ultraviolet lamp of emission.
7. high pressure medicine extraction system according to claim 6, it is characterized in that: described upper tank body top is provided with a charging aperture, described charging aperture is provided with a seal cover, the top of described seal cover is provided with a drain tap, and the control end of described seal cover, described drain tap connects described microprocessor system;
Described seal cover issues and is provided with a ultraviolet ray generating apparatus, and described ultraviolet ray generating apparatus connects described microprocessor system, described ultraviolet ray generating apparatus in the form of a ring, the transmitting terminal that takes place of described ultraviolet ray towards described charging aperture.
8. high pressure medicine extraction system according to claim 7, it is characterized in that: also comprise a mist eliminator, a condenser, a cooler, a reduced-pressure backflow jar, described mist eliminator, condenser, cooler, reduced-pressure backflow jar connect successively, described mist eliminator, reduced-pressure backflow jar connect described lower tank respectively, described lower tank bottom is provided with a discharging opening, and described discharging opening is provided with a discharging valve;
The sidewall of described lower tank is communicated with described mist eliminator, and described mist eliminator connects described condenser, and described condenser connects described cooler, and described cooler connects described reduced-pressure backflow jar, and described reduced-pressure backflow jar is communicated with the sidewall of described lower tank;
Respectively be provided with a controlled valve between described lower tank and described mist eliminator, the described reduced-pressure backflow jar, the control end of described controlled valve connects described microprocessor system.
9. high pressure medicine extraction system according to claim 8, it is characterized in that: also comprise a temperature sensor, baroceptor, described temperature sensor, baroceptor connect described microprocessor system, described temperature sensor is positioned at the inwall bottom of described upper tank body, and described baroceptor is positioned at the upper inside wall of described upper tank body.
10. high pressure medicine extraction system according to claim 1 is characterized in that: described microprocessor system links a wireless communication module, and described microprocessor system connects a calculator by described wireless communication module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110458221.XA CN103182196B (en) | 2011-12-31 | 2011-12-31 | A kind of High pressure drug extraction system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110458221.XA CN103182196B (en) | 2011-12-31 | 2011-12-31 | A kind of High pressure drug extraction system |
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| CN103182196A true CN103182196A (en) | 2013-07-03 |
| CN103182196B CN103182196B (en) | 2016-04-20 |
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| CN201110458221.XA Active CN103182196B (en) | 2011-12-31 | 2011-12-31 | A kind of High pressure drug extraction system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112870750A (en) * | 2021-01-21 | 2021-06-01 | 广西六万山生物科技有限公司 | Distillation retort for leaching effective components of plants and application method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2792590Y (en) * | 2005-06-17 | 2006-07-05 | 苏州市兴科现代中药工艺装备开发有限公司 | Plant effective ingredient extracting separator |
| CN201470150U (en) * | 2009-07-29 | 2010-05-19 | 南京中医药大学 | Integrated microwave extraction-ultrafiltration membrane separator for purification of Chinese traditional medcine |
| CN202044951U (en) * | 2011-03-22 | 2011-11-23 | 湖北中烟工业有限责任公司 | Efficient extracting device for extracting active ingredients of plants |
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2011
- 2011-12-31 CN CN201110458221.XA patent/CN103182196B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2792590Y (en) * | 2005-06-17 | 2006-07-05 | 苏州市兴科现代中药工艺装备开发有限公司 | Plant effective ingredient extracting separator |
| CN201470150U (en) * | 2009-07-29 | 2010-05-19 | 南京中医药大学 | Integrated microwave extraction-ultrafiltration membrane separator for purification of Chinese traditional medcine |
| CN202044951U (en) * | 2011-03-22 | 2011-11-23 | 湖北中烟工业有限责任公司 | Efficient extracting device for extracting active ingredients of plants |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112870750A (en) * | 2021-01-21 | 2021-06-01 | 广西六万山生物科技有限公司 | Distillation retort for leaching effective components of plants and application method thereof |
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| CN103182196B (en) | 2016-04-20 |
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Effective date of registration: 20230901 Address after: Building 2, No. 3398, Puwei Road, Fengxian District, Shanghai, 200000 Patentee after: Shanghai Pibao Biotechnology Development Co.,Ltd. Address before: 201415 No.8 Juting Road, Zhuanghang European Industrial Park, Fengxian District, Shanghai Patentee before: SHANGHAI JINPIBAO PHARMACEUTICAL Co.,Ltd. |