CN2196504Y - High-efficient low-consumption extraction machine - Google Patents
High-efficient low-consumption extraction machine Download PDFInfo
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- CN2196504Y CN2196504Y CN 93209708 CN93209708U CN2196504Y CN 2196504 Y CN2196504 Y CN 2196504Y CN 93209708 CN93209708 CN 93209708 CN 93209708 U CN93209708 U CN 93209708U CN 2196504 Y CN2196504 Y CN 2196504Y
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Abstract
The utility model relates to a high-efficiency low-consumption extraction machine which is used for strengthening the extraction effect of animals and plants (mainly the traditional Chinese medicine). A device having the functions of synchronous operation of boiling, reflux, concentration, distillation, and fractional distillation is composed of an extracting tank, a thin-film evaporator, a stirring thin-film evaporator, a medical liquid storage tank, a condenser, an oil-water separator, an alcohol gravity tank, an alcohol recovery tower, an alcohol storage tank, etc. which are successively connected and communicated through pipes and valves. The machine has sharing devices, high efficiency, energy saving, time saving, low consumption, high yield, and big concentration ratio; the utility model is an ideal extraction device for the effective components of medicinal material and the nutrient components of food in the unit, such as the hospital pharmaceutical production laboratory, the laboratory, the teaching, the scientific research, the factory, etc.
Description
This utility model relates to extraction process equipment (instrument) category of animals and plants (mainly being Chinese crude drug).
The example that is extracted as with Chinese medicine describes below:
Method and relevant device that equal segments processing is produced are all adopted and decoct, concentrate, reclaim in the Chinese medicine of hospital, pharmaceutical factory processing at present.From existing technical data retrieval as can be known: above-mentioned processing, research, production process, do not see a kind of perfect knockdown Chinese medicine course of processing that can make as yet and neither lose effective ingredient, the equipment of coherent one that again can time-saving energy-saving, thereby difficult quality is guaranteed in more existing Chinese crude drug courses of processing, and medical material, ethanol waste are a lot.In order to solve above-mentioned difficulties, the inventor has applied for the boil medicine utility model of (extraction) machine of relevant multi-functional Chinese medicine, and application number is 90216490.2, letters patent book number is 94473, this machine simplicity of design only is fit to hospital and is not suitable for pharmaceutical factory production, and also do not reach the efficient low-consume requirement.
Accompanying drawing 1 is for forming the structural representation of efficient low-consume extractor of the present utility model: extraction pot 1, filter 2, magnetic drive pump 3, membrane evaporator 4, vapour liquid separator 5, agitated thin-film evaporator 6, medicinal liquid basin 7,8, condenser 9, oil water separator 10, ethanol gravity tank 11, alcohol distillation column 12, cooler 13, ethanol basin 14, self priming centrifugal pump 15, hydraulic ejector 16, circulating water pool 17, centrifugal pump 18, by pipeline, valve successively in succession, interpenetrating forms a whole.
Extraction cover of the present utility model, be connected with cylindrical shell by flange, it is reinforced to open the back, three apertures are arranged at the top of extraction pot 1, one is connected with drain pipe by pipeline, allow the medicinal liquid inflow filter, another aperture can be connected with alcohol distillation tower 12 bottoms with condenser 9 by pipeline, can allow and wherein evaporate gas and enter respectively wherein, the 3rd aperture is connected with the venthole of vaporizer by pipeline, allow its evaporation vapour enter wherein or to discharge, one passageway is arranged at extraction pot 1 bottom, have an aperture on the passageway, can allow it enter heating with the boiler steam pipe connection by pipeline, another aperture is a sewage draining exit, the lower end of extraction pot 1 has three apertures, an aperture is by pipeline and membrane evaporator, the steam port that goes out of agitated thin-film evaporator connects, can allow the gas of its two equipment evaporation enter extraction pot 1, another aperture is by pipeline and oil water separator liquid outlet, and gravity tank bottom liquid outlet connects, and allows its liquid enter in the extraction pot 1, the 3rd aperture is connected with filter by pipeline, allow its medicinal liquid enter filter, blind flange is arranged at top, extraction pot lower end, can emit by medicinal residues by breakdown.
The inlet of magnetic drive pump 3 is connected by the bottom liquid outlet of pipeline with filter 2 and vapour liquid separator 5, and the liquid outlet of magnetic drive pump 3 is connected with the lower end liquid outlet of extraction pot 1 and the lower end of membrane evaporator 4 by pipeline, and liquid can be entered wherein respectively.
The lower end of membrane evaporator 4 has three apertures, wherein one of the top, lower end is connected with the liquid outlet of magnetic drive pump 3, but accelerated evaporation speed, two are respectively sewage draining exit and waste vapour outlet in addition, the upper end of membrane evaporator 4 has three apertures, wherein Shang Mian big aperture links to each other with vapour liquid separator 5 by pipeline, and another is connected with boiler evaporating vapour by pipeline, and the 3rd aperture is the waste vapour outlet.
The lower end of vapour liquid separator 5 has a liquid outlet, both can be connected the medicinal liquid that allows wherein with magnetic drive pump 3 by pipeline and enter evaporation in the membrane evaporator 4 once more, can allow medicinal liquid enter again and continue evaporation in the agitated thin-film evaporator 6, a venthole is arranged at the top of vapour liquid separator 5, can also can import alcohol distillation column 12 evaporation vapour input extraction pot 1 as the thermal source that extracts medicinal liquid by pipeline.
The upper end of agitated thin-film evaporator 6 has four apertures, one can be imported Boiler Steam as thermal source by pipeline, the evaporation vapour that also can import vapour liquid separator 5 is as thermal source, it two links to each other with the lower end liquid outlet of vapour liquid separator 5 by pipeline, the gas of its three evaporations in agitated thin-film evaporator 6 can be imported extraction pot 1, alcohol distillation column 12 by pipeline, it four exports as waste vapour, the lower end of agitated thin-film evaporator has three apertures, by pipeline concentrated medicament is imported medicinal liquid storage tank 7 first, in 8, second enter waste liquid, three exhaust waste steam.
Medicinal liquid basin 7, all there is heatable deflection plate medicinal liquid basin 8 inside, its top respectively has three apertures, big aperture, be the vapor opening mouth, be connected with agitated-film vaporizer gland steam exhauster by pipeline, medicinal liquid basin 7 another holes are the admission aperture, be connected with agitated thin-film evaporator lower end steam drain by pipeline, allow steam enter the deflection plate heating, the 3rd aperture is connected with agitated thin-film evaporator fluid aperture by pipeline, allow concentrated medicament enter wherein evaporation, medicinal liquid basin 8 the 3rd aperture is connected with medicinal liquid basin 7 liquid outlets by pipeline, allows concentrated medicament enter wherein and stores.Medicinal liquid basin 7,8, but the place, bottom has the hand hole visor of breakdown, can open after having operated and get it filled.
Respectively there are three apertures the both sides of condenser 9, condensed water is imported from the left end aperture, export from the right-hand end aperture, the top, right side is an air intake, the steam drain of the top by pipeline and alcohol distillation column 12, extraction pot 1 top, cooler 13, ethanol basin 14, ethanol gravity tank 11 links to each other, the below, right side is a sewage draining exit, the top, left side is a steam drain, be connected with hydraulic ejector 16 bleeding points by pipeline, the below, left side is the discharge opeing aperture, be connected with the control valve group with oil water separator 10 by pipeline, condensed fluid can be entered wherein respectively.
The upper end of oil water separator 10 has two apertures, and one links to each other with condenser 9 by pipeline, and another is the oil extraction aperture.The lower end has two apertures, one by pipeline to extraction pot 1 input condensed fluid solvent as a supplement, another is a sewage draining exit.
The upper end of ethanol gravity tank 11 has three apertures, and first links to each other with self priming centrifugal pump 15 by pipeline, input ethanol, and second is connected with running water pipe by pipeline, can introduce tap water, the 3rd admission aperture.The lower end of ethanol gravity tank 11 has an aperture, carries solvent by pipeline to extraction pot 1.
The lower end of alcohol distillation column 12 has an aperture, can link to each other with the upper end steam drain of extraction pot 1 by pipeline, also can be connected with the steam drain of vapour liquid separator 5, agitated thin-film evaporator 6, allow it extract the interior fractional distillation of vaporized alcohol gas input tower in later stage, the upper end of alcohol distillation column 12 has two apertures, vapour input condenser 9 will be evaporated by pipeline in one aperture, another aperture links to each other with spinner flowmeter with one group of control valve by pipeline, the ethanol liquid part of condensation in the condenser 9 is got back in the tower, and another part enters in the cooler 13.
Respectively there are three apertures the both sides of cooler 13, condensed water is imported from the left end aperture, export from the right-hand end aperture, aperture, top, left side is the steam discharge aperture, link to each other by the air intake of pipeline with condenser 9, aperture, below, left side is connected with ethanol basin 14 by pipeline, and aperture, top, left side is an inlet, be connected with the control valve group, aperture, below, right side is a sewage draining exit.
The lower end of ethanol basin 14 has an aperture, is connected by the inlet of pipeline with self priming centrifugal pump 15, makes a jar interior ethanol input ethanol gravity tank 11.The upper end of ethanol basin 14 has three apertures, first is connected by the liquid outlet of pipeline with self priming centrifugal pump 15, can make outside ethanol by in the self priming centrifugal pump 15 input jars, second is connected with cooler 13 by pipeline, allow refrigerative alcohol liquid enter in the jar, the 3rd aperture can link to each other with condenser 9 by pipeline, also as the steam discharge aperture.
The bleeding point of hydraulic ejector 16 is connected by the steam drain of pipeline with condenser 9, to reach above-mentioned each equipment decompression operation.
Be elaborated below in conjunction with accompanying drawing 1: smash Chinese medicine and put into extraction pot 1, add entry or ethanol, open 80 ℃ of steam and boil (or return and heat up in a steamer) after half an hour, start magnetic drive pump 3 and hydraulic ejector 16,1. medicinal liquid enters filter 2 by extraction pot 1 top liquid outlet through pipeline, then through magnetic drive pump 3,2. pipeline is passed to medicinal liquid membrane evaporator 4, medicinal liquid is subjected to that thermal evaporation is laggard goes into vapour liquid separator 5 and separate, at this moment 4. the liquid after the evaporation enter agitated thin-film evaporator 6 continuation evaporations through pipeline, and 5. 7. its evaporation gas enter extraction pot 1 from two its upper side ventholes through pipeline respectively and supply extract drugs as thermal source.Concentrated medicament enters medicinal liquid basin 7,8 through pipeline.Not high enough as concentrated medicament concentration, except that regulating Boiler Steam, two valves of the liquid outlet of scalable vapour liquid separator 5 bottoms also, allow the part of concentrated medicament in the vapour liquid separator 5 3. mix with medicinal liquid from filter 2 through pipeline, enter membrane evaporator 4 again and concentrate, 4. another part enters agitated thin-film evaporator 6 through pipeline and concentrates.8. volatile substance in the extraction pot 1 enters condenser 9 through pipeline, after the condensation again through pipeline (12), (11)) enter in the oil water separator 10, volatile oil is retained in the oil water separator 10,10. moisture then entered in the extraction pot 1 by pipeline.When the water deficient in the extraction pot 1, the water that is stored in the ethanol gravity tank 11 can be replenished according to the amount that flows in the medicinal liquid basin 7.So move in circles, the ingredient in extraction pot 1 is extracted and is finished and can stop.
If solvent is ethanol (or other organic solvent), when extraction proceeds to final stage, close the valve (7) of ethanol gravity tank 11, stop to replenish ethanol, while shut off valve (1), (4), (8) open valve (10), (9), (11), allow the ethanol gas of evaporation 5. 7. 9. enter alcohol distillation column 11 through pipeline, the alcohol steam after the fractional distillation enters condenser 9 through pipeline (18).At this moment, control valve (12), (13) allow ethanol liquid respectively through pipeline (16), and (18) enter in the top and cooler 13 of alcohol distillation column 11, and the ethanol that meets concentration enters ethanol basin 14 through cooler 13.When not having ethanol in the extraction pot 1, open valve (14), (4), (15) allow steam enter the ethanol in the evaporation medicinal residues in the extraction pot 1.After alcohol extraction in the medicinal residues finishes, promptly stop all extracting operation, emit medicinal residues, flushing device closes the valve that make and break.
This utility model compared with prior art its characteristics is.Equipment is shared, save time, energy-conservation, low consumption, yield height, cocnentration factor are big; Decocting for Chinese herbal medicine, concentrate, collect volatile oil and carry out synchronously, medicine return heat up in a steamer, concentrate, reclaim ethanol, fractional distillation ethanol carries out synchronously.
The optimum implementation of this utility model is hospital preparation chamber, factory, the scientific research institution adopts Stainless Steel Shell and pipe is led, valve mechanism, and laboratory should adopt transparent high temperature resistant, high-strength material to make.
Claims (16)
1, a kind of efficient low-consume extractor that is used for animals and plants (mainly being Chinese crude drug) processing, it is characterized in that this machine is by extraction pot 1, filter 2, magnetic drive pump 3, membrane evaporator 4, vapour liquid separator 5, agitated thin-film evaporator 6, medicinal liquid storage tank 7,8, condenser 9, oil water separator 10, ethanol gravity tank 11, alcohol distillation column 12, cooler 13, ethanol storage tank 14, self priming centrifugal pump 15, hydraulic ejector 16, circulating water pool 17, centrifugal pump 18 connects successively by various pipelines, valve, the integral body that interpenetrates and form.
2, extractor according to claim 1, it is characterized in that, extracting cover is connected with cylindrical shell by flange, it is reinforced to open the back, three apertures are arranged at the top of extraction pot 1, one is connected with drain pipe by pipeline, allow the medicinal liquid inflow filter, another aperture can be connected with alcohol distillation tower 12 bottoms with condenser 9 by pipeline, can allow and wherein evaporate gas and enter respectively wherein, the 3rd aperture is connected with the venthole of vaporizer by pipeline, allow its evaporation vapour enter wherein or to discharge, one passageway is arranged at extraction pot 1 bottom, have an aperture on the passageway, can allow it enter heating with the boiler steam pipe connection by pipeline, another aperture is a sewage draining exit, the lower end of extraction pot 1 has three apertures, an aperture is by pipeline and membrane evaporator, and the steam port that goes out of agitated thin-film evaporator connects, and can allow the gas of its two equipment evaporation enter extraction pot 1, another aperture is by pipeline and oil water separator liquid outlet, gravity tank bottom liquid outlet connects, allow its liquid enter in the extraction pot 1, the 3rd aperture is connected with filter by pipeline, allows its medicinal liquid enter filter, blind flange is arranged at top, extraction pot lower end, can emit by medicinal residues by breakdown.
3, extractor according to claim 1, it is characterized in that, the inlet of magnetic drive pump 3 is connected by the bottom liquid outlet of pipeline with filter 2 and vapour liquid separator 5, the liquid outlet of magnetic drive pump 3 is connected with the lower end liquid outlet of extraction pot 1 and the lower end of membrane evaporator 4 by pipeline, and liquid can be entered wherein respectively.
4, extractor according to claim 1, it is characterized in that, the lower end of membrane evaporator 4 has three apertures, wherein one of the top, lower end is connected with the liquid outlet of magnetic drive pump 3, but accelerated evaporation speed, and two are respectively sewage draining exit and waste vapour outlet in addition, the upper end of membrane evaporator 4 has three apertures, wherein Shang Mian big aperture links to each other with vapour liquid separator 5 by pipeline, and another is connected with boiler evaporating vapour by pipeline, and the 3rd aperture is the waste vapour outlet.
5, extractor according to claim 1, it is characterized in that, the lower end of vapour liquid separator 5 has a liquid outlet, both can be connected by pipeline with magnetic drive pump 3, allow medicinal liquid wherein enter evaporation in the membrane evaporator 4 once more, can allow medicinal liquid enter again and continue evaporation in the agitated thin-film evaporator 6, a venthole is arranged at the top of vapour liquid separator 5, can also can import alcohol distillation column evaporation vapour input extraction pot 1 as the thermal source that extracts medicinal liquid by pipeline.
6, extractor according to claim 1, it is characterized in that, the upper end of agitated thin-film evaporator 6 has four apertures, one can be imported Boiler Steam as thermal source by pipeline, the evaporation vapour that also can import vapour liquid separator 5 is as thermal source, it two links to each other with the lower end liquid outlet of vapour liquid separator 5 by pipeline, the gas of its three evaporations in agitated thin-film evaporator 6 can be imported extraction pot 1 by pipeline, alcohol distillation column 12, it four exports as waste vapour, the lower end of agitated thin-film evaporator has three apertures, by pipeline concentrated medicament is imported in the medicinal liquid storage tank 7,8 first, second discharge waste liquid, three exhaust waste steam.
7, according to the described extractor of claim, it is characterized in that, medicinal liquid basin 7, all there is heatable deflection plate medicinal liquid basin 8 inside, its top respectively has three apertures, big aperture, for the vapor opening mouth is connected with agitated-film vaporizer gland steam exhauster by pipeline, medicinal liquid basin 7 another holes are the admission aperture, be connected with agitated thin-film evaporator lower end steam drain by pipeline, allow steam enter the deflection plate heating, the 3rd aperture is connected with agitated thin-film evaporator fluid aperture by pipeline, allows concentrated medicament enter wherein evaporation, medicinal liquid basin 8 the 3rd aperture is connected with medicinal liquid basin 7 liquid outlets by pipeline, allow concentrated medicament enter wherein and store medicinal liquid basin 7,8, but the place, bottom has the hand hole visor of breakdown, can open after having operated and get it filled.
8, extractor according to claim 1, it is characterized in that, respectively there are three apertures the both sides of condenser 9, condensed water is imported from the left end aperture, export from the right-hand end aperture, the top, right side is an air intake, top by pipeline and alcohol distillation column 12, extraction pot 1 top, cooler 13, ethanol basin 14, the steam drain of ethanol gravity tank 11 links to each other, the below, right side is a sewage draining exit, the top, left side is a steam drain, is connected with hydraulic ejector 16 bleeding points by pipeline, and the below, left side is the discharge opeing aperture, be connected with the control valve group with oil water separator 10 by pipeline, condensed fluid can be entered wherein respectively.
9, extractor according to claim 1, it is characterized in that, the upper end of oil water separator 10 has two apertures, one links to each other with condenser 9 by pipeline, another is the oil extraction aperture, the lower end has two apertures, one by pipeline to extraction pot 1 input condensed fluid solvent as a supplement, another is a sewage draining exit.
10, extractor according to claim 1, it is characterized in that, the upper end of ethanol gravity tank 1 has three apertures, first links to each other with self priming centrifugal pump 15 by pipeline, input ethanol, and second is connected with running water pipe by pipeline, can introduce tap water, the 3rd admission aperture, the lower end of ethanol gravity tank 11 has an aperture, carries solvent by pipeline to extraction pot 1.
11, extractor according to claim 1, it is characterized in that, the lower end of alcohol distillation column has an aperture, can link to each other with the upper end steam drain of extraction pot 1 by pipeline, also can with vapour liquid separator 5, the steam drain of agitated thin-film evaporator 6 connects, allow it extract the interior fractional distillation of vaporized alcohol gas input tower in later stage, the upper end of alcohol distillation column 12 has two apertures, vapour input condenser 9 will be evaporated by pipeline in one aperture, another aperture links to each other with spinner flowmeter with one group of control valve by pipeline, the ethanol liquid part of condensation in the condenser 9 is got back in the tower, and another part enters in the cooler 13.
12, extractor according to claim 1, it is characterized in that, respectively there are three apertures the both sides of cooler 13, and condensed water is exported from the right-hand end aperture from the input of left end aperture, aperture, top, left side is the steam discharge aperture, link to each other by the air intake of pipeline with condenser 9, aperture, below, left side is connected with ethanol basin 14 by pipeline, and aperture, top, left side is an inlet, be connected with the control valve group, aperture, below, right side is a sewage draining exit.
13, extractor according to claim 1, it is characterized in that, the lower end of ethanol basin 14 has an aperture, be connected by the inlet of pipeline with self priming centrifugal pump 15, make a jar interior ethanol input ethanol gravity tank 11, the upper end of ethanol basin 14 has three apertures, first is connected by the liquid outlet of pipeline with self priming centrifugal pump 15, can make outside ethanol by in the self priming centrifugal pump 15 input jars, second is connected with cooler 13 by pipeline, allow refrigerative alcohol liquid enter in the jar, the 3rd aperture can link to each other with condenser 9 by pipeline, also as the steam discharge aperture.
14, extractor according to claim 1 is characterized in that, the bleeding point of hydraulic ejector 16 is connected by the steam drain of pipeline with condenser 9, to reach above-mentioned each equipment decompression operation.
15, extractor according to claim 1 is characterized in that, this machine only needs varying sized, increase extraction pot or deduct alcohol distillation column, promptly can be used as the hospital preparation chamber, laboratory, the ethanol of large and small pharmaceutical factory and health product factory and water extraction, or single water extraction equipment.
16, extractor according to claim 1 is characterized in that, this extractor is that stainless steel material, red copper or transparent high temperature resistance and high strength material are made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 93209708 CN2196504Y (en) | 1993-04-08 | 1993-04-08 | High-efficient low-consumption extraction machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 93209708 CN2196504Y (en) | 1993-04-08 | 1993-04-08 | High-efficient low-consumption extraction machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2196504Y true CN2196504Y (en) | 1995-05-10 |
Family
ID=33791823
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 93209708 Expired - Fee Related CN2196504Y (en) | 1993-04-08 | 1993-04-08 | High-efficient low-consumption extraction machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2196504Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101862548A (en) * | 2010-05-26 | 2010-10-20 | 重庆大学 | Combined type extracting device |
| CN103783197A (en) * | 2014-03-04 | 2014-05-14 | 慈溪市科创电子科技有限公司 | Tea extract preparing method |
| CN103834474A (en) * | 2014-03-25 | 2014-06-04 | 周午贤 | High-efficiency taxus chinensis volatile oil extracting device |
| CN105886306A (en) * | 2016-06-29 | 2016-08-24 | 佛山市丰川节能科技有限公司 | Wine liquid heating and evaporation system and method thereof with cyclic utilization of wine steam heat energy |
-
1993
- 1993-04-08 CN CN 93209708 patent/CN2196504Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101862548A (en) * | 2010-05-26 | 2010-10-20 | 重庆大学 | Combined type extracting device |
| CN101862548B (en) * | 2010-05-26 | 2011-09-07 | 重庆大学 | Combined type extracting device |
| CN103783197A (en) * | 2014-03-04 | 2014-05-14 | 慈溪市科创电子科技有限公司 | Tea extract preparing method |
| CN103783197B (en) * | 2014-03-04 | 2015-06-10 | 湘西华方制药有限公司 | Tea extract preparing method |
| CN103834474A (en) * | 2014-03-25 | 2014-06-04 | 周午贤 | High-efficiency taxus chinensis volatile oil extracting device |
| CN105886306A (en) * | 2016-06-29 | 2016-08-24 | 佛山市丰川节能科技有限公司 | Wine liquid heating and evaporation system and method thereof with cyclic utilization of wine steam heat energy |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |