CN201179360Y - Double-dynamic state high-efficiency energy conservation extracting apparatus - Google Patents
Double-dynamic state high-efficiency energy conservation extracting apparatus Download PDFInfo
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- CN201179360Y CN201179360Y CNU2007200587872U CN200720058787U CN201179360Y CN 201179360 Y CN201179360 Y CN 201179360Y CN U2007200587872 U CNU2007200587872 U CN U2007200587872U CN 200720058787 U CN200720058787 U CN 200720058787U CN 201179360 Y CN201179360 Y CN 201179360Y
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Abstract
The utility model relates to the field of the Chinese herbal medicine and propagation extracting device, which is applicable to the extraction and the production of the Chinese herbal medicine and the propagation. The device is a dual-dynamic high-efficient energy-saving extracting equipment provided with a spiral stirrer which can rotate clockwise or counterclockwise and has an inner liquid medicine jacket being partitioned into an upper part and a lower part by a partition board; the inner side wall of the inner liquid medicine jacket is a stainless-steel sieve plate, a liquid outlet passes through a pot body and an outer heating jacket in the tangential direction and is connected with an external circulating device. During the extraction, material is slowly stirred from the center to the circumference under the action of the spiral stirrer, the extract liquid quickly and circularly flows under the action of an external circulating system after being filtered by the inner liquid medicine jacket, the heat exchange process during heating and extracting and the releasing speed of the active ingredients are greatly quickened, thereby the purposes of high efficiency and energy conservation are achieved. The equipment is applicable to the extraction and the production of the technical fields of traditionally Chinese medicine and natural medicine, food, chemical industry, light industry, etc.
Description
Technical field
The utility model relates to Chinese medicine, herbal medicine, animals and plants extraction apparatus field, and particularly Chinese patent drug extracts the extraction apparatus field of production and plant extract production.Specifically be a kind of energy-conservation extraction equipment of two dynamic high-efficiencies that spiral agitator and inner liquid medicine chuck are housed.
Background technology
The solid-liquid extractive technique is widely used in the extracts active ingredients and enrichment process in fields such as Chinese medicine, health food, beverage.Here extractor plays important effect as the capital equipment in the abstraction process to extraction efficiency, extraction time, energy consumption, production capacity etc.
In the Chinese medicine industry, extraction is produced Chinese medicine production especially and is different from the main place that Western medicine is produced, existing traditional Chinese medicine enterprise uses traditional multi-function extractor substantially, such extractor mainly by cylindrical shell, the end open the door, screen cloth, the chuck zone of heating of cylindrical shell and the agitating device of slurry formula of the end on opening the door form.Along with the quickening of modernization of Chinese medicine process, people have had significant progress for Chinese medicine extracts active ingredients aspect, also are that very big development has been arranged to the improvement of multi-function extractor.
But in use some problems of ubiquity are as follows for extractor of the prior art:
(1) dregs of a decoction in the extractor and the heating of soup are undertaken by outer heating jacket, thermal source is steam or heat conduction wet goods heat medium, because the heated material majority in the extractor remains static, heat can only very easily produce hot-spot by heated wall to the internal layer transmission, and integral body is heated inhomogeneous, heat time heating time is long, and because heat transfer rate is slow, cause the leaching process temperature measuring inaccurate, can't accurately control and extract temperature and heating-up time;
(2) the minority extractor is provided with agitating device, but agitating device mostly is the oar formula, in leaching process, be subjected to resistance big, need to use powerful stirring motor, damage paddle when medicinal material easily when more or hard, minority is for short spiral, mixing effect is relatively poor;
(3) extractor uses cleanout door, adopt pneumatic control, cleanout door is done 90 ° open and close action under the effect of cylinder, usually airtight for production safety with reinforcement, need to add artificial locking device on the rotating shaft opposite, the security incidents such as unhook blowdown of avoiding the air pressure shakiness to cause the cylinder return to cause are difficult to realize that control is produced automatically;
(4) some extractor has installed the side filter additional increasing the rate of filtration, but design goes up and use stainless steel mesh, damages easily, needs often to change, and filters cavity and often form the dead angle with extracting tank skin, can't clean, and does not meet pharmaceutical production GMP requirement.
(5) dregs of a decoction that extract after finishing do not have through extracting, medicinal material is general after having extracted to absorb 2 times to the soup of own vol, cause the waste of active ingredient, increased and extracted required solvent, increase production cost, and the solvent that the dregs of a decoction contain causes environmental pollution usually, does not meet the demand of modern Chinese herbal medicine manufacturing enterprise.
The utility model content
The purpose of this utility model is to have overcome above-mentioned shortcoming of the prior art, provide a kind of effective solution leaching process herb liquid to need dynamic problem, increase extraction efficiency greatly, shortened whole extraction time, and the energy-efficient extraction equipment of the novel double-movable attitude that meets pharmaceutical production GMP designing requirement, if supporting by with auxiliary deslagging and online measuring technique can realize that the totally enclosed type of Automatic Control is produced continuously.
In order to realize above-mentioned purpose, the of the present utility model pair of energy-conservation extraction equipment of dynamic high-efficiency has following formation:
The energy-conservation extraction equipment of this pair dynamic high-efficiency comprises extractor, and its main feature is that described extractor is provided with spiral agitator; Tank body is provided with outer heating jacket and inner liquid medicine chuck, and the internal layer sidewall of inner liquid medicine chuck is the stainless steel sieve plate, and the inner liquid medicine chuck is partitioned into two parts up and down by dividing plate, and a liquid outlet is respectively arranged; Tank body is provided with slag notch, and slag notch is by the slag releasing channel transition, and the lower end is provided with the slag notch valve, and slag notch can be connected with the auxiliary equipment of slagging tap by flange.
The energy-conservation extraction equipment of this pair dynamic high-efficiency inner liquid medicine chuck madial wall stainless steel sift plate thickness is 2～5mm, and sieve aperture is square, circular, oval or irregular shape, and slot size is 2mm～0.01mm, and sieve aperture density is 1～100 every square millimeter; Sieve aperture is a random distribution, and the distance between inner liquid medicine chuck madial wall and the tank skin is 10～50mm.The all circular transition of sealing part up and down of inner liquid medicine chuck is sealed sieve aperture is not set, and seals the outside and carries out welded closure with the dead angle of extracting tank skin formation by corrosion resistant plate, realizes rounding off; The inner liquid medicine chuck is partitioned into two parts by a dividing plate, all circular up and down transition of dividing plate, and dividing plate is not with sieve aperture, and the inner liquid medicine chuck madial wall in the dead range of being sealed by dividing plate does not contain sieve aperture, and inner liquid medicine chuck dividing plate at interval is arranged on inner liquid medicine chuck optional position; The inner liquid medicine chuck respectively has a liquid outlet in two parts bottom up and down, is oriented in a tangential direction and passes tank body and outer heating jacket, can be connected with external recycle unit.
The spiral agitator integral body of the energy-conservation extraction equipment of this pair dynamic high-efficiency is cylindrical or spindle, and blade is evenly distributed, can be clockwise or the inhour rotation, and lower end spiral equal diameters extends in the slag releasing channel.
The slag releasing channel of the energy-conservation extraction equipment of this pair dynamic high-efficiency plays fixedly spiral agitator, length is for covering the helical blade of spiral agitator 1 circle half, diameter and spiral agitator blade etc. are big, inwall covers the liner of polytetrafluoroethylene (PTFE) material, can closely contact with spiral agitator, make spiral agitator when rotation fixed-site and reduce frictional resistance.
The slag notch valve of the energy-conservation extraction equipment of this pair dynamic high-efficiency is ball valve or stop valve, diameter is 100～600mm, can be mounted to hand or electrodynamic type or pneumatic type, and its internal diameter is consistent with slag releasing channel, can seal the liquid in whole jar when closing fully, during unlatching the nothing of slagging tap be influenced.
Adopted the energy-conservation extraction equipment of two dynamic high-efficiencies of this utility model, because it is spiral to stir employing, when extracting, pass through the slow rotation of spiral agitator, the medicinal material of jar core is driven up motion by helical blade, the bottom produces the larger volume space simultaneously, the medicinal material of part falls down under the gravity effect around jar, so circulation, thereby solved the common excessive problem of resistance in the whipping process that is stirred in, and because medicinal material becomes the symmetry motion, whole tank body is not produced the effect of waving, reduced mechanical wear; Simultaneously, the liquid outlet of inner liquid medicine chuck can make soup or top-down shuttling movement under the effect of external equipment from bottom to top in leaching process, and all move during the soup turnover along the tank body tangential direction, thin inner liquid medicine chuck has guaranteed can be at the inner rotate-stationary mode that forms of inner liquid medicine chuck in the soup motion process, avoid fouling, when having clogging, sieve aperture can recover strainability easily by the direction flushing, but the rate of filtration has been accelerated in two all tapping of liquid outlet up and down greatly during tapping; Moreover, after extraction is finished, open the slag notch valve, the counter motion by spiral agitator can realize forcing the deslagging effect.Force dynamical fashion by in leaching process, using medicinal material motion and soup to move these two kinds simultaneously, traditional leaching process inefficiency, problem that recovery rate is low have been solved, most extracts active ingredients rate of transform rates improve 20～50%, shorten 30% heat time heating time, energy consumption saves 20%, reached the purpose of the energy savings of enhancing productivity, not only safe and efficient, shortened the whole production time, and equipment meets pharmaceutical production GMP requirement, have wide range of applications, bring great convenience for the extraction production of Chinese medicine and natural drug.
Description of drawings
It shown in the figure section part-structure schematic diagram of the of the present utility model pair of energy-conservation extraction equipment of dynamic high-efficiency.
The specific embodiment
As shown in the figure, the described in the utility model pair of energy-conservation extraction equipment of dynamic high-efficiency comprise extractor (3), the medicinal material of band outer heating jacket (8) and inner liquid medicine chuck (9) enter the mouth (1), fluid-mixing import (5), solvent import (2), wash ball (4), spiral agitator (6), slag releasing channel (12), slag notch valve (13), reach slag notch (14).Outer heating jacket top is provided with steam inlet (7), and the bottom is provided with steam condensate (SC) outlet (16).Inner liquid medicine chuck top and bottom (17) and tank body weld all adopt semicircle pipeline to bind, and make the inner liquid medicine chuck become rounding off, and the dead angle that forms with jar inwall of binding forms rounding off with the whole circle of corrosion resistant plate (20) welded closure; The inner liquid medicine chuck is separated into two parts by a dividing plate (18), dividing plate adopts two semicircle pipeline forms respectively and extracts the tank skin welding, weld with inner liquid medicine chuck wall, become rounding off with inner liquid medicine chuck two parts respectively, the dead angle part that inner liquid medicine chuck inwall and dividing plate form does not contain sieve aperture, whole airtight isolation; The inner liquid medicine chuck is provided with liquid outlet (10), (11) in two parts bottom up and down, all is oriented in a tangential direction with tank body, passes tank body and the external opening of outer heating jacket, can dock with external recycle unit, and can realize flowing to switching by valve pipe combination switching; Spiral agitator (6) can be under the drive of transmission system (21) clockwise or the inhour rotation; The whole circle of slag releasing channel (12) tool polytetrafluoroethyllining lining is closely blocked the spiral agitator blade, as the base of spiral agitator; Valve configurations has auxiliary opening device (15) by the slag notch valve seal at the jar end; Slag notch (14) general laws orchid can be connected with other auxiliary equipment of slagging tap.
The course of work is: open medicinal material inlet (1) or fluid-mixing import (5), put into medicinal material, close medicinal material inlet (1) and fluid-mixing import (5), add by solvent import (2) and extract solvent, after finishing solvent and adding, close solvent import (2); Feed steam by steam inlet (7), begin heating, utilize external circulating system that the extraction solvent is circulated by upper liquid outlet (10), lower liquid outlet (11) simultaneously.Steam off after the arrival temperature, opening spiral agitator (6) makes to be rotated counterclockwise, and the medicinal material of jar center moves upward under the drive of spiral agitator, produce the space of larger volume simultaneously in the bottom, the medicinal material of jar location about moves downward under the gravity effect.Whole leaching process, medicinal material is done at a slow speed around middle mind-set under the effect of spiral agitator and is stirred, soup is by the filtration of inner liquid medicine chuck, under the external circulating system effect, circulate fast, extract solvent and constantly wash away medicinal material, medicinal material is constantly shifted one's position and angle, fully is subjected to washing away of solvent, thereby extracts active ingredients rate of transform rate obviously improves.And the heating process solvent all at the volley, quickened heat transfer process greatly, can at utmost improve extraction production efficiency.After extraction finishes, soup is by the filtration of inner liquid medicine chuck, emit simultaneously from liquid outlet (10), (11), after soup has been put, clockwise rotate spiral agitator, the dregs of a decoction are extruded under the effect of spiral agitator, most soups are extruded, and treat that soup flows out more after a little while, opens slag notch valve (13), continue to start clockwise spiral agitator, the dregs of a decoction are forced to discharge under the effect of spiral agitator.At last, clean complete equipment.The utility model can all be provided with fast-connecting type cleaning device interface on the pipeline of extractor and soup process, clean so that insert cleaning fluid.Particularly inner liquid medicine chuck inwall is designed in the 50mm with the spacing of extracting tank skin, and cleaning fluid tangentially enters the inner liquid medicine chuck at a high speed from liquid outlet (10) or (11), along the tank skin high speed rotary motion, inner liquid medicine chuck inner chamber body is also cleaned up.
The utility model is to aim at the new equipment that satisfies the GMP authentication and produce, and compared to prior art, can high efficiency extract effectively Composition is saved the production time, and solid-liquid separates easily, and extract is haze-free. The utility model also can be applicable to food, chemical industry, The extraction process of the technical fields such as light industry.
Claims (10)
1, a kind of pair of energy-conservation extraction equipment of dynamic high-efficiency includes the extractor of being with outer heating jacket and inner liquid medicine chuck, spiral agitator, and slag releasing channel goes out to look into mouthful valve and slag notch; It is characterized in that the internal layer sidewall of inner liquid medicine chuck is the stainless steel sieve plate, the inner liquid medicine chuck is partitioned into two parts up and down by dividing plate, and a liquid outlet is respectively arranged, and slag notch is connected with the auxiliary equipment of slagging tap by flange, and the slag notch valve is not provided with screen cloth.
2, according to claim 1 pair of energy-conservation extraction equipment of dynamic high-efficiency, it is characterized in that, described inner liquid medicine chuck madial wall stainless steel sift plate thickness is 2～5mm, sieve aperture is square, circular, oval or irregular shape, slot size is 2mm～0.01mm, sieve aperture density is 1～100 every square millimeter, and sieve aperture is a random distribution.
3, according to claim 2 pair of energy-conservation extraction equipment of dynamic high-efficiency, it is characterized in that, distance between inner liquid medicine chuck madial wall and the tank skin is 10～50mm, the all circular transition of sealing part up and down of inner liquid medicine chuck, seal sieve aperture is not set, seal the outside and carry out welded closure by corrosion resistant plate, realize circular transition with the dead angle of extracting tank skin formation.
4, the according to claim 1 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that, the at interval all circular transition of dividing plate of inner liquid medicine chuck, and dividing plate is not with sieve aperture, and the inner liquid medicine chuck madial wall in the dead range of being sealed by dividing plate does not contain sieve aperture.
5, the according to claim 4 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that, inner liquid medicine chuck dividing plate at interval is arranged on inner liquid medicine chuck optional position.
6, the according to claim 1 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that two liquid outlets all are arranged on the bottom of inner liquid medicine chuck, is oriented in a tangential direction to pass tank body and outer heating jacket, can be connected with external recycle unit.
7, the according to claim 1 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that, spiral agitator integral body is cylindrical or spindle, and blade is evenly distributed, can be clockwise or the inhour rotation.
8, the according to claim 7 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that spiral agitator lower end spiral equal diameters extends in the slag releasing channel.
9, according to claim 8 pair of energy-conservation extraction equipment of dynamic high-efficiency, it is characterized in that, slag releasing channel length is for covering the helical blade of spiral agitator 1 circle half, and diameter and spiral agitator blade etc. are big, and inwall covers the liner of polytetrafluoroethylene (PTFE) material.
10, the according to claim 1 pair of energy-conservation extraction equipment of dynamic high-efficiency is characterized in that the slag notch valve is ball valve or stop valve, and diameter is 100～600mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200587872U CN201179360Y (en) | 2007-10-29 | 2007-10-29 | Double-dynamic state high-efficiency energy conservation extracting apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200587872U CN201179360Y (en) | 2007-10-29 | 2007-10-29 | Double-dynamic state high-efficiency energy conservation extracting apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN201179360Y true CN201179360Y (en) | 2009-01-14 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2007200587872U Expired - Lifetime CN201179360Y (en) | 2007-10-29 | 2007-10-29 | Double-dynamic state high-efficiency energy conservation extracting apparatus |
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102078701A (en) * | 2010-12-20 | 2011-06-01 | 东莞广州中医药大学中医药数理工程研究院 | Energy-saving synergetic method and device in extracting production process of traditional Chinese medicine |
| CN103083938A (en) * | 2011-11-01 | 2013-05-08 | 四川汇利实业有限公司 | High-efficiency drug extract tank |
| CN103272403A (en) * | 2013-05-27 | 2013-09-04 | 上海远跃制药机械股份有限公司 | Vacuum infiltration device and method for pretreatment in animal and plant extraction processes |
| CN104801064A (en) * | 2015-04-22 | 2015-07-29 | 江苏沙家浜化工设备有限公司 | Cage-type dynamic forced extracting device |
| CN105363240A (en) * | 2015-11-23 | 2016-03-02 | 浙江财经大学 | Traditional Chinese medicine effective component extraction pretreatment apparatus |
| CN105641969A (en) * | 2016-01-08 | 2016-06-08 | 严修长 | Traditional Chinese medicine extraction tank |
| CN105727588A (en) * | 2014-08-10 | 2016-07-06 | 胡刘满 | Extraction device for extracting plant active components |
| CN104366627B (en) * | 2013-08-17 | 2019-04-26 | 唐山蓝猫饮品集团有限公司 | A kind of wild jujube leaching device |
| CN110639433A (en) * | 2019-10-09 | 2020-01-03 | 李财 | Automatic stirring spiral discharging device of reaction kettle |
| CN110742928A (en) * | 2019-09-09 | 2020-02-04 | 通化百信药业有限公司 | Preparation method and equipment of kangfulingshuan |
| CN111644117A (en) * | 2020-06-15 | 2020-09-11 | 惠安先锋机械有限公司 | Special material dissolving and extracting device for industrial design |
| CN111790179A (en) * | 2020-07-23 | 2020-10-20 | 北京图腾猎技科技有限公司 | Extraction equipment for preparing traditional Chinese medicine decoction pieces and operation method thereof |
| CN111905406A (en) * | 2020-09-03 | 2020-11-10 | 江西中医药大学 | Traditional Chinese medicine percolation equipment and process |
-
2007
- 2007-10-29 CN CNU2007200587872U patent/CN201179360Y/en not_active Expired - Lifetime
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102078701A (en) * | 2010-12-20 | 2011-06-01 | 东莞广州中医药大学中医药数理工程研究院 | Energy-saving synergetic method and device in extracting production process of traditional Chinese medicine |
| CN102078701B (en) * | 2010-12-20 | 2012-11-14 | 东莞广州中医药大学中医药数理工程研究院 | Energy-saving synergetic method and device in extracting production process of traditional Chinese medicine |
| CN103083938A (en) * | 2011-11-01 | 2013-05-08 | 四川汇利实业有限公司 | High-efficiency drug extract tank |
| CN103272403A (en) * | 2013-05-27 | 2013-09-04 | 上海远跃制药机械股份有限公司 | Vacuum infiltration device and method for pretreatment in animal and plant extraction processes |
| CN104366627B (en) * | 2013-08-17 | 2019-04-26 | 唐山蓝猫饮品集团有限公司 | A kind of wild jujube leaching device |
| CN105727588B (en) * | 2014-08-10 | 2017-12-08 | 胡刘满 | Extract the extraction element of plant actives |
| CN105727588A (en) * | 2014-08-10 | 2016-07-06 | 胡刘满 | Extraction device for extracting plant active components |
| CN104801064A (en) * | 2015-04-22 | 2015-07-29 | 江苏沙家浜化工设备有限公司 | Cage-type dynamic forced extracting device |
| CN105363240B (en) * | 2015-11-23 | 2017-05-31 | 浙江财经大学 | Effective Component of Chinese Medicine extracts pretreatment unit |
| CN105363240A (en) * | 2015-11-23 | 2016-03-02 | 浙江财经大学 | Traditional Chinese medicine effective component extraction pretreatment apparatus |
| CN105641969A (en) * | 2016-01-08 | 2016-06-08 | 严修长 | Traditional Chinese medicine extraction tank |
| CN110742928A (en) * | 2019-09-09 | 2020-02-04 | 通化百信药业有限公司 | Preparation method and equipment of kangfulingshuan |
| CN110742928B (en) * | 2019-09-09 | 2023-05-26 | 通化百信药业有限公司 | Method and equipment for preparing recovery suppository |
| CN110639433A (en) * | 2019-10-09 | 2020-01-03 | 李财 | Automatic stirring spiral discharging device of reaction kettle |
| CN111644117A (en) * | 2020-06-15 | 2020-09-11 | 惠安先锋机械有限公司 | Special material dissolving and extracting device for industrial design |
| CN111790179A (en) * | 2020-07-23 | 2020-10-20 | 北京图腾猎技科技有限公司 | Extraction equipment for preparing traditional Chinese medicine decoction pieces and operation method thereof |
| CN111905406A (en) * | 2020-09-03 | 2020-11-10 | 江西中医药大学 | Traditional Chinese medicine percolation equipment and process |
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| CX01 | Expiry of patent term |
Granted publication date: 20090114 |
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| CX01 | Expiry of patent term |