CN210933840U - Multifunctional extracting and concentrating integrated equipment - Google Patents
Multifunctional extracting and concentrating integrated equipment Download PDFInfo
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- CN210933840U CN210933840U CN201921462480.8U CN201921462480U CN210933840U CN 210933840 U CN210933840 U CN 210933840U CN 201921462480 U CN201921462480 U CN 201921462480U CN 210933840 U CN210933840 U CN 210933840U
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Abstract
The utility model discloses a multifunctional extraction and concentration integrated device, which comprises a heater, an evaporation chamber, an extraction tank and the like, wherein the heater is connected with the evaporation chamber, the evaporation chamber is connected with the extraction tank, and the heater and the extraction tank are both connected with a back-washing filter; the extraction tank is simultaneously with receiving oily condensing equipment, one imitates the heater and links to each other with one imitates the evaporating chamber, one imitates vapour and liquid separator and one imitates the heater, one imitates the evaporating chamber, two imitates the heater and links to each other simultaneously with one imitate heater and two imitate the heater, two imitate the heater and link to each other with two imitate the evaporating chamber, two imitate the evaporating chamber and link to each other with the condenser, the condenser links to each other with the cooler, the cooler links to each other with the cistern of receiving, two imitate vapour and liquid separator and two imitate the heater, two imitate the evaporating chamber, the cistern of receiving links to each. The utility model discloses extract the concentration and go on simultaneously, belong to the dynamic extraction, heating time is short, and the yield is high, more energy-conserving.
Description
Technical Field
The utility model belongs to traditional chinese medicine draws concentrated field, especially relates to an integrated device that traditional chinese medicine developments were drawed, were concentrated. Is suitable for water boiling, alcohol extraction, decoction reflux, solvent recovery and the like.
Background
The extraction and concentration are necessary operation units of most traditional Chinese medicine preparations, and the extraction and concentration methods are various. The extraction method comprises the following steps: decocting, refluxing, steam distilling, percolating, and supercritical fluid extracting, microwave extracting, and ultrasonic extracting; the concentration method mainly comprises the following steps: normal pressure evaporation, reduced pressure concentration, film concentration, multi-effect concentration and the like. The novel extraction and concentration methods are not widely used industrially because of their use limitations and cost problems. At present, the industrial extraction method mainly adopts a decoction method, a reflux method, a steam distillation method and a percolation method, and the concentration adopts single-effect or multi-effect concentration. These devices have been used for many years in traditional Chinese medicine production processes, but these methods have significant drawbacks, both in terms of efficiency of preparation and in terms of drug stability. Firstly, for extraction, the operations of decocting, refluxing and steam distillation extraction involve heating a decocting tank, the problems of nonuniform temperature in the tank, long decocting time, high strength, difficult stabilization of effective components, even floating of part of medicinal materials and the surface of decoction, and the like exist, and the time consumption is too long although percolation extraction is favorable for the stability of the medicine. Secondly, in the aspect of concentration, the problems that the heating time is too long, the stability of the concentrated solution is not facilitated and the like obviously exist in single-effect or multi-effect concentration.
The traditional Chinese medicine extraction production line is characterized in that decoction and extraction are carried out firstly to obtain an extracting solution, and then concentration is carried out, so that the process has the defects of long production period, high energy consumption, high medicinal material loss, high solvent dosage, low effective component transfer rate, poor extract quality, high labor intensity, low labor productivity, low equipment utilization rate and the like, and the production pain point.
SUMMERY OF THE UTILITY MODEL
In order to overcome prior art's traditional chinese medicine and draw concentrated defect and production pain point, the utility model provides a multi-functional concentrated integrative equipment of drawing combines together the basic principle that basic theory and traditional chinese medicine of relevant subject draw, and under the condition that accords with the GMP standard, has changed traditional production technology, adopts to draw and concentrates simultaneously, and save time saves the extraction liquid and stores the middle ring, can reach energy-conservation, environmental protection, low consumption, high efficiency, high-quality purpose.
The utility model discloses a following technical scheme realizes: the utility model provides a multi-functional concentrated integrative equipment that draws, includes heater, evaporating chamber, draws the jar be equipped with the pipeline that supplies the liquid medicine circulation between heater and the pipeline evaporating chamber, still be equipped with between heater and the evaporating chamber and supply steam from the pipeline that the heater circulated to the evaporating chamber, the top steam outlet of evaporating chamber links to each other with the steam inlet who draws the jar, and the liquid medicine export that draws the jar leads to the heater.
Further improved, the device also comprises a first-effect heater, a first-effect evaporation chamber, a second-effect heater, a second-effect evaporation chamber, a condenser, a cooler, a liquid collecting tank and a second-effect gas-liquid separator, the oil recovery device comprises an extraction tank, an oil recovery condensing device, a first-effect heater, a first-effect evaporation chamber, a second-effect heater, a first-effect gas-liquid separator and a back-flushing filter, wherein the extraction tank is connected with the oil recovery condensing device and the first-effect heater at the same time, the first-effect heater is connected with the first-effect evaporation chamber, the first-effect evaporation chamber is connected with the second-effect heater, the first-effect gas-liquid separator is connected with the first-effect heater, the first-effect evaporation chamber and the second-effect heater at the same time, the heaters are connected with the first-effect heater and the second-effect heater at the same time, the second-effect heater is connected with the second-effect evaporation chamber, the second-effect evaporation chamber is connected with a condenser, the condenser is connected.
The further improvement still includes vacuum buffer tank, vacuum pump, cooling water circulation jar, the condenser links to each other with vacuum buffer tank, and vacuum buffer tank links to each other with the vacuum pump, and the vacuum pump links to each other with the cooling water circulation jar.
More specifically, the upper part of the heater is connected with the top of the extraction tank through a connecting pipe, the bottom of the heater is connected with the bottom of the backwashing filter through a connecting pipe, a circulating pump is arranged between the heater and the backwashing filter, the upper part of the backwashing filter is connected with the bottom of the extraction tank through a connecting pipe, medicinal materials in the extraction tank can be circularly heated through the heater, and medicinal liquid can flow back to the heater through the bottom connecting pipe and the backwashing filter. By adopting the novel circulating heating system, the time is shorter than that of the traditional jacket heating system, the heating time can be saved by 50 percent, and the energy is saved.
More specifically, the heater is connected with the evaporation chamber through an upper connecting pipe and a lower connecting pipe, liquid medicine can be subjected to gas-liquid separation in the evaporation chamber, the top of the evaporation chamber is connected with the extraction tank through a pipeline, and separated secondary steam is sent into the extraction tank.
More specifically, the bottom of the heater is connected with the bottoms of the first-effect heater and the second-effect heater through pipelines, the liquid medicine can flow into the first-effect heater and the second-effect heater, and a high-pressure fan is arranged between the extraction tank and the first-effect heater, so that the steam from the extraction tank is further heated to be used as a heat source for later concentration. The first-effect heater is connected with the first-effect evaporation chamber through an upper connecting pipe and a lower connecting pipe, the second-effect heater is connected with the second-effect evaporation chamber through an upper connecting pipe and a lower connecting pipe, the top of the first-effect evaporation chamber is connected with the second-effect heater through a pipeline, and secondary steam separated from the first-effect evaporation chamber serves as a heat source of the second-effect heater. The liquid medicine of the heater is shunted to the first-effect heater and the second-effect heater for concentration, the efficiency is improved, the secondary steam of the extraction tank and the secondary steam of the first-effect evaporation chamber are secondarily utilized, the heat utilization efficiency is improved, and more energy is saved.
The extraction tank is further improved, a material pressing device is arranged in the extraction tank, and the light material can be fully contacted with the medium through the material pressing device, so that the amount of the solvent can be reduced by 50%.
The further improvement is that the bottom of the extraction tank is provided with a squeezing solid-liquid separator, so that the liquid medicine and the medicine dregs are fully separated, the yield can be improved by 10-20%, and the sewage discharge is reduced by 80%.
Further improvement, the extracting tank is provided with a vibrating device, so that the medicine dregs are prevented from bridging and are not easy to discharge dregs.
The technical effects of the utility model: in the traditional production process, the extraction tank is used for statically heating and decocting medicinal materials and a solvent in the tank by introducing steam through a jacket, the heating time is long, the extraction tank belongs to a pressure container, potential safety hazards exist, and the extraction tank needs to be periodically monitored and checked by related departments. The extraction tank circularly heats the solvent by a heater outside the extraction tank, the dynamic extraction is realized, the extracting solution is heated by the heater and then enters an evaporator for concentration, the upper steam concentrated by the evaporator is used as a heat source for extraction, the extraction and the concentration are synchronously performed, the heating time is short, and the heating time of the liquid medicine is reduced by 50 percent.
The extraction tank is a normal-pressure container, so that the equipment cost is greatly reduced, the equipment manufacturing cost is low, the operation cost is low, and the overhaul cost is not needed; because the extraction tank is a normal pressure container, the feeding can be performed with positive pressure, vacuum and automatic feeding. In the traditional production process, extracting solution storage tanks with corresponding specifications and quantities need to be configured, the extracting solution storage tanks do not need to be configured in the prior art, the extracting solution from the extracting tank directly enters a concentrator for concentration, the extracting and the concentrating are carried out for 4 hours, the setting can be freely carried out, and the water boiling, the alcohol extraction, the decoction reflux and the solvent recovery are all suitable, so that the continuous production and the separate paste collection can be realized. Adopts a liquid flooding extraction method. High extraction rate, fast extraction, short extraction period, less solvent consumption, etc. and the loss rate of alcohol is less than 5%.
The extraction tank is provided with the extrusion solid-liquid separator, the medicine dregs are extruded and separated, the yield is improved, the yield can be increased by 10-20%, the water consumption is low, and the sewage discharge is reduced by 80%.
Be equipped with press device in the jar of drawing, prevent that the medicinal material from floating, total menstruum volume reduces 50%, and lower dregs of a decoction are equipped with vibrating device in the jar of drawing, prevent that the medicinal material from blockking up, conveniently lower the dregs of a decoction, have adopted back flush filter, convenient washing.
The utility model discloses the utilization ratio of complete equipment increases 30 ~ 40%, practices thrift labour 50%. In the original extraction and concentration process, fresh industrial steam is used for concentration, and after the process is changed, the concentrated heat source is secondary steam decocted in an extraction tank, so that the energy consumption is greatly reduced, and the total energy is saved by 70-80%.
Drawings
Fig. 1 is a flow chart of the apparatus of the present invention.
In the figure: 1-heater, 2-evaporating chamber, 3-extracting tank, 4-oil-collecting condensing device, 5-first effect heater, 6-first effect evaporating chamber, 7-second effect heater, 8-second effect evaporating chamber, 9-condenser, 10-cooler, 11-liquid-collecting tank, 12-vacuum buffer tank, 13-vacuum pump, 14-cooling water circulation tank, 15-second effect gas-liquid separator, 16-first effect gas-liquid separator, 17-back flushing filter, 18-circulating pump, 19-vibrating device, 20-extruding solid-liquid separator, 21-pressing device and 22-high pressure fan.
Detailed Description
For the purpose of facilitating understanding, the present invention will be explained in further detail below with reference to the accompanying drawings.
As shown in figure 1, the multifunctional extraction and concentration integrated equipment consists of a heater 1, an evaporation chamber 2, an extraction tank 3, an oil collection condensing device 4, a first-effect heater 5, a first-effect evaporation chamber 6, a second-effect heater 7, a second-effect evaporation chamber 8, a condenser 9, a cooler 10, a liquid collection tank 11, a vacuum buffer tank 12, a vacuum pump 13, a cooling water circulation tank 14, a second-effect gas-liquid separator 15, a first-effect gas-liquid separator 16 and a back-washing filter 17.
The heater 1 is connected with the evaporation chamber 2, the evaporation chamber 2 is connected with the extraction tank 3, and the heater 1 and the extraction tank 3 are both connected with the back flush filter 17; the extraction tank 3 is simultaneously connected with an oil collecting condensing device 4 and a first-effect heater 5, the first-effect heater 5 is connected with a first-effect evaporation chamber 6, the first-effect evaporation chamber 6 is connected with a second-effect heater 7, a first-effect gas-liquid separator 16 is simultaneously connected with the first-effect heater 5, the first-effect evaporation chamber 6 and the second-effect heater 7, the heater 1 is simultaneously connected with the first-effect heater 5 and the second-effect heater 7, the second-effect heater 7 is connected with the second-effect evaporation chamber 8, the second-effect evaporation chamber 8 is connected with a condenser 9, the condenser 9 is connected with a cooler 10, the cooler 10 is connected with a liquid collecting tank 11, the second-effect gas-liquid separator 15 is connected with the second-effect heater 7, the second-effect evaporation chamber 8 and a liquid collecting tank 11, the condenser 9 is connected with a vacuum buffer tank 12, the vacuum buffer tank 12 is connected with a vacuum pump; the extraction tank 3 is simultaneously connected with a first-effect heater 5 and a second-effect heater 7.
The utility model discloses in, the top of drawing jar 3 is connected through the connecting pipe in heater 1's upper portion, and the bottom of back flush filter 17 is connected through the connecting pipe in heater 1 bottom, installs circulating pump 18 between heater 1 and the back flush filter 17 in addition, and the bottom of drawing jar 3 is connected through the connecting pipe in back flush filter 17's upper portion, but draws the medicinal material in jar 3 through heater 1 circulation heating, and liquid medicine accessible bottom connecting pipe and back flush filter 17 flow back to heater 1. By adopting the novel circulating heating system, the time is shorter than that of the traditional jacket heating system, the heating time can be saved by 50 percent, and the energy is saved.
The heater 1 is connected with the evaporation chamber 2 through an upper connecting pipe and a lower connecting pipe, liquid medicine can be subjected to gas-liquid separation in the evaporation chamber, the top of the evaporation chamber 2 is connected with the extraction tank 3 through a pipeline, and separated secondary steam is sent into the extraction tank 3.
The bottom of the heater 1 is connected with the bottoms of the first-effect heater 5 and the second-effect heater 7 through pipelines, the liquid medicine can flow into the first-effect heater 5 and the second-effect heater 7, and the high-pressure fan 22 is arranged between the extraction tank 3 and the first-effect heater 5, so that the steam from the extraction tank is further heated and serves as a heat source for subsequent concentration. The primary-effect heater 5 is connected with the primary-effect evaporation chamber 6 through an upper connecting pipe and a lower connecting pipe, the secondary-effect heater 7 is connected with the secondary-effect evaporation chamber 8 through an upper connecting pipe and a lower connecting pipe, the top of the primary-effect evaporation chamber 6 is connected with the secondary-effect heater 7 through a pipeline, and secondary steam separated from the primary-effect evaporation chamber 6 serves as a heat source of the secondary-effect heater 7. The liquid medicine of the heater 1 is shunted to the first-effect heater 5 and the second-effect heater 7 for concentration, the efficiency is improved, the secondary steam of the extracting tank 3 and the secondary steam of the first-effect evaporation chamber 6 are secondarily utilized, and the heat utilization efficiency is improved. The energy is saved more, and the energy is saved,
the steam outlet of the double-effect evaporation chamber 8 is connected with a condenser 9 and a cooler 10, the discharge hole of the cooler 10 is connected with a liquid receiving tank 11, and the condensed liquid enters the liquid receiving tank 11 for temporary storage. The condenser 9 is connected with a vacuum buffer tank 12 through a pipeline, the vacuum buffer tank 12 is connected with a vacuum pump 13 through a pipeline, and the vacuum pump 13 is connected with a cooling water circulation tank 14 through a pipeline.
As shown in figure 1, a pressing device 21 is arranged in the extraction tank 3, and the light material can be fully contacted with the medium through the pressing device 21, so that the amount of the solvent can be reduced by 50%. In traditional extraction tank 3, no material device 21 (or anti-floating device) is pressed, and some lighter chinese-medicinal materials often float on the menstruum, can't fully contact with the menstruum, have influenced the extraction yield of medicinal material. The utility model discloses set up press device 21 in extracting the jar, press device 21 adopts pneumatic press device to be good, comprises cylinder and pressure flitch, and the pressure flitch is connected to the cylinder push rod, through the flexible of cylinder, makes to press the flitch to dip below the menstruum, blocks light medicinal material and floats, makes medicinal material and menstruum fully contact, is favorable to the active ingredient in the medicinal material to draw out completely.
The bottom of the extraction tank 3 is provided with an extrusion solid-liquid separator 20, which ensures that the liquid medicine is fully separated from the dregs of a decoction and can improve the yield by 10 to 20 percent. Traditional extraction process of slagging tap puts the back for the extract, opens the door of slagging tap, and the liquid medicine that the very high dregs of a decoction of water content is being mixed not putting to the greatest extent transports away or directly puts into the underground behind the car of slagging tap, and the loading is pulled away to artifical shovel, and this just causes the workshop environment abominable, and partial liquid medicine is lost. At present, the extrusion solid-liquid separator 20 is arranged below the extraction tank, the device has a slag extrusion function, extruded liquid medicine can be utilized, the extraction yield is increased, the slag is extruded and separated, the yield is improved, the yield can be increased by 10-20%, the water content of extruded slag is extremely low, the workshop environment and the transportation are not affected, the sewage discharge amount is reduced, and the sewage discharge amount is reduced by 80%.
The extracting tank 3 is provided with a vibrating device 19 to prevent the dregs from bridging and being difficult to discharge. A traditional extraction tank is not provided with a vibration device, and dregs of a decoction are arched in the tank (commonly called as 'bridging'), so that the dregs are difficult to discharge. The utility model discloses the vibrating device 19 that increases when the dregs of a decoction arch in jar knot, opens vibrating device 19, through the vibration, helps breaking the arch sediment of appearing completely, and the dregs of a decoction can be following basically completely.
The feeding mode of the extraction tank 3 is applicable to positive pressure, vacuum and automatic feeding.
The utility model discloses well two effect evaporation chamber 8 adopts the evaporation chamber of area receipts cream function, but equipment continuous production receives the cream alone.
The utility model discloses an extract concentrated process flow:
after the medicinal materials are put into the extraction tank 3, the solvent is added according to the proportion, the pressing device 21 is started, so that the medicinal materials are completely soaked in the solvent, and the medicinal materials are fully contacted with the solvent. Soaking for a period of time, circularly heating by a heater 1 to obtain volatile oil, and recovering the volatile oil by an oil collecting and condensing device 4;
closing a solvent circulation pipeline, opening valves of upper connecting pipes of a heater 1 and an evaporation chamber 2, enabling liquid medicine to enter the heater 1 and the evaporation chamber 2 through a backwashing filter 17, heating through the heater 1, enabling liquid medicine steam to enter the evaporation chamber 2 in a tangential direction, performing gas-liquid separation in the evaporation chamber, enabling separated secondary steam to enter an extraction tank 3, distributing through a distribution pipe, and continuously heating the liquid medicine in the extraction tank 3;
the secondary steam in the extraction tank 3 is pressurized by the high-pressure fan 22 and enters the first-effect heater 5 to serve as a heat source of the first-effect heater, the liquid medicine from the heater 1 is further heated, the secondary steam from the first-effect heater 5 enters the first-effect evaporation chamber 6 in the tangential direction, and gas-liquid separation is carried out in the first-effect evaporation chamber 6;
the secondary steam separated from the primary-effect evaporation chamber 6 is used as a heat source of the secondary-effect heater 7, the liquid medicine from the heater 1 is further heated, the secondary steam from the secondary-effect heater 7 enters the secondary-effect evaporation chamber 8 in the tangential direction, vapor-liquid separation is carried out in the secondary-effect evaporation chamber 8, the secondary steam separated from the secondary-effect evaporation chamber 8 enters the condenser 9 and the cooler 10, and the condensed liquid enters the liquid collecting tank 11 for temporary storage;
after the liquid medicine is concentrated to a certain specific gravity, the liquid medicine is poured into the double-effect evaporation chamber 8, a jacket heating system of the double-effect evaporation chamber 8 is opened, and the liquid medicine is further concentrated to obtain paste.
After extraction, the extraction tank 3 extrudes the residue by the extrusion solid-liquid separator 20 and discharges the residue, and the separated liquid medicine enters the heater 1 for concentration.
The utility model can select single-effect extraction concentration or double-effect extraction concentration according to the process after the traditional Chinese medicine liquid is extracted.
In the traditional production process, the extraction tank is used for statically heating and decocting medicinal materials and a solvent in the tank by introducing steam through a jacket, the heating time is long, the extraction tank belongs to a pressure container, potential safety hazards exist, and the extraction tank needs to be periodically monitored and checked by related departments. The existing extraction tank circularly heats the solvent by an external heater of the extraction tank, belongs to dynamic extraction, and has short heating time and 50 percent less heating time of liquid medicine.
The extraction tank is a normal-pressure container, so that the equipment cost is greatly reduced, the equipment manufacturing cost is low, the operation cost is low, and the overhaul cost is not needed; because the extraction tank is a normal pressure container, the feeding can be performed with positive pressure, vacuum and automatic feeding. In the traditional production process, extracting solution storage tanks with corresponding specifications and quantities need to be configured, the extracting solution storage tanks do not need to be configured in the prior art, the extracting solution from the extracting tank directly enters a concentrator for concentration, the extracting and the concentrating are carried out for 4 hours, the setting can be freely carried out, and the water boiling, the alcohol extraction, the decoction reflux and the solvent recovery are all suitable, so that the continuous production and the separate paste collection can be realized. Adopts a liquid flooding extraction method. High extraction rate, fast extraction, short extraction period, less solvent consumption, etc. and the loss rate of alcohol is less than 5%.
The utility model discloses the utilization ratio of complete equipment increases 30 ~ 40%, practices thrift labour 50%. In the original extraction and concentration process, fresh industrial steam is used for concentration, and after the process is changed, the concentrated heat source is secondary steam decocted in an extraction tank, so that the energy consumption is greatly reduced, and the total energy is saved by 70-80%.
The above embodiments are merely preferred embodiments of the present invention, and simple changes in the spirit or selection of relatively poor embodiments of the present invention shall also belong to the protection scope of the present invention.
Claims (9)
1. A multi-functional concentrated integrative equipment that draws, characterized by: including heater, evaporating chamber, draw the jar be equipped with the pipeline that supplies the liquid medicine circulation between heater and the pipeline evaporating chamber, still be equipped with between heater and the evaporating chamber and supply steam from the pipeline that the heater circulated to the evaporating chamber, the top steam outlet of evaporating chamber links to each other with the steam inlet who draws the jar, and the liquid medicine export of drawing the jar leads to the heater.
2. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: the oil recovery device comprises an extraction tank, an oil recovery condensing device, a first-effect heater, a second-effect heater, a condenser, a cooler, a liquid collection tank, a second-effect gas-liquid separator, a first-effect gas-liquid separator and a backwashing filter, wherein the extraction tank is connected with the oil recovery condensing device and the first-effect heater at the same time, the first-effect heater is connected with the first-effect evaporation chamber, the first-effect evaporation chamber is connected with the second-effect heater, the first-effect gas-liquid separator is connected with the first-effect heater, the first-effect evaporation chamber and the second-effect heater at the same time, the heater is connected with the first-effect heater and the second-effect heater at the same time, the second-effect heater is connected with the second-effect evaporation chamber, the second-effect evaporation chamber is connected with the condenser, the condenser is connected with the cooler, the cooler is connected with the liquid collection tank, the second-effect gas-liquid separator.
3. The multifunctional extraction and concentration integrated equipment as claimed in claim 2, wherein: the condenser is connected with the vacuum buffer tank, the vacuum buffer tank is connected with the vacuum pump, and the vacuum pump is connected with the cooling water circulation tank.
4. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: the upper part of the heater is connected with the top of the extraction tank through a connecting pipe, the bottom of the heater is connected with the bottom of the backwashing filter through a connecting pipe, a circulating pump is arranged between the heater and the backwashing filter, and the upper part of the backwashing filter is connected with the bottom of the extraction tank through a connecting pipe.
5. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: the heater is connected with the evaporation chamber through an upper connecting pipe and a lower connecting pipe, liquid medicine can be subjected to gas-liquid separation in the evaporation chamber, and the top of the evaporation chamber is connected with the extraction tank through a pipeline.
6. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: the bottom of the heater is connected with the bottoms of the first-effect heater and the second-effect heater through pipelines, liquid medicine can flow into the first-effect heater and the second-effect heater, and a high-pressure fan is arranged between the extraction tank and the first-effect heater; the first-effect heater is connected with the first-effect evaporation chamber through an upper connecting pipe and a lower connecting pipe, the second-effect heater is connected with the second-effect evaporation chamber through an upper connecting pipe and a lower connecting pipe, and the top of the first-effect evaporation chamber is connected with the second-effect heater through a pipeline.
7. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: and a material pressing device is arranged in the extraction tank.
8. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: and the bottom of the extraction tank is provided with an extrusion solid-liquid separator.
9. The multifunctional extraction and concentration integrated equipment as claimed in claim 1, wherein: and the extracting tank is provided with a vibrating device.
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| CN201921462480.8U CN210933840U (en) | 2019-09-04 | 2019-09-04 | Multifunctional extracting and concentrating integrated equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465108A (en) * | 2019-09-04 | 2019-11-19 | 江西赫柏康华制药设备有限公司 | The multi-functional extraction concentration integrated equipment of one kind and technique |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465108A (en) * | 2019-09-04 | 2019-11-19 | 江西赫柏康华制药设备有限公司 | The multi-functional extraction concentration integrated equipment of one kind and technique |
| CN110465108B (en) * | 2019-09-04 | 2024-01-19 | 江西赫柏康华制药设备有限公司 | Multifunctional extraction and concentration integrated equipment and process |
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