CN207237358U - Plant extract production line - Google Patents
Plant extract production line Download PDFInfo
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- CN207237358U CN207237358U CN201721194940.4U CN201721194940U CN207237358U CN 207237358 U CN207237358 U CN 207237358U CN 201721194940 U CN201721194940 U CN 201721194940U CN 207237358 U CN207237358 U CN 207237358U
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Abstract
The utility model provides a kind of plant extract production line, including dustless feed bin, presoak bubbler and extraction element, the feed inlet of the feeding port connection preimpregnation bubbler of dustless feed bin, presoak the feeding port one of the discharge port connection extraction element of bubbler, extraction element includes the first extraction equipment and the second extraction equipment, extraction element further includes discharger, plunger pump one, plunger pump two and temporary storage tank, slag-drip opening one is equipped with discharger, the discharge port of discharger is arranged on the top of the feeding port two of the second extraction equipment, the liquid outlet two of second extraction equipment connects the solvent entrance one of the first extraction equipment by plunger pump one；This kind of plant extract production line, cost is low and flow rate is high, can realize abundant immersion, so that in follow-up extraction processing so that active ingredient is more easy to extract, and energy saving and extraction efficiency is high.
Description
Technical field
It the utility model is related to a kind of plant extract production line.
Background technology
Plant extract mainly through crushing, immersion, extraction and etc. realization.At present in the extraction process of plant, utilize
Extraction equipment extract the elite composition in plant.Existing extraction equipment can use multicomputer process, multicomputer into
During row extraction processing, the discharger of previous unit is generally arranged at beside unit and lands setting, and discharger is pulled out after material residue again
Another group of extraction equipment is sent into by elevator, it is necessary to additionally realize the transmission of material using elevator under this mode, cost compared with
It is high.In addition, in existing production process, subsequent processing is entered after directly being condensed using extracting solution, causes heat waste, influenced
The lifting of efficiency.
Material is stored in feed bin after being pulverized.Current existing feed bin in use, due to material for particle or
It is powdered, easily it is detained in the inner wall of feed bin, forms buildup, it is impossible to smooth feeding.Meanwhile when material is admitted to feed bin, hold
Easily it is deposited at feed inlet, in the cone formed below of feed inlet, when the height of cone reaches feed inlet, can not continues
Space in the feed bin of charging, square column type or cylinder can only utilize about 1/3rd, it is impossible to realize efficiently using for space.
, it is necessary to be soaked to material during plant extract, the infuser device used at present is mainly using vertical
Formula steeping tank, after being soaked, direct feeding to subsequent processing is processed.Under such mode, there is material during immersion
Easily swim in the surface of water, it is impossible to fully immersion, the problem of causing efficiency to reduce, be not easy to extract.
The above problem is should to pay attention to and solve the problems, such as in the design process of plant extract production line.
Utility model content
The purpose of this utility model is to provide a kind of plant extract production line and solves needs existing in the prior art additionally
The transmission of material is realized using elevator, cost is higher, it is impossible to realize efficiently using for storage bin space, it is impossible to fully immersion,
Cause efficiency to reduce, be not easy to extract the problem of.
The technical solution of the utility model is：
A kind of plant extract production line, including dustless feed bin, preimpregnation bubbler and extraction element, the feeding port of dustless feed bin connect
The feed inlet of logical preimpregnation bubbler, presoaks the feeding port one of the discharge port connection extraction element of bubbler, and extraction element is carried including first
Taking equipment and the second extraction equipment, one end of the first extraction equipment are equipped with feeding port one, venthole one and liquid outlet one, and first carries
The other end of taking equipment is equipped with solvent entrance one, air intake one and slag-drip opening one, and one end of the second extraction equipment is equipped with feeding port
2nd, venthole two and liquid outlet two, the other end of the second extraction equipment are equipped with solvent entrance two, air intake two and slag-drip opening two,
Extraction element further includes discharger, plunger pump one, plunger pump two and temporary storage tank, and slag-drip opening one is equipped with discharger, and discharger goes out
Material mouth is arranged on the top of the feeding port two of the second extraction equipment, and the liquid outlet two of the second extraction equipment passes through the connection of plunger pump one the
The solvent entrance one of one extraction equipment.
Further, dustless feed bin includes suction equipment and storage bin, and suction equipment is equipped with drain hole, the top of storage bin
Equipped with feed inlet, feed inlet connects the drain hole of suction equipment, and storage bin includes holding material top and holds material lower part, holds material top and set
There is the top for holding material lower part, hold material lower part and use V-type, air blowing feed member is equipped with storage bin, and air blowing feed member is arranged on to hold and expects
Top and the junction for holding material lower part, air blowing feed member include gas bag and jet thrust, and jet thrust connects the gas outlet of gas bag, storing
Storehouse inner top, which is equipped with, puts down material component, and putting down material component includes putting down material motor peace material scraper plate, and the flat output shaft for expecting motor is connected to flat
Expect the middle part of scraper plate, bottom is equipped with feeding material component in storage bin, and feeding material component includes feeding motor and feeding spiral rod, feeding spiral shell
The output shaft of the end connection feeding motor of swing arm, the both ends of feeding spiral rod are respectively and movably connected to the bottom two of storage bin
Side.
Further, suction equipment uses negative pressure of vacuum suction equipment, and suction equipment includes Material sucking machine and vacuum pump, suction
The discharge port of the material sucking port connection pulverizer of machine, Material sucking machine connection vacuum pump, suction equipment further include dedusting tank, the row of Material sucking machine
Air port dedusting tank connection.
Further, jet thrust is towards the bottom of storage bin.
Further, preimpregnation bubbler use intermittent preimpregnation bubbler, intermittent preimpregnation bubbler including steeping tank, blender and
Stirring motor, the top of steeping tank are equipped with feed inlet, and the bottom of steeping tank is equipped with discharge port, is equipped with blender in steeping tank, stirs
Mix device to be driven by stirring motor, steeping tank uses horizontal steeping tank, and blender uses double spiral agitator, and blender includes stirring
Axis, right-handed screw paddle and backpitch paddle, right-handed screw paddle and backpitch paddle are arranged on agitating shaft.
Further, steeping tank and agitating shaft are coaxial configuration, and the both ends of steeping tank are respectively equipped with end cap, the two of agitating shaft
End is respectively and movably connected on end cap, and end cap is additionally provided with sealing.
Further, agitating shaft is equipped with some bracing pieces one and bracing piece two, and one end of bracing piece one is connected to agitating shaft
On, the other end of bracing piece one is connected on right-handed screw paddle, and one end of bracing piece two is connected on agitating shaft, bracing piece two
The other end be connected on right-handed screw paddle.
Further, the discharge port of steeping tank connects the feeding port one of the first extraction equipment by feeding with plunger pump.
Further, the liquid outlet one of the first extraction equipment connects temporary storage tank by plunger pump two, and temporary storage tank passes through plunger
Pump tee joint has heat reclaim unit, and heat reclaim unit includes First Heat Exchanger, the second heat exchanger and condenser, the first heat exchange
The Heating medium one of device connects the outlet pipe of Chinese medicine extractor, one the second heat exchanger of connection of heating agent outlet of First Heat Exchanger
Heating medium two, the second heat exchanger heating agent outlet two connection condensers inlets, condenser be additionally provided with liquid outlet, cooling
Water inlet and cooling water outlet, the refrigerant inlet two of the second heat exchanger connect pure water pump, and the refrigerant exit two of the second heat exchanger connects
The refrigerant inlet one of logical First Heat Exchanger, First Heat Exchanger are additionally provided with refrigerant exit one, and refrigerant exit one connects steam generator,
Steam generator is respectively communicated with the air intake two of the air intake one of the first extraction equipment, the second extraction equipment.
The beneficial effects of the utility model are：
First, this kind of plant extract production line, the top of the feeding port two by the way that discharger to be arranged on to the second extraction equipment,
The second extraction equipment can be directly entered by high potential difference material, realizes that material conveys without using elevator, can drop
Low processing cost.This kind of plant extract production line, the liquid outlet two of the second extraction equipment pass through first extraction of the connection of plunger pump one
The solvent entrance one of equipment, it is possible to increase flow rate, reduces failure rate.This kind of plant extract production line, it is reasonable in design, into
This low and flow rate is high, beneficial to production and application.
2nd, in the utility model, dustless feed bin is implemented in combination with feeding by vibration with air blowing two ways, can realize suitable
Sharp high efficiency feeding, is guarded without personnel, solves the problems, such as that the discharging efficiency that has some setbacks is low.By setting flat material component, can avoid
Solid accumulation so that cloth is uniform, so that avoid the problem that both sides space cannot efficiently use inside storage bin after solid accumulation,
So as to realize the space availability ratio of higher.
3rd, in the utility model, after preimpregnation bubbler enables to material to enter steeping tank, fully immersion is realized, so that
In follow-up extraction processing so that active ingredient is more easy to extract.By setting double spiral agitator, two-way stirring material can
Avoid the problem that material swims in liquid surface and cannot fully soak.The stirring of double spiral agitator can be in material in steeping tank
It is interior to be sufficiently mixed with liquid, ensure abundant immersion, shorten subsequent extracted process time more than 20%, reduce processing cost, improve and add
Work efficiency rate.
4th, this kind of plant extract production line, heat reclaim unit, by setting First Heat Exchanger, the second heat exchanger, is realized
Effective recycling to the heat of extracting solution, while realizing energy saving purpose, can effectively improve efficiency more than 20%.Can be real
Feed liquor while now changing liquid, does not influence being carried out continuously for production, after heat exchange, can realize energy saving more than 45%.
Brief description of the drawings
Fig. 1 is the structure diagram of the utility model embodiment plant extract production line；
Fig. 2 is the structure diagram of extraction element in embodiment；
Fig. 3 is the structure diagram of dustless feed bin in embodiment；
Fig. 4 is the structure diagram of storage bin in embodiment；
Fig. 5 is the structure diagram that bubbler is presoaked in embodiment；
Fig. 6 is the structure diagram of heat reclaim unit in embodiment；
Wherein：The dustless feed bins of 1-, 2- preimpregnation bubblers, 3- extraction elements, 4- heat reclaim units, 5- feeding plunger pumps；
11- storage bins, 12- jet thrusts, 13- put down material motor, and 14- puts down material scraper plate, 15- feeding motors, 16- feeding screws
Bar, 17- Material sucking machines, 18- vacuum pumps, 19- dedusting tanks, 110- pulverizers；11- holds material top, and 112- holds material lower part.
21- steeping tanks, 22- stirring motors, 23- agitating shafts, 24- right-handed screw paddles, 25- backpitch paddles, 26- ends
Lid, 27- sealings, 28- retarders, 29- feed inlets, 210- discharge ports, 211- bracing pieces one, 212- bracing pieces two.
The first extraction equipments of 31-, the second extraction equipments of 32-, 33- dischargers, 34- steam generators, 35- feeding ports one,
36- liquid outlets one, 37- solvents entrance one, 38- feeding ports two, 39- liquid outlets two, 310- plunger pumps one, 311- plunger pumps two,
312- temporary storage tanks；
41- First Heat Exchangers, the second heat exchangers of 42-, 43- Heating mediums one, 44- heating agents outlet one, 45- Heating mediums
Two, 46- heating agent outlet two, 47- condensers, 48- inlets, 49- liquid outlets, 410- cooling water inlets, 411- cooling water outlets,
412- refrigerant inlets one, 413- refrigerant inlets two, 414- refrigerant exits one, 415- refrigerant exits two, 416- pure water pumps.
Embodiment
Describe the preferred embodiment of the utility model in detail below in conjunction with the accompanying drawings.
Embodiment
A kind of plant extract production line, such as Fig. 1, including dustless feed bin 1, preimpregnation bubbler 2 and extraction element 3, dustless feed bin 1
Feeding port connection preimpregnation bubbler 2 feed inlet, preimpregnation bubbler 2 discharge port connection extraction element 3 feeding port 1, extraction
Device 3 includes the first extraction equipment 31 and the second extraction equipment 32, and one end of the first extraction equipment 31 is equipped with feeding port 1, goes out
Steam ports one and liquid outlet 1, the other end of the first extraction equipment 31 are equipped with solvent entrance 1, air intake one and slag-drip opening one,
One end of second extraction equipment 32 is equipped with feeding port 2 38, venthole two and liquid outlet 2 39, the second extraction equipment 32 it is another
End is equipped with solvent entrance two, air intake two and slag-drip opening two, further includes discharger 33, plunger pump 1,2 311 and of plunger pump
Temporary storage tank 312, slag-drip opening one are equipped with discharger 33, and the discharge port of discharger 33 is arranged on the feeding port 2 38 of the second extraction equipment 32
Top, the liquid outlet 2 39 of the second extraction equipment 32 passes through the solvent entrance that plunger pump 1 connects the first extraction equipment 31
One 37, counterflow extraction apparatus is respectively adopted in the first extraction equipment 31 and the second extraction equipment 32.
This kind of plant extract production line, by discharger 33 is arranged on the second extraction equipment 32 feeding port 2 38 it is upper
Side, can be directly entered the second extraction equipment 32 by high potential difference material, realize that material conveys without using elevator, energy
Enough reduce processing cost.This kind of plant extract production line, the liquid outlet 2 39 of the second extraction equipment 32 are connected by plunger pump 1
The solvent entrance 1 of logical first extraction equipment 31, it is possible to increase flow rate, reduces failure rate.This kind of plant extract production line,
Reasonable in design, cost is low and flow rate is high, beneficial to production and application.
Such as Fig. 3, dustless feed bin 1 includes suction equipment and storage bin 11 in embodiment, and suction equipment is equipped with drain hole, storing
The top in storehouse 11 is equipped with feed inlet, and feed inlet connects the drain hole of suction equipment, and storage bin 11 includes holding material top 111 and holding expecting
Lower part 112, holds material top 111 and is equipped with the top for holding material lower part 112, holds material lower part 112 and uses V-type, such as Fig. 4, in storage bin 11
Equipped with air blowing feed member, and air blowing feed member is arranged on the junction for holding material top 111 and holding material lower part 112, air blowing feed member bag
Gas bag and jet thrust 12 are included, jet thrust 12 connects the gas outlet of gas bag, and 11 inner top of storage bin is equipped with flat material component, puts down material component
Including flat 13 peace material scraper plate 14 of material motor, the output shaft of flat material motor 13 is connected to the middle part of flat material scraper plate 14, storage bin 11
Interior bottom is equipped with feeding material component, and feeding material component includes feeding motor 15 and feeding spiral rod 16, and the end of feeding spiral rod 16 connects
The output shaft of feeding motor 15, the both ends of feeding spiral rod 16 are respectively and movably connected to the two bottom sides of storage bin 11.
Dustless feed bin 1 can avoid solid accumulation by setting flat material component in embodiment so that and cloth is uniform, so that
11 inside both sides space of storage bin cannot efficiently use after avoiding the problem that solid accumulation, so as to realize the space of higher profit
With rate.By air blowing feed member, the buildup at slope in storage bin 11 is carried out by air blowing feeding by jet thrust 12, avoids slope
The problem of buildup.By the feeding material component of bottom, the conveying of material in storage bin 11 is realized, storage bin 11 is held under material using V-type
Portion 112, feeding material component are arranged on the least significant end for holding material lower part 112, can realize most effective feeding.Dustless feed bin 1 is by shaking
It is dynamic to be implemented in combination with feeding with air blowing two ways, it can realize smooth high efficiency feeding, be guarded without personnel, solve discharging and have some setbacks
The problem of efficiency is low.
Suction equipment uses negative pressure of vacuum suction equipment, and suction equipment includes Material sucking machine 17 and vacuum pump 18, Material sucking machine 17
Material sucking port connection pulverizer discharge port, Material sucking machine 17 connect vacuum pump 18.Suction equipment further includes dedusting tank 19, dedusting tank
The exhaust outlet of 19 connection Material sucking machines 17.The suction of material is realized by negative pressure of vacuum suction equipment, and by dedusting tank 19, is realized
Dedusting purpose.
The feed inlet both sides of storage bin 11 are respectively equipped with flat material component.By flat material component, realize equal in storage bin 11
Even cloth, avoids solid accumulation at feed inlet.Jet thrust 12 is further ensured that air blowing feeding to sending towards the bottom of storage bin 11
Expect component.
Bubbler 2 is presoaked using intermittent preimpregnation bubbler 2, such as Fig. 5, including steeping tank 21, blender and stirring motor 22, leaching
The top of bubble tank 21 is equipped with feed inlet 29, and the bottom of steeping tank 21 is equipped with discharge port 210, is equipped with blender in steeping tank 21, stirs
Mix device to be driven by stirring motor 22, steeping tank 21 uses horizontal steeping tank 21, and blender uses double spiral agitator, blender bag
Agitating shaft 23, right-handed screw paddle 24 and backpitch paddle 25 are included, right-handed screw paddle 24 and backpitch paddle 25 are all provided with
In on agitating shaft 23.
After preimpregnation bubbler 2 enables to material to enter steeping tank 21 in embodiment, fully immersion is realized, so that follow-up
In extraction processing so that active ingredient is more easy to extract.By setting double spiral agitator, two-way stirring material, can avoid thing
Material swims in the problem of liquid surface cannot fully soak.The stirring of double spiral agitator can material in the steeping tank 21 with
Liquid is sufficiently mixed, and is ensured fully immersion, is shortened subsequent extracted process time more than 20%, reduces processing cost, improves processing effect
Rate.
The use process of preimpregnation bubbler 2 is specially in embodiment：After the water of 1/3 volume is added in steeping tank 21, add
Material, when stirring immersion 2 is small.After using the immersion of the intermittent preimpregnation bubbler 2 of embodiment, it is not necessary to which large-scale high-power extraction is set
It is standby, extraction rate reached can be caused to more than 95%.
Steeping tank 21 and agitating shaft 23 are coaxial configuration, and the both ends of steeping tank 21 are respectively equipped with end cap 26, agitating shaft 23
Both ends are respectively and movably connected on end cap 26, and end cap 26 is additionally provided with sealing 27.It is equipped with and slows down between stirring motor 22 and blender
Device 28, stirring motor 22 are arranged on base, and steeping tank 21 is arranged on chassis.
Discharge port 210 connects the feeding port of extraction element 3 by charging line one, feeding plunger pump 5, charging line two
One 35.By feeding plunger pump 5, it can ensure solid and liquid synchronous transport, and can realize long distance delivery.Steeping tank
21 are additionally provided with manhole and visor.Easy to observe immersion situation in steeping tank 21.
Agitating shaft 23 is equipped with some bracing pieces 1 and bracing piece 2 212, and one end of bracing piece 1 is connected to stirring
On axis 23, the other end of bracing piece 1 is connected on right-handed screw paddle 24, and one end of bracing piece 2 212 is connected to stirring
On axis 23, the other end of bracing piece 2 212 is connected on right-handed screw paddle 24.Embodiment is by setting bracing piece 1, adding
Strong bar 2 212, by increasing capacitance it is possible to increase right-handed screw paddle 24, backpitch paddle 25 fixation stability, extend usage time, and
Stirring dynamics knead dough product can be increased, material is quickly realized abundant immersion.
Such as Fig. 2 and Fig. 6, the liquid outlet 1 of the first extraction equipment 11 connects temporary storage tank 112 by plunger pump 2 111.Temporarily
Deposit tank 112 has heat reclaim unit 4 by plunger pump tee joint.Such as Fig. 6, heat reclaim unit 4 includes First Heat Exchanger 41, the
Two heat exchangers 42 and condenser 47, the Heating medium 1 of First Heat Exchanger 41 connect the outlet pipe of Chinese medicine extractor, the
The Heating medium 2 45 of one 44 the second heat exchanger 42 of connection of heating agent outlet of one heat exchanger 41, the heating agent outlet of the second heat exchanger 42
The inlet 48 of 2 46 connection condensers 47, condenser 47 are additionally provided with liquid outlet 49, cooling water inlet 410 and cooling water outlet
411, the refrigerant inlet 2 413 of the second heat exchanger 42 connects pure water pump 416, and the refrigerant exit 2 415 of the second heat exchanger 42 connects
The refrigerant inlet 1 of First Heat Exchanger 41, First Heat Exchanger 41 are additionally provided with refrigerant exit 1.
By setting First Heat Exchanger 41, the second heat exchanger 42, realize effective recycling to the heat of extracting solution, realize section
While the purpose of energy, efficiency more than 20% can be effectively improved.This kind is used for the heat reclaim unit 4 of Chinese medicine extractor, energy
Feed liquor while liquid is changed in enough realizations, does not influence being carried out continuously for production, after heat exchange, can realize energy saving more than 45%.
The process of realizing of heat reclaim unit 4 is specially：Extracting solution in the outlet pipe of Chinese medicine extractor is through heating agent
Import 1 enters First Heat Exchanger 41, after First Heat Exchanger 41 and pure water carry out heat exchange, by the heat of First Heat Exchanger 41
Matchmaker outlet 1 enters the Heating medium 2 45 of the second heat exchanger 42, carries out heat exchange with pure water in the second heat exchanger 42 again
Afterwards, after condenser 47, into next workshop section；Pure water is entered the refrigerant inlet two of the second heat exchanger 42 by pure water pump 416
413, after carrying out heat exchange with extracting solution, the refrigerant of First Heat Exchanger 41 is entered by the refrigerant exit 2 415 of the second heat exchanger 42
Import 1, after carrying out heat exchange with extracting solution again, is gone out by the refrigerant exit 1 of First Heat Exchanger 41, completes heat exchange
Process.
Refrigerant exit 1 connects steam generator 13, steam generator 13 be respectively communicated with the first extraction equipment 1 into vapour
The air intake two of the one, second extraction equipment 2 of mouth.Into the pure water temperature after heat exchange excessively about at 45 °C, into steam generator
13 be vaporized after use.Condenser 47 uses shell and tube condenser 47.It is outer respectively outside First Heat Exchanger 41, the second heat exchanger 42
It is covered with thermal insulation layer.Realize that heat is isolated, avoid dissipating outside heat, improve organic efficiency.
Claims (9)
1. a kind of plant extract production line, including dustless feed bin, preimpregnation bubbler and extraction element, the feeding port connection of dustless feed bin
The feed inlet of bubbler is presoaked, presoaks the feeding port one of the discharge port connection extraction element of bubbler, extraction element includes the first extraction
Equipment and the second extraction equipment, one end of the first extraction equipment are equipped with feeding port one, venthole one and liquid outlet one, the first extraction
The other end of equipment is equipped with solvent entrance one, air intake one and slag-drip opening one, one end of the second extraction equipment be equipped with feeding port two,
Venthole two and liquid outlet two, the other end of the second extraction equipment are equipped with solvent entrance two, air intake two and slag-drip opening two, it is special
Sign is：Extraction element further includes discharger, plunger pump one, plunger pump two and temporary storage tank, and slag-drip opening one is equipped with discharger, discharging
The discharge port of device is arranged on the top of the feeding port two of the second extraction equipment, and the liquid outlet two of the second extraction equipment passes through plunger pump one
Connect the solvent entrance one of the first extraction equipment.
2. plant extract production line as claimed in claim 1, it is characterised in that：Dustless feed bin includes suction equipment and storing
Storehouse, suction equipment are equipped with drain hole, and the top of storage bin is equipped with feed inlet, and feed inlet connects the drain hole of suction equipment, storing
Storehouse includes holding material top and holds material lower part, holds material top and is equipped with the top for holding material lower part, holds material lower part and uses V-type, in storage bin
Equipped with air blowing feed member, and air blowing feed member is arranged on the junction for holding material top and holding material lower part, and air blowing feed member includes gas bag
And jet thrust, jet thrust connect the gas outlet of gas bag, storage bin inner top is equipped with flat material component, and putting down material component includes flat material motor
Peace material scraper plate, the output shaft of flat material motor are connected to the middle part of flat material scraper plate, and bottom is equipped with feeding material component, feeding in storage bin
Component includes feeding motor and feeding spiral rod, the output shaft of the end connection feeding motor of feeding spiral rod, feeding spiral rod
Both ends be respectively and movably connected to the two bottom sides of storage bin.
3. plant extract production line as claimed in claim 2, it is characterised in that：Suction equipment is set using negative pressure of vacuum suction
Standby, suction equipment includes Material sucking machine and vacuum pump, the discharge port of the material sucking port connection pulverizer of Material sucking machine, Material sucking machine connection vacuum
Pump, suction equipment further include dedusting tank, the exhaust outlet dedusting tank connection of Material sucking machine.
4. plant extract production line as claimed in claim 3, it is characterised in that：Jet thrust is towards the bottom of storage bin.
5. plant extract production line as claimed in claim 1, it is characterised in that：Preimpregnation bubbler uses intermittent preimpregnation bubbler,
Intermittent preimpregnation bubbler includes steeping tank, blender and stirring motor, and the top of steeping tank is equipped with feed inlet, the bottom of steeping tank
Equipped with discharge port, blender is equipped with steeping tank, blender is driven by stirring motor, and steeping tank uses horizontal steeping tank, stirring
Device uses double spiral agitator, and blender includes agitating shaft, right-handed screw paddle and backpitch paddle, right-handed screw paddle and
Backpitch paddle is arranged on agitating shaft.
6. plant extract production line as claimed in claim 5, it is characterised in that：Steeping tank and agitating shaft are coaxial configuration, leaching
The both ends of bubble tank are respectively equipped with end cap, and the both ends of agitating shaft are respectively and movably connected on end cap, and end cap is additionally provided with sealing.
7. plant extract production line as claimed in claim 5, it is characterised in that：Agitating shaft is equipped with some bracing pieces one and strengthens
Bar two, one end of bracing piece one are connected on agitating shaft, and the other end of bracing piece one is connected on right-handed screw paddle, bracing piece
Two one end is connected on agitating shaft, and the other end of bracing piece two is connected on right-handed screw paddle.
8. plant extract production line as claimed in claim 5, it is characterised in that：The discharge port of steeping tank passes through feeding plunger
The feeding port one of pump the first extraction equipment of connection.
9. plant extract production line as claimed in claim 1, it is characterised in that：The liquid outlet one of first extraction equipment passes through column
Two connection temporary storage tank of plug pump, temporary storage tank have heat reclaim unit by plunger pump tee joint, and heat reclaim unit is changed including first
Hot device, the second heat exchanger and condenser, the outlet pipe of the connection Chinese medicine extractor of Heating medium one of First Heat Exchanger, first
The Heating medium two of one the second heat exchanger of connection of heating agent outlet of heat exchanger, the two connection condenser of heating agent outlet of the second heat exchanger
Inlet, condenser is additionally provided with liquid outlet, cooling water inlet and cooling water outlet, and the refrigerant inlet two of the second heat exchanger connects
Pure water pump, the refrigerant exit two of the second heat exchanger connect the refrigerant inlet one of First Heat Exchanger, and First Heat Exchanger is additionally provided with refrigerant
Outlet one, refrigerant exit one connect steam generator, and steam generator is respectively communicated with the air intake one, second of the first extraction equipment
The air intake two of extraction equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721194940.4U CN207237358U (en) | 2017-09-18 | 2017-09-18 | Plant extract production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721194940.4U CN207237358U (en) | 2017-09-18 | 2017-09-18 | Plant extract production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207237358U true CN207237358U (en) | 2018-04-17 |
Family
ID=61889191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721194940.4U Active CN207237358U (en) | 2017-09-18 | 2017-09-18 | Plant extract production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207237358U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107497137A (en) * | 2017-09-18 | 2017-12-22 | 江苏华泰重工装备有限公司 | Plant extract production line |
-
2017
- 2017-09-18 CN CN201721194940.4U patent/CN207237358U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107497137A (en) * | 2017-09-18 | 2017-12-22 | 江苏华泰重工装备有限公司 | Plant extract production line |
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