CN208659926U - Height circulation extract equipment - Google Patents
Height circulation extract equipment Download PDFInfo
- Publication number
- CN208659926U CN208659926U CN201721194310.7U CN201721194310U CN208659926U CN 208659926 U CN208659926 U CN 208659926U CN 201721194310 U CN201721194310 U CN 201721194310U CN 208659926 U CN208659926 U CN 208659926U
- Authority
- CN
- China
- Prior art keywords
- extract equipment
- heat exchanger
- equipment
- plunger pump
- liquid outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model provides a kind of high circulation extract equipment, including the first extract equipment and the second extract equipment, it further include 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 set to the top of the feeding port two of the second extract equipment, the liquid outlet two of second extract equipment is connected to the solvent entrance one of the first extract equipment by plunger pump one, and the liquid outlet one of the first extract equipment is connected to temporary storage tank by plunger pump two；The high circulation extract equipment of this kind, the top of the feeding port two by the way that discharger to be arranged in the second extract equipment can be made material be directly entered the second extract equipment by high potential difference, without using elevator, can reduce processing cost.The liquid outlet two of second extract equipment is connected to the solvent entrance one of the first extract equipment by plunger pump one, can be improved flow rate, reduces failure rate.The high circulation extract equipment of this kind, reasonable in design, at low cost and flow rate is high, is conducive to produce and use.
Description
Technical field
The utility model relates to a kind of high circulation extract equipments.
Background technique
In the extraction process of Chinese medicine, the essence composition in Chinese medicine is extract using extract equipment.It is existing at present
Multicomputer processing can be used in extract equipment, and when multicomputer extracts processing, the discharger of previous unit is generally arranged at machine
Setting is simultaneously landed in group side, and discharger, which is pulled out after material residue, is sent into another group of extract equipment by elevator again, under this mode, needs
Additionally use elevator, higher cost.In addition, entering next work after directly condensing using extracting solution in existing production process
Sequence causes heat waste, affects the promotion of efficiency.
The above problem is should to pay attention to and solve the problems, such as in the design process of extract equipment.
Utility model content
The purpose of the utility model is to provide a kind of high circulation extract equipments to solve existing in the prior art need additionally
Using elevator, the problem of higher cost.
The technical solution of the utility model is:
A kind of high circulation extract equipment, including the first extract equipment and the second extract equipment, one end of the first extract equipment
Equipped with feeding port one, venthole one and liquid outlet one, the other end of the first extract equipment is equipped with solvent entrance one, one and of air intake
Slag-drip opening one, one end of the second extract equipment are equipped with feeding port two, venthole two and liquid outlet two, the second extract equipment it is another
End is equipped with solvent entrance two, air intake two and slag-drip opening two, further includes discharger, plunger pump one, plunger pump two and temporary storage tank, row
Cinder notch one is equipped with discharger, and the discharge port of discharger is set to the top of the feeding port two of the second extract equipment, the second extract equipment
Liquid outlet two the solvent entrance one of the first extract equipment is connected to by plunger pump one, the liquid outlet one of the first extract equipment passes through
Plunger pump two is connected to temporary storage tank.
Further, counterflow extraction apparatus is respectively adopted in the first extract equipment and the second extract equipment.
Further, temporary storage tank has heat reclaim unit by plunger pump tee joint.
Further, heat reclaim unit includes First Heat Exchanger, the second heat exchanger and condenser, the heat of First Heat Exchanger
Matchmaker's import one is connected to the liquid outlet pipe of Chinese medicine extractor, the heating agent of one the second heat exchanger of connection of heating agent outlet of First Heat Exchanger
Import two, the inlet of the two connection condenser of heating agent outlet of the second heat exchanger, condenser are additionally provided with liquid outlet, cooling water inlet
And cooling water outlet, the refrigerant inlet two of the second heat exchanger are connected to pure water pump, the connection of refrigerant exit two first of the second heat exchanger
The refrigerant inlet one of heat exchanger, First Heat Exchanger are additionally provided with refrigerant exit one, and refrigerant exit one is connected to steam generator, steam hair
Raw device is respectively communicated with the air intake two of the air intake one of the first extract equipment, the second extract equipment.
Further, condenser uses shell and tube condenser.
Further, thermal insulation layer is covered with outside First Heat Exchanger, the second heat exchanger respectively.
The beneficial effects of the utility model are: the high circulation extract equipment of this kind, by the way that discharger setting is extracted second
The top of the feeding port two of equipment can make material be directly entered the second extract equipment by high potential difference, without using being promoted
Machine can reduce processing cost.The high circulation extract equipment of this kind, the liquid outlet two of the second extract equipment are connected to by plunger pump one
The solvent entrance one of first extract equipment can be improved flow rate, reduce failure rate.The high circulation extract equipment of this kind, structure are set
Rationally, at low cost and flow rate is high for meter, is conducive to produce and use.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model embodiment；
Fig. 2 is the structural schematic diagram of heat reclaim unit in embodiment；
Wherein: the first extract equipment of 1-, the second extract equipment of 2-, 3- discharger, 4- heat reclaim unit, 5- feeding port
One, 6- liquid outlet one, 7- solvent entrance one, 8- feeding port two, 9- liquid outlet two, 10- plunger pump one, 11- plunger pump two, 12-
Temporary storage tank, 13- steam generator；
41- First Heat Exchanger, the second heat exchanger of 42-, 43- Heating medium one, 44- heating agent export one, 45- Heating medium
Two, 46- heating agent outlet two, 47- condenser, 48- inlet, 49- liquid outlet, 410- cooling water inlet, 411- cooling water outlet,
412- refrigerant inlet one, 413- refrigerant inlet two, 414- refrigerant exit one, 415- refrigerant exit two, 416- pure water pump.
Specific embodiment
The preferred embodiment that according to the present invention will be described in detail below with reference to the accompanying drawings.
Embodiment
A kind of high circulation extract equipment, such as Fig. 1, including the first extract equipment 1 and the second extract equipment 2, the first extraction are set
Standby 1 one end is equipped with feeding port 1, venthole one and liquid outlet 1, and the other end of the first extract equipment 1 is equipped with solvent entrance
One 7, one end of air intake one and slag-drip opening one, the second extract equipment 2 is equipped with feeding port 28, venthole two and liquid outlet 29,
The other end of second extract equipment 2 is equipped with solvent entrance two, air intake two and slag-drip opening two, further includes discharger 3, plunger pump one
10, plunger pump 2 11 and temporary storage tank 12, slag-drip opening one are equipped with discharger 3, and the discharge port of discharger 3 is set to the second extract equipment 2
Feeding port 28 top, the liquid outlet 29 of the second extract equipment 2 is connected to the molten of the first extract equipment 1 by plunger pump 1
The liquid outlet 1 of matchmaker's entrance 1, the first extract equipment 1 is connected to temporary storage tank 12 by plunger pump 2 11.First extract equipment, 1 He
Counterflow extraction apparatus is respectively adopted in second extract equipment 2.
The high circulation extract equipment of this kind, the top of the feeding port 28 by the way that discharger 3 to be arranged in the second extract equipment 2,
Material can be made to be directly entered the second extract equipment 2 by high potential difference, material conveying is realized without using elevator, can drop
Low processing cost.The liquid outlet 29 of the high circulation extract equipment of this kind, the second extract equipment 2 passes through the connection of plunger pump 1 first
The solvent entrance 1 of extract equipment 1 can be improved flow rate, reduce failure rate.The high circulation extract equipment of this kind, structure design
Rationally, at low cost and flow rate is high, is conducive to produce and use.
Temporary storage tank 12 has heat reclaim unit 4 by plunger pump tee joint.Such as Fig. 2, heat reclaim unit 4 is changed including first
Hot device 41, the second heat exchanger 42 and condenser 47, the Heating medium 1 of First Heat Exchanger 41 are connected to going out for Chinese medicine extractor
Liquid pipe road, the Heating medium 2 45 of one 44 the second heat exchanger 42 of connection of heating agent outlet of First Heat Exchanger 41, the second heat exchanger 42
2 46 connection condensers 47 of heating agent outlet inlets 48, condenser 47 is additionally provided with liquid outlet 49, cooling water inlet 410 and cold
But the refrigerant inlet 2 413 of water out 411, the second heat exchanger 42 is connected to pure water pump 416, the refrigerant exit two of the second heat exchanger 42
The refrigerant inlet 1 of 415 connection First Heat Exchangers 41, First Heat Exchanger 41 are additionally provided with refrigerant exit 1.
By the way that First Heat Exchanger 41, the second heat exchanger 42 is arranged, realizes effective recycling to the heat of extracting solution, realize section
While the purpose of energy, 20% or more efficiency 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 be realized 45% or more energy conservation.
The realization process of heat reclaim unit 4 specifically: the extracting solution in the liquid 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 is gone out after carrying out heat exchange with extracting solution again by the refrigerant exit 1 of First Heat Exchanger 41, completes heat exchange
Process.
Refrigerant exit 1 is connected to steam generator 13, steam generator 13 be respectively communicated with the first extract equipment 1 into vapour
The air intake two of the one, second extract 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.It realizes heat isolation, avoids dissipating outside heat, improve recovery efficiency.
Claims (6)
1. a kind of high circulation extract equipment, including the first extract equipment and the second extract equipment, one end of the first extract equipment are set
There are feeding port one, venthole one and liquid outlet one, the other end of the first extract equipment is equipped with solvent entrance one, air intake one and row
One end of cinder notch one, the second extract equipment is equipped with feeding port two, venthole two and liquid outlet two, the other end of the second extract equipment
Equipped with solvent entrance two, air intake two and slag-drip opening two, it is characterised in that: further include discharger, plunger pump one, two and of plunger pump
Temporary storage tank, slag-drip opening one are equipped with discharger, and the discharge port of discharger is set to the top of the feeding port two of the second extract equipment, and second
The liquid outlet two of extract equipment is connected to the solvent entrance one of the first extract equipment by plunger pump one, and the first extract equipment goes out liquid
Mouth one is connected to temporary storage tank by plunger pump two.
2. high circulation extract equipment as described in claim 1, it is characterised in that: the first extract equipment and the second extract equipment point
It Cai Yong not counterflow extraction apparatus.
3. high circulation extract equipment as described in claim 1, it is characterised in that: temporary storage tank has heat by plunger pump tee joint
Recyclable device.
4. circulation extract equipment as described in claim 1 high, it is characterised in that: heat reclaim unit include First Heat Exchanger,
Second heat exchanger and condenser, the Heating medium one of First Heat Exchanger are connected to the liquid outlet pipe of Chinese medicine extractor, the first heat exchange
Device heating agent outlet one connection the second heat exchanger Heating medium two, the second heat exchanger heating agent outlet two connection condensers into
Liquid mouth, condenser are additionally provided with liquid outlet, cooling water inlet and cooling water outlet, and the refrigerant inlet two of the second heat exchanger is connected to pure water
Pump, the refrigerant exit two of the second heat exchanger are connected to the refrigerant inlet one of First Heat Exchanger, and First Heat Exchanger is additionally provided with refrigerant exit
One, refrigerant exit one is connected to steam generator, and the air intake one, second that steam generator is respectively communicated with the first extract equipment extracts
The air intake two of equipment.
5. high circulation extract equipment as claimed in claim 4, it is characterised in that: condenser uses shell and tube condenser.
6. high circulation extract equipment as claimed in claim 4, it is characterised in that: outside First Heat Exchanger, the second heat exchanger respectively
It is covered with thermal insulation layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721194310.7U CN208659926U (en) | 2017-09-18 | 2017-09-18 | Height circulation extract equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721194310.7U CN208659926U (en) | 2017-09-18 | 2017-09-18 | Height circulation extract equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208659926U true CN208659926U (en) | 2019-03-29 |
Family
ID=65819471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721194310.7U Expired - Fee Related CN208659926U (en) | 2017-09-18 | 2017-09-18 | Height circulation extract equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208659926U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107510601A (en) * | 2017-09-18 | 2017-12-26 | 江苏华泰重工装备有限公司 | Height circulation extraction equipment |
-
2017
- 2017-09-18 CN CN201721194310.7U patent/CN208659926U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107510601A (en) * | 2017-09-18 | 2017-12-26 | 江苏华泰重工装备有限公司 | Height circulation extraction equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107008026A (en) | Nickel sulfate evaporative crystallization technique | |
| CN206001743U (en) | Absorption type heat pump system | |
| CN107619078A (en) | A kind of device of method treatment of acidic wastewater using concentration stripping | |
| CN106196727B (en) | A kind of heat pump system and its operation method | |
| CN207501713U (en) | A kind of jacketed spiral winded type condenser | |
| CN208659926U (en) | Height circulation extract equipment | |
| CN106196718B (en) | Absorption type heat pump system and its round-robin method | |
| CN106746118A (en) | A kind of system and method for utilization heat recovery from sewage alcohol ketone | |
| CN105271324B (en) | A kind of low pressure exhaust steam recycling system | |
| CN109248467A (en) | A kind of technique extracting total-tanshinone from Radix Salviae Miltiorrhizae | |
| CN205953539U (en) | Scrubbing tower device and trichlorosilane tail gas recovery system | |
| CN205216242U (en) | Flash distillation heat sink | |
| CN206113402U (en) | Heat pump system | |
| CN205832658U (en) | A kind of waste heat recycling device in xylose production process | |
| CN205288056U (en) | Useless ammonia processing system of propane diamine production line | |
| CN105148550B (en) | Dichloromethane extract separator | |
| CN207214022U (en) | Heat reclaim unit for Chinese medicine extractor | |
| CN206896878U (en) | A kind of device for being dehydrated ternary azeotrope by extracting rectifying | |
| CN103740871B (en) | A kind of recovery system of flushing cinder water and steam and method | |
| CN109529403A (en) | Energy-saving dual-use traditional Chinese medicine extraction, concentrator | |
| CN108662915A (en) | The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect | |
| CN106479668A (en) | Device for extracting star anise oil by negative pressure circulating water | |
| CN204767471U (en) | With high -temperature gas concentrate system all | |
| CN204125401U (en) | The production line of first, ethanol mixed solvent is reclaimed in sodium salt class drug manufacture | |
| CN105536431A (en) | Steam residual heat recycling energy-saving device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190329 |