CN209123397U - A kind of ginger zingiberol circulation extracting apparatus - Google Patents
A kind of ginger zingiberol circulation extracting apparatus Download PDFInfo
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- CN209123397U CN209123397U CN201821830083.7U CN201821830083U CN209123397U CN 209123397 U CN209123397 U CN 209123397U CN 201821830083 U CN201821830083 U CN 201821830083U CN 209123397 U CN209123397 U CN 209123397U
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- reaction warehouse
- condenser
- ginger
- circulation
- pipe
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Abstract
The utility model discloses a kind of ginger zingiberol circulation extracting apparatus, including hopper, pulverizer, reaction warehouse, temperature adjustment storehouse, condenser, solvent storage tank and second distillation tank, pulverizer is installed between the feed inlet and hopper of reaction warehouse, temperature adjustment storehouse is surrounded by outside reaction warehouse, centre is equipped with electric mixing device；Condenser is connected to by steam (vapor) outlet at the top of reaction warehouse, the liquid outlet of condenser is connected to the loop head of solvent storage tank by first circulation pipe；First circulation pipe also passes through return pipe and is connected to reaction warehouse；Solvent storage tank bottom is connected to reaction warehouse by second circulation pipe.The utility model solvent can carry out reciprocal extraction-evaporation-condensation-extraction process, avoid solvent loss, and solvent recovery work can also be easily carried out after extracting, separation simultaneously also extracts ginger slag, it is constantly stirred by agitating paddle, and temperature is adjusted the effect and quality that extraction is increased to the temperature of suitable extraction by temperature adjustment storehouse 4.
Description
Technical field
The utility model relates to biological abstraction technique field, in particular to a kind of ginger zingiberol circulation extracting apparatus.
Background technique
Ginger is a kind of industrial crops for having very much value of exploiting and utilizing, is removed containing physiological activators such as zingerone, gingerols
Outside, also contain protein, polysaccharide, vitamin and various trace elements, integrate nutrition, seasoning, health care, from ancient times by physician
It is considered as the health care product of integration of drinking and medicinal herbs, there is dispelling cold, clearing damp, warm stomach, accelerate the plurality of health care functions such as blood circulation.Ginger product exists
International market is becoming increasingly popular, especially in great demand in Southeast Asia, Japan and other countries and area, every year can be a large amount of for country's wound
Foreign exchange.In order to increase the use value of ginger, Some Enterprises carry out the extraction of zingiberol to ginger, and many enterprises are all first using ginger
Then juicing is extracted inside ginger juice again, actually also remain zingiberol inside ginger slag, because zingiberol is not dissolved completely in ginger
In juice, therefore the extraction of zingiberol is not fully, and in order to extract the zingiberol in ginger slag, organic solvent can be used to be extracted
It takes, but recycling and the separation problem of solvent will be generated using organic solvent, because the boiling point of organic solvent is lower, but it is warm
It spends in lower situation and is unfavorable for extracting the progress of work, therefore these problems are also required to be resolved.
Utility model content
The technical problem to be solved by the present invention is to provide it is a kind of extraction it is more complete, solvent facilitates the ginger of recycling
Zingiberol circulation extracting apparatus.
The technical solution of the utility model are as follows:
A kind of ginger zingiberol circulation extracting apparatus, including hopper, pulverizer, reaction warehouse, temperature adjustment storehouse, condenser, solvent are deposited
Storage tank and second distillation tank install pulverizer, are surrounded by temperature adjustment outside reaction warehouse between the feed inlet and hopper of the reaction warehouse
Storehouse, centre are equipped with electric mixing device；The reaction warehouse bottom is equipped with diversion pipe, and the diversion pipe is equipped with the second valve；
Steam (vapor) outlet is set at the top of the reaction warehouse, and the steam (vapor) outlet is connected to condenser, and the liquid outlet of the condenser passes through the
One circulation pipe is connected to the loop head of solvent storage tank, installs third valve before the loop head；The first circulation pipe
Reaction warehouse is also connected to by return pipe, the first valve is installed on the return pipe；The solvent storage tank bottom passes through the
Two circulation pipes are connected to reaction warehouse, install the 5th valve on the second circulation pipe；Installation filling at the top of the solvent storage tank
It manages, the 4th valve is installed on the filler pipe.
Further, diversion pipe is connected to second distillation tank, and heater is installed in the second distillation tank, and bottom is equipped with
Liquid pipe, the outlet tube install the 6th valve, and the second distillation tank top also passes through gas-guide tube and is back to reaction warehouse top.
Further, condenser is water circulation condenser or compressed air condenser.
Further, steam (vapor) outlet is horn-like.
Further, further include control for controlling the heater in the pulverizer, temperature adjustment storehouse and second distillation tank
Case.
The utility model has the beneficial effect that
The utility model solvent can carry out reciprocal extraction-evaporation-condensation-extraction process, avoid solvent loss, and
And solvent recovery work can also be easily carried out after extracting, separation simultaneously also extracts ginger slag, passes through stirring
Paddle constantly stirs and temperature is adjusted the effect that extraction is increased to the temperature of suitable extraction by temperature adjustment storehouse, keeps extraction completeer
Entirely.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model.
In figure: 1- hopper, 2- pulverizer, 3- reaction warehouse, 31- return pipe, the first valve of 31a-, 32- diversion pipe, 32a-
Two valves, 33- steam (vapor) outlet, 4- temperature adjustment storehouse, 5- control cabinet, 6- electric mixing device, 7- condenser, 71- first circulation pipe, 8-
Solvent storage tank, 81- loop head, 81a- third valve, 82- filler pipe, the 4th valve of 82a-, 83- second circulation pipe, 83a-
5th valve, 9- second distillation tank, 91- gas-guide tube, 92- outlet tube, the 6th valve of 92a-.
Specific embodiment
Specific embodiment of the present utility model is described further with reference to the accompanying drawing.It should be noted that
The explanation of these embodiments is used to help to understand the utility model, but does not constitute the restriction to the utility model.This
Outside, technical characteristic involved in the various embodiments of the present invention described below is as long as they do not conflict with each other
It can be combined with each other.
As shown in Figure 1:
A kind of ginger zingiberol circulation extracting apparatus, including it is hopper 1, pulverizer 2, reaction warehouse 3, temperature adjustment storehouse 4, condenser 7, molten
Agent storage tank 8 installs pulverizer 2, is surrounded by temperature adjustment storehouse 4 outside reaction warehouse 3 between the feed inlet and hopper 1 of the reaction warehouse 3,
Centre is equipped with electric mixing device 6；3 bottom of reaction warehouse is equipped with diversion pipe 32, and the diversion pipe 32 is equipped with the second valve
Door 32a；Steam (vapor) outlet 33 is set at the top of the reaction warehouse 3, and the steam (vapor) outlet 33 is connected to condenser 7, the condenser 7
Liquid outlet is connected to the loop head 81 of solvent storage tank 8 by first circulation pipe 71, installs third before the loop head 81
Valve 81a；The first circulation pipe 71 is also connected to reaction warehouse 3 by return pipe 31, is equipped with first on the return pipe 31
Valve 31a；8 bottom of solvent storage tank is connected to reaction warehouse 3 by second circulation pipe 83, pacifies on the second circulation pipe 83
Fill the 5th valve 83a；Filler pipe 82 is installed at the top of the solvent storage tank 8, the 4th valve 82a is installed on the filler pipe 82.
When use, ginger is cleaned and is entered after peeling from hopper 1, is crushed by pulverizer 2, subsequently into reaction warehouse
3, the temperature control medium in temperature adjustment storehouse is water, is changed by the temperature of water to change the reaction temperature in reaction warehouse 3, is adjusted to being suitable for
The temperature of extraction or for separating solvent.The solvent toward the injection extraction of solvent storage tank 8 is opened from filler pipe 82, is closed after injection
The 4th valve 82a is closed, prevents from volatilizing；Then it opens electric mixing device 6 and the 5th valve 83a, solvent enters in reaction warehouse 2,
Zingiberol in ginger slag and ginger juice is extracted, is adjusted temperature in the range for being suitable for extraction by temperature adjustment storehouse 4 in extraction process
It is interior, since the boiling point of solvent is lower, the condensation of solvent by thermal evaporation, after gasification by condenser 7 is easy from condenser 7
Liquid outlet outflow close third valve 81a during extraction, open the first valve 31a, condensed solvent passes through
Second circulation pipe 83 flows back to reaction warehouse, the extraction so to move in circles-evaporation-condensation-extraction process, completion to be extracted
Afterwards, third valve 81a is opened, the first valve 31a is closed, closes the 5th valve 83a, the appropriate water temperature that temperature adjustment storehouse 4 is turned up, solvent
It can volatilize rapidly, then be flow to by the condensation of condenser 7 and complete to recycle in solvent storage tank 8, open the after solvent volatilization completely
Two valve 32a release zingiberol.
The utility model solvent can carry out reciprocal extraction-evaporation-condensation-extraction process, avoid solvent loss, and
And solvent recovery work can also be easily carried out after extracting, separation simultaneously also extracts ginger slag, passes through stirring
Paddle constantly stirs and temperature is adjusted the effect and quality that extraction is increased to the temperature of suitable extraction by temperature adjustment storehouse 4.
Although solvent can be evaporated by way of heating is recycled to solvent storage tank 8 after the completion of extracting zingiberol,
Still can also have the solvent of part in the zingiberol extracted, in order to can abundant recycling design, diversion pipe 32 is connected to secondary
Alembic 9, the second distillation tank 9 is interior to install heater (not shown), and bottom is equipped with outlet tube 92, and the outlet tube 92 is installed
6th valve 92a, 9 top of second distillation tank are also back to 3 top of reaction warehouse by gas-guide tube 91.Zingiberol first flow to secondary
It in alembic 9, is then heated by heater, is returned in reaction warehouse 3 after so that solvent is gasified through gas-guide tube 91, then again by cold
Condenser condensing recovery.
Specifically, condenser 7 is water circulation condenser or compressed air condenser.
Specifically, collecting the steam of solvent for convenience, steam (vapor) outlet 33 is horn-like.
It further include for controlling the pulverizer 2, temperature adjustment storehouse 4, in second distillation tank 9 specifically, controlling for convenience
The control cabinet of heater and condenser 7.
The embodiments of the present invention is explained in detail in conjunction with attached drawing above, but the utility model is not limited to be retouched
The embodiment stated.For a person skilled in the art, right in the case where not departing from the utility model principle and spirit
These embodiments carry out a variety of change, modification, replacement and modification, still fall in the protection scope of the utility model.
Claims (5)
1. a kind of ginger zingiberol circulation extracting apparatus, including hopper (1), pulverizer (2), reaction warehouse (3), temperature adjustment storehouse (4), condensation
Device (7), solvent storage tank (8), it is characterised in that: pulverizer is installed between the feed inlet and hopper (1) of the reaction warehouse (3)
(2), it is surrounded by temperature adjustment storehouse (4) outside reaction warehouse (3), centre is equipped with electric mixing device (6)；Reaction warehouse (3) bottom
Equipped with diversion pipe (32), the diversion pipe (32) is equipped with the second valve (32a)；Setting steam goes out at the top of the reaction warehouse (3)
Mouth (33), the steam (vapor) outlet (33) are connected to condenser (7), and the liquid outlet of the condenser (7) passes through first circulation pipe
(71) it is connected to the loop head (81) of solvent storage tank (8), third valve (81a) is installed before the loop head (81)；Institute
It states first circulation pipe (71) to be also connected to reaction warehouse (3) by return pipe (31), the first valve is installed on the return pipe (31)
Door (31a)；Solvent storage tank (8) bottom is connected to reaction warehouse (3) by second circulation pipe (83), the second circulation pipe
(83) the 5th valve (83a) is installed on；Filler pipe (82) are installed at the top of the solvent storage tank (8), on the filler pipe (82)
4th valve (82a) is installed.
2. ginger zingiberol circulation extracting apparatus according to claim 1, it is characterised in that: the diversion pipe (32) is connected to
Second distillation tank (9), the second distillation tank (9) is interior to install heater, and bottom is equipped with outlet tube (92), the outlet tube (92)
6th valve (92a) is installed, is also back to reaction warehouse (3) top by gas-guide tube (91) at the top of the second distillation tank (9).
3. ginger zingiberol circulation extracting apparatus according to claim 1, it is characterised in that: the condenser (7) is followed for water
Ring condenser or compressed air condenser.
4. ginger zingiberol circulation extracting apparatus according to claim 1, it is characterised in that: the steam (vapor) outlet (33) is loudspeaker
Shape.
5. ginger zingiberol circulation extracting apparatus according to claim 2, it is characterised in that: further include for controlling the powder
Broken machine (2), temperature adjustment storehouse (4), the heater in second distillation tank (9) and condenser (7) control cabinet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821830083.7U CN209123397U (en) | 2018-11-07 | 2018-11-07 | A kind of ginger zingiberol circulation extracting apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821830083.7U CN209123397U (en) | 2018-11-07 | 2018-11-07 | A kind of ginger zingiberol circulation extracting apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209123397U true CN209123397U (en) | 2019-07-19 |
Family
ID=67244199
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821830083.7U Expired - Fee Related CN209123397U (en) | 2018-11-07 | 2018-11-07 | A kind of ginger zingiberol circulation extracting apparatus |
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| Country | Link |
|---|---|
| CN (1) | CN209123397U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112641028A (en) * | 2020-12-20 | 2021-04-13 | 湖南安化芙蓉山茶业有限责任公司 | Temperature-regulating sealwort steaming method and temperature-regulating sealwort steaming device |
| CN113025428A (en) * | 2021-03-08 | 2021-06-25 | 舒城鸿升农林科技有限公司 | Blumea balsamifera processing and extracting equipment |
| CN113616080A (en) * | 2021-08-23 | 2021-11-09 | 谭先朝 | Cold and hot sharing flavor beverage extraction system |
-
2018
- 2018-11-07 CN CN201821830083.7U patent/CN209123397U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112641028A (en) * | 2020-12-20 | 2021-04-13 | 湖南安化芙蓉山茶业有限责任公司 | Temperature-regulating sealwort steaming method and temperature-regulating sealwort steaming device |
| CN113025428A (en) * | 2021-03-08 | 2021-06-25 | 舒城鸿升农林科技有限公司 | Blumea balsamifera processing and extracting equipment |
| CN113616080A (en) * | 2021-08-23 | 2021-11-09 | 谭先朝 | Cold and hot sharing flavor beverage extraction system |
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| 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: 20190719 Termination date: 20191107 |