CN202705336U - Separating and collecting device for volatile oil in natural plants - Google Patents
Separating and collecting device for volatile oil in natural plants Download PDFInfo
- Publication number
- CN202705336U CN202705336U CN2012202000661U CN201220200066U CN202705336U CN 202705336 U CN202705336 U CN 202705336U CN 2012202000661 U CN2012202000661 U CN 2012202000661U CN 201220200066 U CN201220200066 U CN 201220200066U CN 202705336 U CN202705336 U CN 202705336U
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- separating
- tank
- separating tank
- pump
- material pump
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Abstract
The utility model discloses a separating and collecting device for volatile oil in natural plants. The separating and collecting device comprises a first separating tank and a second separating tank which are connected with each other; product inlets, a cooling water inlet and a cooling water outlet are respectively arranged on the first separating tank, and a first material pump is disposed below the first separating tank; a second material pump and a third material pump which are connected with the first separating tank are arranged below the second separating tank, and the other end of the second material pump and the other end of the third material pump are connected with a collecting tank; a heat exchanger is connected to the upper portion of the collecting tank, and the lower portion of the collecting tank is connected with a vacuum pump and is connected with the second separating tank by the vacuum pump; and a cooling water inlet and a cooling water outlet are arranged on the heat exchanger, the lower portion of the heat exchanger is connected with the collecting tank by a fourth material pump, a product outlet is arranged on a pipeline for connecting the heat exchanger with the collecting tank, and a solvent inlet is arranged on a pipeline for connecting the heat exchanger with the fourth material pump. The separating and collecting device has the advantages that the different types of volatile oil generated when processed foods such as fruit juice, tea leaves and coffee are extracted and concentrated can be captured, are separated and purified and then are respectively recovered.
Description
Technical field
The utility model relates to a kind of separation and collection device, in particular, and this practical device that relates to a kind of separation and collect volatile oil in the natural phant.
Background technology
Abundant and growth in the living standard along with people's material life, people not merely have been confined to solve hungry problem for the requirement of food, but more and more pursue its deeper quality, therefore, caused in order to the additives industries that improves Food Quality day by day prosperous.
Industry personage all knows, foodstuff additive are a kind of chemosynthesis product or crude substance for food processing technology.Adding and use foodstuff additive in food is needs of modern food processing, for preventing food spoilage, guarantee food supply and food quality, satisfy people to the requirement of food nutrition and color, the prosperity food products market has all played vital role.Yet synthetic chemical products additive also needs the test of time for food safety, but natural additive for foodstuff has advantageous value.
The utility model content
Problem to be solved in the utility model, it is exactly the present situation according to aforementioned food processing technology, a kind of device that separates and collect volatile oil in the natural phant is provided, capture and reclaim to the natural flavor that will send in fruit juice, tealeaves and the coffee course of processing, and then it is backfilling in the food in the food deep-processing process, improve the quality of food and the technical purpose of color thereby reach with natural additive for foodstuff.
The purpose of this utility model is achieved by the following technical programs:
A kind of device that separates and collect volatile oil in the natural phant, comprise interconnective first, second separating tank, be provided with first, second product import on described the first separating tank, the top of described the first separating tank is provided with the water coolant import and export, and the bottom of described the first separating tank arranges the first product pump; The bottom of described the second separating tank arranges respectively second, third product pump; One end of described second, third product pump connects described the first separating tank, and the other end of described second, third product pump connects holding tank; The top of described holding tank connects interchanger, and the bottom of described holding tank connects vacuum pump and is connected with described the second separating tank by described vacuum pump; Be provided with the water coolant import and export on the described interchanger, the bottom of described interchanger is connected with the bottom of described holding tank by the 4 materials pump, described interchanger connects on the pipeline of described holding tank and is provided with products export, and described interchanger connects on the pipeline of 4 materials pump the solvent import is set.
The beneficial effects of the utility model are:
(1) can catch the processed food such as fruit juice, tealeaves and coffee fragrant volatile oil in extraction, concentration process;
(2) volatile component that captures can be separated and purifies;
(3) volatile component of different components can be reclaimed respectively.
Description of drawings
Accompanying drawing is structural representation of the present utility model.
Embodiment
For the utility model more easily is understood, below in conjunction with drawings and Examples the technical solution of the utility model is described in detail.
With reference to accompanying drawing, the device of volatile oil in separation of the present utility model and the collection natural phant comprises the first separating tank 1 and the second separating tank 2 that connect by pipeline:
Be provided with the first product import 13 and the second product import 14 on described the first separating tank 1, the top of described the first separating tank 1 is provided with cooling water outlet 11 and entrance of cooling water 12, and the bottom of described the first separating tank 1 arranges the first product pump 51;
The bottom of described the second separating tank 2 arranges respectively interconnective the second product pump 52 and 3 material pump 53, one end of described the second product pump 52 and 3 material pump 53 connects described the first separating tank 1 by pipeline, and the other end of described the second product pump 52 and 3 material pump 53 connects holding tank 3 by pipeline;
The top of described holding tank 3 connects interchanger 4 by pipeline, and the bottom of described holding tank 3 connects vacuum pump 54 by pipeline and is connected with described the second separating tank 2 by described vacuum pump 54;
Be provided with entrance of cooling water 42 and cooling water outlet 41 on the described interchanger 4, the bottom of described interchanger 4 is connected by the bottom of 4 materials pump 55 with described holding tank 3, be provided with products export 31 on the pipeline of the described holding tank 3 of described interchanger 4 connections, be provided with solvent import 551 on the pipeline of described interchanger 4 connection 4 materials pumps 55.
Working process of the present utility model may further comprise the steps:
(1) in the course of processing of the extraction of the processed food such as fruit or tealeaves, the different steps such as concentrated, difference according to the volatile component of its different steps is directed to the first separating tank 1 with its emptying steam and by the first product import 13 and the second product import 14;
(2) device that utilizes described the first separating tank 1 inside separates the volatile component of boiling point difference and the differentiated different components of lift velocity, and making it after the cooling of described the first separating tank 1 top, enter the second separating tank 2, the raffinate of described the first separating tank 1 bottom is then discharged by the first product pump 51;
(3) utilizing vacuum in described the second separating tank 2 to arrange further separates liquids and gases, portion gas is recycled in the described holding tank 3 by described vacuum pump 4, the liquid that sinks to described the second separating tank 2 bottoms is then sent back in described the first separating tank 1 by described the second product pump 52 and is carried out Re-isolation, and the liquid behind the Re-isolation is transferred in the described holding tank 3 by described 3 material pump 53 and reclaimed;
(4) in described holding tank 3, add the part solvent by described solvent import 551, utilize the continuous Circulation of described 4 materials pump 55, the volatile component that is recovered to described holding tank 3 is cooled off and repeatedly absorb, when it reaches finite concentration, discharge and packing by products export 31, obtain the finished product.
Above with reference to drawings and Examples, the utility model is schematically described, this description does not have restricted.Those of ordinary skill in the art will be understood that in actual applications, and the set-up mode of each parts all some change may occur in the utility model, and other staff also may make similar Design under its enlightenment.Only it is pointed out that otherwise break away from design aim of the present utility model, all apparent change and similar Design thereof all are included within the protection domain of the present utility model.
Claims (1)
1. a device that separates and collect volatile oil in the natural phant comprises interconnective first, second separating tank, it is characterized in that:
Be provided with first, second product import on described the first separating tank, the top of described the first separating tank is provided with the water coolant import and export, and the bottom of described the first separating tank arranges the first product pump;
The bottom of described the second separating tank arranges respectively second, third product pump, and an end of described second, third product pump connects described the first separating tank, and the other end of described second, third product pump connects holding tank;
The top of described holding tank connects interchanger, and the bottom of described holding tank connects vacuum pump and is connected with described the second separating tank by described vacuum pump;
Be provided with the water coolant import and export on the described interchanger, the bottom of described interchanger is connected with the bottom of described holding tank by the 4 materials pump, described interchanger connects on the pipeline of described holding tank and is provided with products export, and described interchanger connects on the pipeline of 4 materials pump the solvent import is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202000661U CN202705336U (en) | 2012-05-04 | 2012-05-04 | Separating and collecting device for volatile oil in natural plants |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202000661U CN202705336U (en) | 2012-05-04 | 2012-05-04 | Separating and collecting device for volatile oil in natural plants |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202705336U true CN202705336U (en) | 2013-01-30 |
Family
ID=47585657
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012202000661U Expired - Lifetime CN202705336U (en) | 2012-05-04 | 2012-05-04 | Separating and collecting device for volatile oil in natural plants |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202705336U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109090700A (en) * | 2018-09-20 | 2018-12-28 | 云南中烟工业有限责任公司 | A kind of high efficiency preparation method and purposes of coffee absolute oil |
-
2012
- 2012-05-04 CN CN2012202000661U patent/CN202705336U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109090700A (en) * | 2018-09-20 | 2018-12-28 | 云南中烟工业有限责任公司 | A kind of high efficiency preparation method and purposes of coffee absolute oil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130130 |