CN202342937U - Terminal condensing unit for extracting capsochrome - Google Patents
Terminal condensing unit for extracting capsochrome Download PDFInfo
- Publication number
- CN202342937U CN202342937U CN2011204859497U CN201120485949U CN202342937U CN 202342937 U CN202342937 U CN 202342937U CN 2011204859497 U CN2011204859497 U CN 2011204859497U CN 201120485949 U CN201120485949 U CN 201120485949U CN 202342937 U CN202342937 U CN 202342937U
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- tank body
- tank
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- capsochrome
- freezing liquid
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Abstract
The utility model belongs to the technical filed of extracting and processing natural products and relates to a terminal condensing unit for extracting capsochrome. The left and right ends of an enclosed cylindrical tank are in hemispherical structures, the bottom of the left end of the tank is fixedly provided with a freezing liquid inlet which is parallel to the bottom side of the tank, the bottom of the right end of the tank is provided with an outlet which is perpendicular to the bottom side of the tank, the top of the right end of the tank is provided with a mixed gas inlet, and the left end of the top of the tank is provided with a freezing liquid outlet and a mixed gas outlet in sequence. The lower part of the tank is respectively provided with a left support and a right support away from both ends, and the lower side of the tank between the left support and the right support is provided with a first re-dissolution port, a second re-dissolution port and a third re-dissolution port which are arranged at equal space in sequence from left to right. Pipes in the inner cavity of the tank are correspondingly communicated so as to realize the function of condensing liquefied gas in the process of extracting capsochrome. The terminal condensing unit for extracting capsochrome has the advantages of simple structure, easiness for control of processing conditions, high steam utilization at the time of extracting capsochrome, good effect, low cost and high economic value.
Description
Technical field:
The utility model belongs to the natural product extraction processing technique field, relates to the terminal condensing unit that a kind of capsochrome that adopts automation control system from chilli powder, to extract and use in the natural red colouring matter process extracts usefulness.
Background technology:
At present; Fast development along with economic society; People's living standard improves year by year, and is also increasingly high to the requirement of employed additive composition in the life, and colouring agent that in existing medicine, cosmetics and food and drink, adopts or pigment mainly contain two big types; One type is technology and the qualified synthetic dyestuff of safety requirements, and another kind of is the natural colouring matter that from natural plants or animal body, extracts.Natural colouring matter more and more comes into one's own as the use of food, medicine and cosmetic additive agent or colouring agent, particularly in developed country and area, contacts with human body or the colouring agent that uses must be to adopt nontoxic natural colouring matter.In recent years; The technical development that China extracts natural colouring matter is rapid; Units such as natural colouring matter research institute of the University Of Qingdao extraction natural colouring matter that began one's study from 1988; Present established mature technology comprises some technical methods and technologies such as capsochrome extraction, the extraction of grape pigment, potato pigment extraction, the extraction of purple perilla pigment, the extraction of Semen sesami nigrum pigment and the extraction of radish pigment; And the natural colouring matter that these technology and method are extracted has been widely used in various food, medicine and the cosmetics.Existing capsochrome method for distilling adopts the solvent leaching method basically; But the apparatus that is adopted during leaching is varied; These device ubiquity complex structures, shortcoming such as automaticity is not high, and the pigment loss late is higher in the leaching process; So the residual harmful composition in high efficiency separation extraction and the effective elimination capsochrome has become the technology of paying close attention in the industry, also be the key technology that improves the capsochrome quality.Research and inquire into a kind of apparatus that is specifically designed to the high efficiency extraction capsochrome and caused engineers and technicians' and brainstrust attention in the industry.
Summary of the invention:
The purpose of the utility model is to overcome the shortcoming that exists in the prior art; Seek a kind of special-purpose terminal condensing unit of extraction capsochrome that adopts the jar core structure that stainless steel material is processed into of designing and preparing; This device adopts effective Automatic Cycle technology, can improve the utilization ratio of solvent for use in the capsochrome leaching process expeditiously.
To achieve these goals, the agent structure of the utility model comprises tank body, freezing liquid outlet, mixed gas outlet, combi inlet port, freezing liquid import, dissolves mouth for first time, dissolves mouth for second time, dissolves mouth, discharge outlet, left socle and right support the 3rd time; The tank body right ends side of closed tubular structure is a hemispherical dome structure; Tank body left end side bottom fixedly is shaped on the freezing liquid import parallel with the tank body bottom side; Tank body right-hand end bottom side is shaped on and the vertical discharge outlet in sideline, tank body bottom side; Tank body right-hand member top side is shaped on combi inlet port, and left end place, tank body top side 10～20cm distance at interval is shaped on freezing liquid outlet and mixed gas outlet successively; The tank body bottom is shaped on left socle and right support respectively apart from both end sides 30～50cm place, and equidistant from left to right arrangement is shaped on successively and dissolves mouth and the 3rd time molten mouth for first time molten mouthful, second time on the tank body lower side between left socle and the right support; Each pipeline is corresponding in the inner chamber of tank body is communicated with, and realizes extracting the liquefied gas condensation function in the capsochrome process.
The utility model compared with prior art, it is simple in structure, cost of manufacture is low, fabrication process condition is prone to control, steam utilization is high when being used for the extraction of capsochrome, effective, cost is low, economic worth is good.
Description of drawings:
Fig. 1 is the structural principle sketch map of the utility model.
The specific embodiment:
Below through embodiment and combine accompanying drawing to be described further.
Embodiment:
The agent structure of present embodiment comprises tank body 1, freezing liquid outlet 2, mixed gas outlet 3, combi inlet port 4, freezing liquid import 5, dissolve for first time dissolve mouthfuls 6, second time dissolve mouthfuls 8 mouthfuls 7, the 3rd time, discharge outlet 9, left socle 10 and right support 11; The tank body 1 right ends side of closed tubular structure is a hemispherical dome structure; Tank body 1 left end side bottom fixedly is shaped on the freezing liquid import 5 parallel with tank body 1 bottom side; Tank body 1 right-hand end bottom side is shaped on and the vertical discharge outlet 9 in sideline, tank body 1 bottom side; Tank body 1 right-hand member top side is shaped on combi inlet port 4, and left end place, tank body 1 top side 10～20cm distance at interval is shaped on freezing liquid outlet 2 and mixed gas outlet 3 successively; Tank body 1 bottom is shaped on left socle 10 and right support 11 respectively apart from both end sides 30～50cm place, and equidistant from left to right arrangement is shaped on molten mouthful of 6, second times molten mouthful of 7 and the 3rd times molten mouths 8 successively first time on tank body 1 lower side between left socle 10 and the right support 11; Each pipeline is corresponding in the inner chamber of tank body 1 is communicated with, and realizes extracting the liquefied gas condensation function in the capsochrome process.
Present embodiment is used for the extraction of capsochrome, and the streamline complete set of equipments butt joint that both can be used as automatic production capsochrome is used, and also can use separately; It uses the result to prove that the recovery rate of present embodiment can reach more than 90%, and the pigment quality is good.
Claims (1)
1. one kind is extracted the terminal condensing unit that capsochrome is used, and it is characterized in that agent structure comprises tank body, freezing liquid outlet, mixed gas outlet, combi inlet port, freezing liquid import, dissolves mouth for first time, dissolves mouth for second time, dissolves mouth, discharge outlet, left socle and right support the 3rd time; The tank body right ends side of closed tubular structure is a hemispherical dome structure; Tank body left end side bottom fixedly is shaped on the freezing liquid import parallel with the tank body bottom side; Tank body right-hand end bottom side is shaped on and the vertical discharge outlet in sideline, tank body bottom side; Tank body right-hand member top side is shaped on combi inlet port, and left end place, tank body top side 10～20cm distance at interval is shaped on freezing liquid outlet and mixed gas outlet successively; The tank body bottom is shaped on left socle and right support respectively apart from both end sides 30～50cm place, and equidistant from left to right arrangement is shaped on successively and dissolves mouth and the 3rd time molten mouth for first time molten mouthful, second time on the tank body lower side between left socle and the right support.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204859497U CN202342937U (en) | 2011-11-29 | 2011-11-29 | Terminal condensing unit for extracting capsochrome |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204859497U CN202342937U (en) | 2011-11-29 | 2011-11-29 | Terminal condensing unit for extracting capsochrome |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202342937U true CN202342937U (en) | 2012-07-25 |
Family
ID=46531964
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204859497U Expired - Fee Related CN202342937U (en) | 2011-11-29 | 2011-11-29 | Terminal condensing unit for extracting capsochrome |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202342937U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381621A (en) * | 2015-12-14 | 2016-03-09 | 黄少安 | Distillation and condensation storage tank for processing water phase and organic phase |
-
2011
- 2011-11-29 CN CN2011204859497U patent/CN202342937U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381621A (en) * | 2015-12-14 | 2016-03-09 | 黄少安 | Distillation and condensation storage tank for processing water phase and organic phase |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120725 Termination date: 20121129 |