CN103007557A - Low-temperature vacuum concentration device for plant extracts - Google Patents
Low-temperature vacuum concentration device for plant extracts Download PDFInfo
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- CN103007557A CN103007557A CN201210569049XA CN201210569049A CN103007557A CN 103007557 A CN103007557 A CN 103007557A CN 201210569049X A CN201210569049X A CN 201210569049XA CN 201210569049 A CN201210569049 A CN 201210569049A CN 103007557 A CN103007557 A CN 103007557A
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- plant extracts
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Abstract
The invention relates to a low-temperature vacuum concentration device for plant extracts. The device is composed of a concentrated tank, a hot water circulating pump, a heating medium heat exchanger, a hot water circulating tank, and a water jet vacuum system. The device provided by the invention is a special device for low-temperature vacuum concentration which employs circulating hot water as a heating medium. The low-temperature vacuum concentration device can effectively prevent the problem of coke breeze generation caused by local high temperature of the heater, has the advantages of low heat loss, high heat utilization rate and remarkable energy-saving effect, can increase product quality, and is suitable for resisting explosion or preventing applications in high temperature operation areas.
Description
Technical field
The invention belongs to a Plant Extracts production equipment, particularly a Plant Extracts cryogenic vacuum enrichment facility.
Background technology
At present, the plant extracts industry is concentrated, be widely used steam-heated interior circulation single-effect vacuum enrichment facility and method, it is because the heating tubulation of single-action inherence is circular layout, advance steam port and only have one, and vapor (steam) temperature is higher, and all more than 0.2Mpa, namely relevant temperature is more than 120 ℃ for industrial steam pressure; The impact of the too large and localized hyperthermia of the temperature difference of heat medium and plant extracts liquid is particularly when liquid when to be concentrated into relative density be 1.28～1.33 thick paste, very easily in the generation breeze.Prior art exists the deficiency that is easy to produce block breeze.
Through Chinese publication retrieval, find 58 of relevant patents of invention, 122 of utility model patents, 8 of design patents the scheme identical with present patent application of not finding.
Summary of the invention
The object of the invention is to: for the deficiencies in the prior art, propose a kind of middle plant extracts cryogenic vacuum enrichment facility.
Plant extracts cryogenic vacuum enrichment facility of the present invention is characterized in that: its device sprays vacuum system by concentration tank, hot water circulating pump, heat medium heat exchanger, cycling hot pond, water and forms; Its hot water circulating pump water inlet is connected with the cycling hot pond, the hot water circulating pump delivery port is connected with heat medium heat exchanger water inlet, heat medium heat exchanger delivery port is connected with the heat exchanger water inlet of concentration tank, and the heat exchanger delivery port of concentration tank is connected with the cycling hot pond and consists of concentrated heat-exchange system; The air inlet that the top steam drain of concentration tank and water spray the water-jet pump of vacuum system is connected and consists of vacuum concentration system; Water sprays vacuum system and is constituted by water-jet pump and water circulating pump, circulating water pool.
The present invention's beneficial effect compared with prior art: the present invention can effectively avoid heater localized hyperthermia to produce a breeze difficult problem for adopting circulating hot water as the concentrated isolated plant of the low temperature of heat medium; Its heat loss is few, heat utilization efficiency is high, energy-saving effect is remarkable; But Effective Raise plant extracts product quality, and be suitable for explosion-proof or avoid the high-temperature operation district to use.
Description of drawings
The invention will be further described below in conjunction with accompanying drawing, but embodiments of the present invention are not limited to this.
Fig. 1---device schematic diagram
Among the figure: steam pipe (1), heat medium heat exchanger (2), concentration tank (3), cycling hot pond (4), hot water circulating pump (5), discharging opening valve (6), water-jet pump (7), circulating water pool (8), water circulating pump (9), feed pipe (10).
The specific embodiment
As shown in Figure 1: plant extracts cryogenic vacuum enrichment facility of the present invention, spray vacuum system by interior circulation concentration tank (3), hot water circulating pump (5), heat medium heat exchanger (2), cycling hot pond (4), water and form; Its hot water circulating pump (5) water inlet is connected with circulating hot water (4) pond, hot water circulating pump (5) delivery port is connected with heat medium heat exchanger (2) water inlet, heat medium heat exchanger (2) delivery port is connected with the heat exchanger water inlet of interior circulation concentration tank (3), and the heat exchanger delivery port of interior circulation concentration tank (3) is connected with cycling hot pond (4) and consists of in the single-action the concentrated heat-exchange system of circulation; The air inlet that the top steam drain of interior circulation concentration tank (3) and water spray the water-jet pump (7) of vacuum system is connected and consists of circulating vacuum concentration systems in the single-action; The steam inlet of the heat medium heat exchanger (2) of circulating vacuum enrichment facility is connected in steam pipe in the single-action.Water sprays vacuum system and is constituted by water-jet pump (7) and water circulating pump (9), circulating water pool (8).
Plant extracts cryogenic vacuum enrichment facility of the present invention, all parts or equipment all can adopt prior art to make or buy acquisition; Assembling between all parts or the equipment all can adopt prior art to install to finish.
Plant extracts cryogenic vacuum enrichment facility of the present invention can effectively avoid heater localized hyperthermia to produce a breeze difficult problem; Its heat loss is few, heat utilization efficiency is high, energy-saving effect is remarkable; But Effective Raise plant extracts product quality, and be suitable for explosion-proof or avoid the high-temperature operation district to use.
Claims (1)
1. a Plant Extracts cryogenic vacuum enrichment facility is characterized in that: its device sprays vacuum system by concentration tank, hot water circulating pump, heat medium heat exchanger, cycling hot pond, water and forms; Its hot water circulating pump water inlet is connected with the cycling hot pond, the hot water circulating pump delivery port is connected with heat medium heat exchanger water inlet, heat medium heat exchanger delivery port is connected with the heat exchanger water inlet of concentration tank, and the heat exchanger delivery port of concentration tank is connected with the cycling hot pond and consists of concentrated heat-exchange system; The air inlet that the top steam drain of concentration tank and water spray the water-jet pump of vacuum system is connected and consists of vacuum concentration system; Water sprays vacuum system and is constituted by water-jet pump and water circulating pump, circulating water pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210569049.XA CN103007557B (en) | 2012-12-25 | 2012-12-25 | Low-temperature vacuum concentration device for plant extract |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210569049.XA CN103007557B (en) | 2012-12-25 | 2012-12-25 | Low-temperature vacuum concentration device for plant extract |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103007557A true CN103007557A (en) | 2013-04-03 |
| CN103007557B CN103007557B (en) | 2015-08-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201210569049.XA Active CN103007557B (en) | 2012-12-25 | 2012-12-25 | Low-temperature vacuum concentration device for plant extract |
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| CN (1) | CN103007557B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112656018A (en) * | 2019-10-16 | 2021-04-16 | 姜志斌 | Safe concentration technical equipment for VLT vacuum low-temperature aqueous medium paste without gelatinization |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87101339A (en) * | 1987-05-21 | 1988-12-07 | 张庆玉 | Vacuum far infrared concentrator |
| CN2237944Y (en) * | 1994-11-02 | 1996-10-23 | 山东泰山酿酒饮料(集团)股份有限公司 | Device for extracting seaweed juice |
| CN101564403A (en) * | 2009-04-17 | 2009-10-28 | 林建英 | Method for extracting and processing medicinal fungus water |
-
2012
- 2012-12-25 CN CN201210569049.XA patent/CN103007557B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87101339A (en) * | 1987-05-21 | 1988-12-07 | 张庆玉 | Vacuum far infrared concentrator |
| CN2237944Y (en) * | 1994-11-02 | 1996-10-23 | 山东泰山酿酒饮料(集团)股份有限公司 | Device for extracting seaweed juice |
| CN101564403A (en) * | 2009-04-17 | 2009-10-28 | 林建英 | Method for extracting and processing medicinal fungus water |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112656018A (en) * | 2019-10-16 | 2021-04-16 | 姜志斌 | Safe concentration technical equipment for VLT vacuum low-temperature aqueous medium paste without gelatinization |
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| CN103007557B (en) | 2015-08-05 |
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Effective date of registration: 20181213 Address after: 110 000 No. 118 Leye Street, Shenbei New District, Shenyang City, Liaoning Province Patentee after: Shenyang Feilong Pharmaceutical Co., Ltd. Address before: 542800 No. 40 Xiyuan Lane, East Road, Babu District, Hezhou City, Guangxi Zhuang Autonomous Region (Research and Development Institute of New Materials) Patentee before: Wei Limei |
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