CN102319516A - Low-temperature vacuum thickener - Google Patents
Low-temperature vacuum thickener Download PDFInfo
- Publication number
- CN102319516A CN102319516A CN201110262644A CN201110262644A CN102319516A CN 102319516 A CN102319516 A CN 102319516A CN 201110262644 A CN201110262644 A CN 201110262644A CN 201110262644 A CN201110262644 A CN 201110262644A CN 102319516 A CN102319516 A CN 102319516A
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- heating tank
- evaporator
- pot
- drainer
- charging aperture
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A low-temperature vacuum thickener relates to the technical field of liquid low-temperature concentration. The invention mainly comprises a heating pot, an evaporating pot, and a condensing pot; the heating pot, the evaporating pot, and the condensing pot of the invention respectively have negative-pressure sealing performance and are connected by pipelines; a steam system is connected to a hot steam inlet of the heating pot; a water-charging pump in series connection with a cooling pipe in the condensing pot is opened; a vacuum pump connected to a vacuum-pumping outlet of the condensing pot is opened; and the system can be used normally. The invention has a simple and reasonable structure, and can concentrate various liquid with different concentrations. The invention can meet the concentration requirements of liquid, maintain original fragrance and colors of the raw material, increase the quality of the concentrate, and reduce concentration cost.
Description
Technical field
The present invention relates to the low temperature concentration technique field of liquid.
Background technology
As everyone knows, in existing tradition concentrates, all adopt means concentrated liquids such as liquid heat or natural evaporation, and the fragrance loss of traditional concentrated liquid is more, energy consumption is big.
Summary of the invention
The object of the invention is to design a kind of liquid concentration machine can keep the original fragrance look of liquid gas, and has the cryogenic vacuum thickener of low energy consumption.
The present invention mainly is made up of heating tank, evaporator and drainer;
Set out material mouth and charging aperture respectively in the upper and lower part of heating tank; Lower end at heating tank connects the concentrate baiting valve; Steam heat exchanging tube is set in heating tank, and the two ends of said steam heat exchanging tube are respectively equipped with vapours import and condensate drain outlet, and are provided with deflector; Make steam heat-exchanging efficient best, said vapours import and condensate drain outlet are separately positioned on the sidewall of heating tank;
Be provided with steam outlet at the evaporator top, the evaporator middle part is provided with the charging aperture that is connected with the discharging opening of said heating tank, and the evaporator lower end is provided with the discharging opening that is connected with the charging aperture of heating tank, and the evaporator middle part is provided with the stoste charging aperture;
Be provided with the steam inlet port that links to each other with the steam outlet of evaporator on drainer top; The bottom of drainer is provided with and vacuumizes outlet, and cooling tube is set in drainer, and stretch out at the two ends of said cooling tube autocondensation jar respectively; And be connected in series with cooling tower through intake pump; Establish deflector in the cooling tube, make cooling heat transferring efficient best, the condensed water drain valve is set in the lower end of drainer.
Heating tank of the present invention, evaporator, drainer have negative-pressure sealing property respectively; And be connected by pipeline; Vapours import at heating tank inserts vapour system; Open the intake pump that is connected in series with the interior cooling tube of drainer, open with vacuumizing of drainer and export the vavuum pump that links to each other, native system just can drop into normal the use.
Operation principle of the present invention is: stoste gets into evaporator by the stoste charging aperture of evaporator under suction function; When stoste reached a certain amount of, vapour system began heating, and stoste is remained in the certain temperature range; Because the evaporator lower end is provided with the discharging opening that is connected with the charging aperture of heating tank; Therefore stoste get into heating tank, and stoste comes to life in heating tank under suction function, and form steam.Steam gets into drainer through the steam outlet on the evaporator, and under the cooling tube heat exchange cooling effect of drainer, steam becomes the condensed water drain valve of condensed water autocondensation jar again and discharges.Concentrate circulates between heating tank and evaporator, makes by the liquid that concentrates to thicken, and discharges from the concentrate baiting valve of heating tank.
The present invention is simple and reasonable for structure, can carry out concentrating of variable concentrations to various liquid.Satisfy the requirement of liquid concentration, keep the former savory and look gas of raw material, improve the concentrate quality, and lower concentrated cost.
Description of drawings
Fig. 1 is a kind of structural representation of the present invention.
The specific embodiment
As shown in Figure 1, the present invention mainly is made up of heating tank 1, evaporator 3 and drainer 5.
Set out material mouth and charging aperture in the upper and lower part of heating tank 1 respectively, connect concentrate baiting valve 15 in the lower end of heating tank 1.
Steam heat exchanging tube 20 is set in heating tank 1; Be provided with a plurality of deflectors 21 between the heat exchanger tube; The two ends of steam heat exchanging tube 20 are respectively equipped with vapours import 17 and condensate drain outlet 16, and vapours import 17 and condensate drain outlet 16 are separately positioned on the sidewall of heating tank 1.
Be provided with steam outlet at evaporator 3 tops, evaporator 3 middle parts are provided with charging aperture, between the discharging opening of the charging aperture of evaporator 3 and heating tank 1, connect feed pipe 2.
Evaporator 3 lower ends are provided with discharging opening, between the charging aperture of this discharging opening and heating tank 1, are connected feed liquid pipeline 14.
Evaporator 3 middle parts are provided with the stoste charging aperture, and this stoste charging aperture is connected with stoste dolly 12 through inhaling stoste pipe 13.
Be provided with the steam inlet port on drainer 5 tops, between the steam outlet of this steam inlet port and evaporator 3, connect steam pipe 4.
The bottom of drainer 5 is provided with and vacuumizes outlet, and this vacuumizes outlet and links to each other with vavuum pump 10 through vacuum pipe 9.
In the lower end of drainer 5 condensed water drain valve 11 is set.
Claims (1)
1. the cryogenic vacuum thickener is characterized in that mainly being made up of heating tank, evaporator and drainer;
Set out material mouth and charging aperture respectively in the upper and lower part of heating tank; Lower end at heating tank connects the concentrate baiting valve; Steam heat exchanging tube is set in heating tank; The two ends of said steam heat exchanging tube are respectively equipped with vapours import and condensate drain outlet, and said vapours import and condensate drain outlet are separately positioned on the sidewall of heating tank;
Be provided with steam outlet at the evaporator top, the evaporator middle part is provided with the charging aperture that is connected with the discharging opening of said heating tank, and the evaporator lower end is provided with the discharging opening that is connected with the charging aperture of heating tank, and the evaporator middle part is provided with the stoste charging aperture;
Be provided with the steam inlet port that links to each other with the steam outlet of evaporator on drainer top; The bottom of drainer is provided with and vacuumizes outlet; Cooling tube is set in drainer; Stretch out at the two ends of said cooling tube autocondensation jar respectively, and be connected in series with cooling tower through intake pump, in the lower end of drainer the condensed water drain valve is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110262644A CN102319516A (en) | 2011-09-07 | 2011-09-07 | Low-temperature vacuum thickener |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110262644A CN102319516A (en) | 2011-09-07 | 2011-09-07 | Low-temperature vacuum thickener |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102319516A true CN102319516A (en) | 2012-01-18 |
Family
ID=45447423
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110262644A Pending CN102319516A (en) | 2011-09-07 | 2011-09-07 | Low-temperature vacuum thickener |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102319516A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691137A (en) * | 2013-12-26 | 2014-04-02 | 龙源海洋生物股份有限公司 | Fish pressed liquor concentrator |
| CN105289021A (en) * | 2015-11-23 | 2016-02-03 | 大连华卓生物科技有限公司 | Apparatus and method for concentrating collagen solution used for articular cartilage regeneration |
| CN105918723A (en) * | 2016-04-29 | 2016-09-07 | 新疆康元生物科技股份有限公司 | Concentrated hippophae rhamnoides fruit juice, preparation method of concentrated hippophae rhamnoides fruit juice and juice concentrating device |
| CN105942119A (en) * | 2016-04-29 | 2016-09-21 | 新疆康元生物科技股份有限公司 | Hippophae fruit powder, preparation method of hippophae fruit powder and fruit powder processing device |
| CN110755862A (en) * | 2019-11-25 | 2020-02-07 | 湖南安化芙蓉山茶业有限责任公司 | Vacuum concentration device and energy-saving efficient tea juice concentration system |
-
2011
- 2011-09-07 CN CN201110262644A patent/CN102319516A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691137A (en) * | 2013-12-26 | 2014-04-02 | 龙源海洋生物股份有限公司 | Fish pressed liquor concentrator |
| CN105289021A (en) * | 2015-11-23 | 2016-02-03 | 大连华卓生物科技有限公司 | Apparatus and method for concentrating collagen solution used for articular cartilage regeneration |
| CN105918723A (en) * | 2016-04-29 | 2016-09-07 | 新疆康元生物科技股份有限公司 | Concentrated hippophae rhamnoides fruit juice, preparation method of concentrated hippophae rhamnoides fruit juice and juice concentrating device |
| CN105942119A (en) * | 2016-04-29 | 2016-09-21 | 新疆康元生物科技股份有限公司 | Hippophae fruit powder, preparation method of hippophae fruit powder and fruit powder processing device |
| CN110755862A (en) * | 2019-11-25 | 2020-02-07 | 湖南安化芙蓉山茶业有限责任公司 | Vacuum concentration device and energy-saving efficient tea juice concentration system |
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Legal Events
| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120118 |