CN203598528U - Steam cyclic heating type longan pulp nutrient solution extracting tank - Google Patents
Steam cyclic heating type longan pulp nutrient solution extracting tank Download PDFInfo
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- CN203598528U CN203598528U CN201320688371.4U CN201320688371U CN203598528U CN 203598528 U CN203598528 U CN 203598528U CN 201320688371 U CN201320688371 U CN 201320688371U CN 203598528 U CN203598528 U CN 203598528U
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- tank body
- nutrient solution
- hot air
- longan pulp
- heat exchanger
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Abstract
The utility model discloses a steam cyclic heating type longan pulp nutrient solution extracting tank. The extracting tank mainly comprises a tank body, a top cover, a hot air guide pipe, a heat exchanger, a fan and a one-way valve, wherein the top cover is arranged on an opening of the tank body; the upper end of the hot air guide pipe is communicated with the top of the tank body through the top cover, and the lower end of the hot air guide pipe is communicated with the bottom of the tank body; the heat exchanger and the fan are arranged on the hot air guide pipe; the heat exchanger is used for providing heat for materials in the tank body; the one-way valve is arranged on the hot air guide pipe and is close to the bottom of the tank body. A purified water leading-in pipe is connected to the side wall of the tank body, and a control valve is arranged on the purified water leading-in pipe. An additive leading-in pipe is connected to the side wall of the tank body, and a control valve is arranged on the additive leading-in pipe. By adopting the structure, liquid in the tank is heated in a steam cyclic heating manner, and meanwhile, the extraction of the longan pulp nutrient solution can be accelerated under blowing of air stream.
Description
Technical field
The utility model relates to a kind of extractor, specifically a kind of dried longan pulp nutrient solution extractor.
Background technology
The operation principle of extractor is simple decoction process, medicinal herb soak is in water, adopt Steam Heating, through certain hour, effective ingredient is extracted, the length of decocting time, decide in its sole discretion according to the performance of different material, the difficulty or ease that inventory is extracted because of Chinese herbal medicine shape and effective ingredient differ, can not make unified regulation, suggestion inventory is no more than 2/3rds of volume of equipment and is advisable, in the time extracting aromatic oil, indirect steam is by condensation, after cooling, profit enters oil water separator, light oil is discharged on separator top, heavy oil is discharged in bottom, water is decocted and is finished to carry out vacuum fluid by overflow discharge or backflow (idiographic flow is shown in nozzle orientation and uses scheme of installation), so not only can shorten the fluid time and main effective raffinate in slag being taken out to the greatest extent, avoid waste.Dregs of a decoction arch knots (being commonly called as " bridging ") are slagged tap while having any problem, drive lifting cylinder, make lifting arm reciprocating up and down, assist broken arch to slag tap, till the dregs of a decoction go out to the greatest extent substantially.
There is the difference of essence in the extraction of the extraction of this patent and mode of heating and traditional extractor and mode of heating.
Summary of the invention
The purpose of this utility model is to provide the vapor recycle heated type dried longan pulp nutrient solution extractor that a kind of extraction effect is good.
For achieving the above object, the technical scheme that the utility model adopts is:
Vapor recycle heated type dried longan pulp nutrient solution extractor, it is mainly made up of tank body, top cover, hot air duct, heat exchanger, blower fan, check valve, described top cover is located on the tank mouth of tank body, the upper end of described hot air duct is communicated with the top of tank body by top cover, lower end is communicated with the bottom of tank body, described heat exchanger and blower fan are located on hot air duct, and described heat exchanger provides heat for the material in tank body, and described check valve is located on hot air duct and near the position of tank base.
On the sidewall of described tank body, be connected with pure water ingress pipe, described pure water ingress pipe is provided with control valve.
On the sidewall of described tank body, be connected with additive ingress pipe, described additive ingress pipe is provided with control valve.
On the bottom of described tank body, be connected with nutrient solution delivery line.
Described tank body is to be made up of stainless steel material.
The upper port of described hot air duct adopts the version of enlarging.
The beneficial effects of the utility model: owing to adopting above-mentioned version, utilize the mode of vapor recycle heating to heat to pot liquid, meanwhile, under the blowing of air-flow, can accelerate the extraction of dried longan pulp nutrient solution.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
Fig. 1 is structural representation of the present utility model.
In figure: 1, tank body; 2, top cover; 3, hot air duct; 4, heat exchanger; 5, blower fan; 6, check valve; 7, pure water ingress pipe; 8, control valve; 9, additive ingress pipe; 10, control valve; 11, nutrient solution delivery line.
The specific embodiment
As shown in Figure 1, vapor recycle heated type dried longan pulp nutrient solution extractor, it is mainly made up of tank body 1, top cover 2, hot air duct 3, heat exchanger 4, blower fan 5, check valve 6, described top cover 2 is located on the tank mouth of tank body 1, the upper end of described hot air duct 3 is communicated with the top of tank body 1 by top cover 2, lower end is communicated with the bottom of tank body 1, described heat exchanger 4 and blower fan 5 are located on hot air duct 3, described heat exchanger 4 provides heat for the material in tank body 1, and described check valve 6 is located on hot air duct 3 and near the position of tank body 1 bottom.
Described tank body 1 is to be made up of stainless steel material.On the sidewall of tank body 1, be connected with pure water ingress pipe 7, described pure water ingress pipe 7 is provided with control valve 8.On the sidewall of tank body 1, be also connected with additive ingress pipe 9, described additive ingress pipe 9 is provided with control valve 10.On the bottom of tank body 1, be connected with nutrient solution delivery line 11.
The upper port of described hot air duct 3 adopts the version of enlarging, is conducive to like this discharge of steam.
The above is preferred embodiment of the present utility model; certainly can not limit with this interest field of the utility model; should be understood that; for those skilled in the art; the technical solution of the utility model is modified or is equal to replacement, do not depart from the protection domain of technical solutions of the utility model.
Claims (6)
1. a vapor recycle heated type dried longan pulp nutrient solution extractor, it is characterized in that: it is mainly made up of tank body, top cover, hot air duct, heat exchanger, blower fan, check valve, described top cover is located on the tank mouth of tank body, the upper end of described hot air duct is communicated with the top of tank body by top cover, lower end is communicated with the bottom of tank body, described heat exchanger and blower fan are located on hot air duct, described heat exchanger provides heat for the material in tank body, and described check valve is located on hot air duct and near the position of tank base.
2. vapor recycle heated type dried longan pulp nutrient solution extractor according to claim 1, is characterized in that: on the sidewall of described tank body, be connected with pure water ingress pipe, described pure water ingress pipe is provided with control valve.
3. vapor recycle heated type dried longan pulp nutrient solution extractor according to claim 1, is characterized in that: on the sidewall of described tank body, be connected with additive ingress pipe, described additive ingress pipe is provided with control valve.
4. vapor recycle heated type dried longan pulp nutrient solution extractor according to claim 1, is characterized in that: on the bottom of described tank body, be connected with nutrient solution delivery line.
5. vapor recycle heated type dried longan pulp nutrient solution extractor according to claim 1, is characterized in that: described tank body is to be made up of stainless steel material.
6. vapor recycle heated type dried longan pulp nutrient solution extractor according to claim 1, is characterized in that: the upper port of described hot air duct adopts the version of enlarging.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320688371.4U CN203598528U (en) | 2013-11-04 | 2013-11-04 | Steam cyclic heating type longan pulp nutrient solution extracting tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320688371.4U CN203598528U (en) | 2013-11-04 | 2013-11-04 | Steam cyclic heating type longan pulp nutrient solution extracting tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203598528U true CN203598528U (en) | 2014-05-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320688371.4U Expired - Fee Related CN203598528U (en) | 2013-11-04 | 2013-11-04 | Steam cyclic heating type longan pulp nutrient solution extracting tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203598528U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103550950A (en) * | 2013-11-04 | 2014-02-05 | 广东果美乐食品有限公司 | Circulating steam heating type longan pulp nutrient solution extracting tank |
| CN105104917A (en) * | 2015-09-14 | 2015-12-02 | 天津市可居食品有限公司 | Steam heating type material soaking device capable of preventing material bags from sinking |
-
2013
- 2013-11-04 CN CN201320688371.4U patent/CN203598528U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103550950A (en) * | 2013-11-04 | 2014-02-05 | 广东果美乐食品有限公司 | Circulating steam heating type longan pulp nutrient solution extracting tank |
| CN103550950B (en) * | 2013-11-04 | 2016-03-30 | 广东果美乐食品有限公司 | Vapor recycle heated type dried longan pulp nutrient solution extractor |
| CN105104917A (en) * | 2015-09-14 | 2015-12-02 | 天津市可居食品有限公司 | Steam heating type material soaking device capable of preventing material bags from sinking |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140521 Termination date: 20141104 |
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| EXPY | Termination of patent right or utility model |