CN204411743U - The hydronic plant of compression hot gas just extract concentration systems - Google Patents
The hydronic plant of compression hot gas just extract concentration systems Download PDFInfo
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- CN204411743U CN204411743U CN201520026732.8U CN201520026732U CN204411743U CN 204411743 U CN204411743 U CN 204411743U CN 201520026732 U CN201520026732 U CN 201520026732U CN 204411743 U CN204411743 U CN 204411743U
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- extract
- heating chamber
- pipe
- chamber
- stream pipe
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Abstract
The hydronic plant of compression hot gas just extract concentration systems, the chamber of stream pipe heating chamber and two seal isolation in concentrated chamber is divided in the concentration tank of this system, the gas compression heat pump of two series connection has been installed in stream pipe heating chamber side, gas compression heat pump sucks cryogenic gas in stream pipe heating chamber, arrange in inflow pipe heating chamber again after overcompression heats up, first extract in convection tube carries out laser heating, make to keep continuous high temperature in stream pipe heating chamber, carry the not outer row of gas of the heating of waste heat, the waste heat of gas is fully used, greatly save the energy that heating needs, because gas compression heat pump can be arranged on one side of concentration tank, the circulating path of heated air outside concentration tank can shorten greatly, and the thermal loss of hot gas in cyclic process greatly reduces.From the steam that the first extract steam output pipe in concentrated chamber exports, be communicated to the bottom of fractionating column, with the extracting solution contained in fractionating column recovered steam, reclaim leaching liquor to greatest extent.
Description
Technical field
The utility model belongs to effective ingredients in plant extraction equipment technical field, relates to the hydronic plant of a kind of compression hot gas just extract concentration systems.
Background technology
When the extracts active ingredients of plant, first will in infusion tank with leaching liquor plant material is soaked, infusion, being transferred in concentration tank containing the first extract of effective ingredients in plant after infusion concentrates.
In prior art, the chamber of the stream pipe heating chamber on top and two seal isolation in concentrated chamber of bottom is divided in the tank body of the first extract concentration tank of drift tube type plant, the pipe that enters of first extract is arranged on stream pipe heating chamber top, in stream pipe heating chamber side, Preheated steam inlet pipe is installed, Preheated steam goes out pipe and hydrops discharge pipe, the stream pipe of first extract arranged side by side is installed in stream pipe heating chamber, the stream pipe upper end of first extract seals side by side and is connected with the pipe that enters of first extract, the bottom surface of flow tube heating chamber is worn in the lower end of the stream pipe of first extract, top in the concentrated chamber of access, the efferent duct of just extract steam is installed in the side surface upper part in concentrated chamber, bottom is provided with smart cream and goes out pipe.When entering the stream pipe of the first extract in inflow pipe heating chamber through the first extract of infusion, first extract in the high-temperature steam convection tube that stream pipe heating chamber side enters heats, after extract leaves stream pipe originally, vaporize in concentrated chamber, Separation of Solid and Liquid, the steam separated after vaporization exports from the first extract steam output pipe in concentrated chamber, and the smart cream side of separating is stayed bottom concentrated chamber.This employing steam heats, and by the first extract condensing mode of active ingredient Separation of Solid and Liquid, the required distance of steam access is comparatively far away, and the consumption of steam is large, and thermal loss is larger.
Summary of the invention
For in prior art, through the plant just extract of infusion, carry out in drift tube type concentration tank vapours heating concentrated time, there is heating steam in the problem produced and in course of conveying, thermal loss is larger, the utility model provides the hydronic plant of a kind of compression hot gas just extract concentration systems, the chamber of stream pipe heating chamber and two seal isolation in concentrated chamber is divided in the concentration tank of this system, the pipe that enters of first extract is arranged on stream pipe heating chamber top, the stream pipe of first extract arranged side by side is installed in stream pipe heating chamber, what the stream pipe upper end sealing of first extract connected side by side first extract enters pipe, the bottom surface of flow tube heating chamber is worn in lower end, top in the concentrated chamber of access, the efferent duct of just extract steam is installed in the middle and upper part, side in concentrated chamber, bottom is provided with smart cream and goes out pipe, in stream pipe heating chamber side, Preheated steam inlet pipe is installed, Preheated steam goes out pipe and hydrops discharge pipe, stream pipe heating chamber side lower is also provided with air intake duct, air intake duct is provided with gas-liquid separator, air intake duct is also in series with two gas compression heat pumps, the escape pipe of gas compression heat pump is connected on the side surface upper part of stream pipe heating chamber, the efferent duct of first extract steam is connected to the bottom of fractionating column, the bottom of fractionating column is provided with distilled water discharge pipe, top is provided with exhaust emission tube, side is provided with the recovery tube of just extract.
Adopt technique scheme, owing to having installed the gas compression heat pump of two series connection in stream pipe heating chamber side, gas compression heat pump sucks cryogenic gas in stream pipe heating chamber, arrange in inflow pipe heating chamber again after overcompression heats up, first extract in convection tube carries out laser heating, like this, just make to keep continuous high temperature in stream pipe heating chamber, and, recycle for the gas heated in stream pipe heating chamber, not outer row, the waste heat entrained by gas obtains fully effective utilization, has greatly saved the energy that heating needs; Because gas compression heat pump can be arranged on one side of concentration tank, the circulating path of heated air outside concentration tank can shorten greatly, and the thermal loss of hot gas in cyclic process greatly reduces.
From the steam that the first extract steam output pipe in concentrated chamber exports, be communicated to the bottom of fractionating column, with the extracting solution contained in fractionating column recovered steam, reclaim leaching liquor to greatest extent.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Embodiment: as shown in Figure 1, the hydronic plant of a kind of compression hot gas just extract concentration systems, the chamber of stream pipe heating chamber 8 and 2 two seal isolation in concentrated chamber is divided in the concentration tank 9 of this system, the pipe 7 that enters of first extract is arranged on stream pipe heating chamber 8 top, the stream pipe 6 of first extract arranged side by side is installed in stream pipe heating chamber 8, at the beginning of the stream pipe 6 upper end sealing connection arranged side by side of first extract, extract enters pipe 7, the bottom surface of flow tube heating chamber 8 is worn in lower end, top in the concentrated chamber 2 of access, the efferent duct 14 of just extract steam is installed in the middle and upper part, side in concentrated chamber 2, bottom is provided with smart cream and goes out pipe 1, in stream pipe heating chamber 8 side, Preheated steam inlet pipe 4 is installed, Preheated steam goes out pipe 5 and hydrops discharge pipe 3, stream pipe heating chamber 8 side lower is also provided with air intake duct 12, air intake duct 12 is provided with gas-liquid separator 13, air intake duct 12 is also in series with two gas compression heat pumps 11, the escape pipe 10 of gas compression heat pump 11 is connected on the side surface upper part of stream pipe heating chamber 8, the efferent duct 14 of first extract steam is connected to the bottom of fractionating column 17, the bottom of fractionating column 17 is provided with distilled water discharge pipe 15, top is provided with exhaust emission tube 18, side is provided with the recovery tube 16 of just extract.
Claims (1)
1. compress the hydronic plant of hot gas just extract concentration systems, the chamber of stream pipe heating chamber (8) and (2) two seal isolation in concentrated chamber is divided in the concentration tank (9) of this system, the pipe (7) that enters of first extract is arranged on stream pipe heating chamber (8) top, the stream pipe (6) of first extract arranged side by side is installed in stream pipe heating chamber (8), what stream pipe (6) the upper end sealing of first extract connected side by side first extract enters pipe (7), the bottom surface of flow tube heating chamber (8) is worn in lower end, top in the concentrated chamber (2) of access, in stream pipe heating chamber (8) side, Preheated steam inlet pipe (4) is installed, Preheated steam goes out pipe (5) and hydrops discharge pipe (3), the efferent duct (14) of just extract steam is installed in the middle and upper part, side of concentrated chamber (2), bottom is provided with smart cream and goes out pipe (1), it is characterized in that: stream pipe heating chamber (8) side lower is also provided with air intake duct (12), air intake duct (12) is provided with gas-liquid separator (13), air intake duct (12) is also in series with two gas compression heat pumps (11), the escape pipe (10) of gas compression heat pump (11) is connected on the side surface upper part of stream pipe heating chamber (8), the efferent duct (14) of first extract steam is connected to the bottom of fractionating column (17), the bottom of fractionating column (17) is provided with distilled water discharge pipe (15), top is provided with exhaust emission tube (18), side is provided with the recovery tube (16) of just extract.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520026732.8U CN204411743U (en) | 2015-01-15 | 2015-01-15 | The hydronic plant of compression hot gas just extract concentration systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520026732.8U CN204411743U (en) | 2015-01-15 | 2015-01-15 | The hydronic plant of compression hot gas just extract concentration systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204411743U true CN204411743U (en) | 2015-06-24 |
Family
ID=53462154
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520026732.8U Expired - Fee Related CN204411743U (en) | 2015-01-15 | 2015-01-15 | The hydronic plant of compression hot gas just extract concentration systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204411743U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108619745A (en) * | 2017-03-24 | 2018-10-09 | 天津邦特磁性材料有限公司 | A kind of full-automatic concentration systems of neodymium iron boron waste material filtrate |
| CN110478930A (en) * | 2019-08-21 | 2019-11-22 | 王亚威 | A kind of fractionating column |
-
2015
- 2015-01-15 CN CN201520026732.8U patent/CN204411743U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108619745A (en) * | 2017-03-24 | 2018-10-09 | 天津邦特磁性材料有限公司 | A kind of full-automatic concentration systems of neodymium iron boron waste material filtrate |
| CN110478930A (en) * | 2019-08-21 | 2019-11-22 | 王亚威 | A kind of fractionating column |
| CN110478930B (en) * | 2019-08-21 | 2021-05-04 | 乐平市瑞盛制药有限公司 | Fractionating tower |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150624 Termination date: 20210115 |