CN104587703B - Compression hot gas hydronic plant lixiviate infusion system - Google Patents
Compression hot gas hydronic plant lixiviate infusion system Download PDFInfo
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- CN104587703B CN104587703B CN201510019685.9A CN201510019685A CN104587703B CN 104587703 B CN104587703 B CN 104587703B CN 201510019685 A CN201510019685 A CN 201510019685A CN 104587703 B CN104587703 B CN 104587703B
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- pipe
- infusion
- leaching liquor
- infusion tank
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Abstract
Compression hot gas hydronic plant lixiviate infusion system, the steam-heating pipe of the infusion tank of this system has been installed in series two gas compression heat pumps and a buffering air accumulator, raw material residue fumigation steam is installed in the bottom of infusion tank and enters pipe, top is provided with residue fumigation steam and goes out pipe, and residue fumigation steam goes out the fractionation recovery tower bottom that pipe is connected to leaching liquor.During work, high-temperature steam is transported in steam heating tube, rapidly pre-warming is carried out to leaching liquor in tank, steam off afterwards, start gas compression heat pump, steam suction gas compression heat pump in the steam heating tube of buffering air accumulator is carried out mechanical compress heat, be back in steam heating tube after heating, circulating-heating is carried out to the leaching liquor in infusion tank; After infusion terminates, pass into residue fumigation steam from the bottom of infusion tank, separate stifling for the leaching liquor in residue, the steam after separation passes in the fractionation recovery tower of leaching liquor, carries out fractionation recovery to leaching liquor.
Description
Technical field
The invention belongs to effective ingredients in plant extraction equipment technical field, relate to a kind of compression hot gas hydronic plant lixiviate infusion system.
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.When the immersion infusion of raw material, in the heating steam pipe of high-temperature steam input infusion tank, the raw material in infusion tank is heated.This heating infusion mode, considers from the angle of production safety, and the boiler producing high-temperature steam is comparatively far away apart from the required distance of infusion tank, and boiler thermal loss in the process producing high-temperature steam and conveying high-temperature steam is larger.
In addition, this infusion tank, at the end of lixiviate infusion, can infiltrate a large amount of leaching liquor in the residue of raw material, and this part leaching liquor can go out of use together with residue, causes leaching liquor to waste.
Summary of the invention
For in prior art, during effective ingredients in plant lixiviate infusion, heating steam thermal loss in generation and course of conveying is larger, leaching liquor with raw material residue by the problem of discarding in a large number, a kind of compression hot gas hydronic plant lixiviate infusion system is provided, in the infusion tank of this system, steam-heating pipe is housed, steam condensing reflux device is housed above infusion tank, the entrance of the steam circulating pipe of steam condensing reflux device is arranged on the top of infusion tank, steam circulating pipe has been installed in series two condensers, the outlet of steam circulating pipe is arranged on the middle and upper part of infusion tank, the entrance adding pipe and material feedstock of leaching liquor is also housed above infusion tank, in the below of infusion tank, Kitchen sifter is housed, solid discharge is equipped with in side, bottom is equipped with the first extract after infusion and is gone out pipe, the entrance of the steam-heating pipe of infusion tank is provided with entrance threeway, one termination steam of entrance threeway enters pipe, another termination heat of compression gas return valve, the outlet of steam-heating pipe is provided with outlet threeway, one termination steam of outlet threeway goes out pipe, another termination heated air inlet valve, between compression hot gas return valve and heated air inlet valve, be installed in series two gas compression heat pumps and a buffering air accumulator.
Raw material residue fumigation steam is installed in the bottom of infusion tank and enters pipe, residue fumigation steam is installed at the top of infusion tank and pipe, residue fumigation steam goes out the fractionation recovery tower bottom that pipe is connected to leaching liquor, distilled water is installed in the bottom of fractionation recovery tower and pipe, side be from top to bottom equipped with respectively high dense leaching liquor go out pipe, in dense leaching liquor go out pipe and low dense leaching liquor go out pipe, the top of fractionation recovery tower is provided with air discharge duct.
Adopt technique scheme, when infusion tank is started working, high-temperature steam is transported in the steam heating tube of infusion tank, rapidly pre-warming is carried out to the raw material in tank and leaching liquor, after leaching liquor comes to life, stop Steam Heating, open heated air inlet valve and compression hot gas return valve, start gas compression heat pump, by the steam suction gas compression heat pump in the steam heating tube of buffering air accumulator, carry out mechanical compress to steam to heat, high-temperature steam after heating is back in steam heating tube again, leaching liquor in infusion tank is heated, realize the leaching liquor circulating-heating in infusion tank.This compressor that utilizes makes steam keep the working method of continuous high temperature, and the vapor flow pipe that working site is arranged is shorter, and working site clean hygiene, the thermal loss of steam in flow process is less.
After infusion terminates, pass into residue fumigation steam from the bottom of infusion tank, separate stifling for the leaching liquor in residue, the steam after separation passes in the fractionation recovery tower of leaching liquor, carries out fractionation recovery to leaching liquor.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Embodiment: as shown in Figure 1, a kind of compression hot gas hydronic plant lixiviate infusion system, in the infusion tank 5 of this system, steam-heating pipe 6 is housed, steam condensing reflux device is housed above infusion tank 5, the entrance of the steam circulating pipe 8 of steam condensing reflux device is arranged on the top of infusion tank 5, steam circulating pipe 8 has been installed in series two condensers 7, the outlet of steam circulating pipe 8 is arranged on the middle and upper part of infusion tank 5, the entrance 9 adding pipe 11 and material feedstock of leaching liquor is also housed above infusion tank 5, in the below of infusion tank 5, Kitchen sifter 4 is housed, solid discharge 3 is equipped with in side, first extract after infusion is equipped with in bottom goes out pipe 2, the entrance of the steam-heating pipe 6 of infusion tank is provided with entrance threeway 18, one termination steam of entrance threeway 18 enters pipe 19, another termination heat of compression gas return valve 17, the outlet of steam-heating pipe 6 is provided with outlet threeway 14, one termination steam of outlet threeway 14 goes out pipe 16, another termination heated air inlet valve 15, between compression hot gas return valve 17 and heated air inlet valve 15, be installed in series two gas compression heat pumps 12 and a buffering air accumulator 13, raw material residue fumigation steam is installed in the bottom of infusion tank 5 and enters pipe 1, at the top of infusion tank 5, residue fumigation steam is installed and pipe 10, residue fumigation steam goes out fractionation recovery tower 24 bottom that pipe 10 is connected to leaching liquor, in the bottom of fractionation recovery tower 24, distilled water is installed and pipe 20, side be from top to bottom equipped with respectively high dense leaching liquor go out pipe 23, in dense leaching liquor go out pipe 22 and low dense leaching liquor goes out pipe 21, the top of fractionation recovery tower 24 is provided with air discharge duct 25.
Claims (2)
1. compress hot gas hydronic plant lixiviate infusion system, in the infusion tank (5) of this system, steam-heating pipe (6) is housed, in the top of infusion tank (5), steam condensing reflux device is housed, the entrance of the steam circulating pipe (8) of steam condensing reflux device is arranged on the top of infusion tank (5), steam circulating pipe (8) has been installed in series two condensers (7), the outlet of steam circulating pipe (8) is arranged on the middle and upper part of infusion tank (5), the entrance (9) adding pipe (11) and material feedstock of leaching liquor is also housed in the top of infusion tank (5), in the below of infusion tank (5), Kitchen sifter (4) is housed, solid discharge (3) is equipped with in side, bottom is equipped with the first extract after infusion and is gone out pipe (2), it is characterized in that: on the entrance of the steam-heating pipe (6) of infusion tank, entrance threeway (18) is installed, one termination steam of entrance threeway (18) enters pipe (19), another termination heat of compression gas return valve (17), the outlet of steam-heating pipe (6) is provided with outlet threeway (14), one termination steam of outlet threeway (14) goes out pipe (16), another termination heated air inlet valve (15), between compression hot gas return valve (17) and heated air inlet valve (15), be installed in series two gas compression heat pumps (12) and buffering air accumulator (13).
2. compression hot gas as claimed in claim 1 hydronic plant lixiviate infusion system, it is characterized in that: raw material residue fumigation steam is installed in the bottom of infusion tank (5) and enters pipe (1), residue fumigation steam is installed at the top of infusion tank (5) and pipe (10), residue fumigation steam goes out fractionation recovery tower (24) bottom that pipe (10) is connected to leaching liquor, distilled water is installed in the bottom of fractionation recovery tower (24) and pipe (20), side is equipped with high dense leaching liquor from top to bottom respectively and is gone out pipe (23), in dense leaching liquor go out pipe (22) and low dense leaching liquor go out manage (21), the top of fractionation recovery tower (24) is provided with air discharge duct (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510019685.9A CN104587703B (en) | 2015-01-15 | 2015-01-15 | Compression hot gas hydronic plant lixiviate infusion system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510019685.9A CN104587703B (en) | 2015-01-15 | 2015-01-15 | Compression hot gas hydronic plant lixiviate infusion system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104587703A CN104587703A (en) | 2015-05-06 |
| CN104587703B true CN104587703B (en) | 2016-03-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510019685.9A Expired - Fee Related CN104587703B (en) | 2015-01-15 | 2015-01-15 | Compression hot gas hydronic plant lixiviate infusion system |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107683933B (en) * | 2017-09-14 | 2021-04-06 | 广东维思奇食品有限公司 | Candy boiling device |
| CN115299560A (en) * | 2022-07-22 | 2022-11-08 | 上海康识食品科技有限公司 | Fried wide noodles and production process thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101843989A (en) * | 2009-06-05 | 2010-09-29 | 王建设 | Multi-purpose plant component extracting and separating complete device and application thereof |
| CN101979117A (en) * | 2010-10-28 | 2011-02-23 | 华东理工大学 | Volatile component rectifying-extracting coupled extraction device and method |
| CN204411767U (en) * | 2015-01-15 | 2015-06-24 | 云南玉溪万方天然药物有限公司 | Compression hot gas hydronic plant lixiviate infusion system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008020865A1 (en) * | 2006-08-18 | 2008-02-21 | Semo Milling, Llc | Power production using grain fractionation products |
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2015
- 2015-01-15 CN CN201510019685.9A patent/CN104587703B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101843989A (en) * | 2009-06-05 | 2010-09-29 | 王建设 | Multi-purpose plant component extracting and separating complete device and application thereof |
| CN101979117A (en) * | 2010-10-28 | 2011-02-23 | 华东理工大学 | Volatile component rectifying-extracting coupled extraction device and method |
| CN204411767U (en) * | 2015-01-15 | 2015-06-24 | 云南玉溪万方天然药物有限公司 | Compression hot gas hydronic plant lixiviate infusion system |
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| CN104587703A (en) | 2015-05-06 |
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Granted publication date: 20160330 Termination date: 20210115 |