CN104645662B - Heat exchange reinforced plant extract tank - Google Patents
Heat exchange reinforced plant extract tank Download PDFInfo
- Publication number
- CN104645662B CN104645662B CN201510108081.1A CN201510108081A CN104645662B CN 104645662 B CN104645662 B CN 104645662B CN 201510108081 A CN201510108081 A CN 201510108081A CN 104645662 B CN104645662 B CN 104645662B
- Authority
- CN
- China
- Prior art keywords
- tank body
- pipe
- tube
- tank
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The present invention relates to a kind of heat exchange reinforced plant extract tank, belong to reflux, extract, equipment technical field.It includes the tank body with chuck, described tank body has material and adds entrance, solvent addition pipe and extracting solution discharge pipe, also include heat exchanger, described heat exchanger includes heat exchanger tube, described heat exchanger tube is by constituting the cooling water conveying pipe of inner tube and constituting the solvent delivery pipe of outer tube and form, and described solvent delivery pipe and described solvent add pipe and connect；Also including being positioned at the condenser assembly above described tank body, described condenser assembly includes condenser, vapor absorption pipe, is positioned at the condensing tube within condenser, return duct and the control valve being arranged on return duct；Described vapor absorption pipe stretches into described tank interior from the top of described tank body.The invention comprehensively utilizes used heat, reduce energy consumption for enterprise, and saved the preheating time augmenting solvent, add economic benefit for enterprise.
Description
Technical field
The present invention relates to a kind of heat exchange reinforced plant extract tank, belong to reflux, extract, equipment technical field.
Background technology
Extracting, concentrating is pharmacy, food, the very important operation of chemical industry.In generally using extraction pot chuck, hot water is as thermal source, and external recirculated cooling water cools down.After medical material decocts certain time in extraction pot, medicinal liquid is transported to resin column and is purified.The solvent supplemented subsequently needs to be warming up to the temperature close in tank before entering extraction pot, and medicinal liquid at least required cool to 40 DEG C before upper column purification, and this relates to the excess loss of heat energy.
Summary of the invention
The invention solves the problems that above-mentioned technical problem, thus provide a kind of heat exchange reinforced plant extract tank, it has energy-conservation advantage.
The technical scheme that the present invention solves the problems referred to above is as follows:
Heat exchange reinforced plant extract tank, including the tank body with chuck, described tank body has material and adds entrance, solvent addition pipe and extracting solution discharge pipe, also include heat exchanger, described heat exchanger includes heat exchanger tube, described heat exchanger tube is by constituting the cooling water conveying pipe of inner tube and constituting the solvent delivery pipe of outer tube and form, and described solvent delivery pipe and described solvent add pipe and connect；Also including being positioned at the condenser assembly above described tank body, described condenser assembly includes condenser, vapor absorption pipe, is positioned at the condensing tube within condenser, return duct and the control valve being arranged on return duct；Described vapor absorption pipe stretches into described tank interior from the top of described tank body；Described heat exchanger includes that heat exchanger tube and heat-exchanging water tank, described condenser include that condensing tube and condensation water tank, described condensation water tank are connected by connecting tube with heat-exchanging water tank, and described connecting tube is provided with valve.
Condensed water in condensation water tank is allowed to liquefaction backflow for the steam cooling generating tank internal solvent, therefore, condensed water its temperature in use for some time can significantly rise, and condensation effect cannot be produced or faint condensation effect can only be produced, and the solvent requiring supplementation with in tank can be heated up owing to having of a relatively high temperature by condensed water.Heat exchanger tube has inner and outer tubes, and inner tube for the conveying of colder liquid, realizes the transmission of temperature for the conveying of relatively hot liquid, outer tube by tube wall.And in this technical scheme, heat exchanger tube is in addition to the liquid of inner tube outer tube conveying different temperatures, heat exchange bobbin carriage is for storing the liquid of comparative high temperature, and this liquid comes from condensation water tank, thus further increasing the utilization rate of heat energy, and achieve the temperature transfer pattern being followed successively by hot-cold-heat from inside to outside, further increase heat transfer effect, final realization supplements the solvent entering tank interior, it is not necessary to or in only needing to open chuck, a small amount of steam can be achieved with the preheating to solvent.
Preferred as technique scheme, described condenser assembly also includes that intermediary's tank, described intermediary tank are arranged on described return duct, and between described condenser and described control valve.
Intermediary's tank for temporarily storing the solvent of condensing reflux, this solvent can be ethanol can also be water, or other conventional organic solvent such as normal hexane etc..
As control valve is always on, then intermediary's tank is almost without memory action, and this kind of operating mode typically appears in continuous extraction process.The present invention supports continuous extraction process and traditional extraction technique simultaneously.
Preferred as technique scheme, described condenser assembly also includes excretory duct and branches back to flow tube, described excretory duct and branch back to flow tube and be arranged in parallel, and is provided with bleed valve on described excretory duct.
Preferred as technique scheme, also includes journal stirrup and the hanger being arranged at tank body.
Preferred as technique scheme, also includes that extracting solution return duct, described extracting solution return duct stretch into described tank interior from the top of described tank body.
Preferred as technique scheme, described journal stirrup is arranged at the sidewall of tank body, makes described tank body be set up in floor by described journal stirrup, makes the bottom of described tank body be suspended under floor simultaneously.
In sum, the method have the advantages that
The invention comprehensively utilizes used heat, reduce energy consumption for enterprise, and saved the preheating time augmenting solvent, add economic benefit for enterprise；
The condenser assembly of the present invention so that solvent is recycled, saves the consumption of solvent.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention；
In figure, 1 tank body, 2 chucks, 3 heat exchangers, 4 condenser assemblies, 9 floors；
1-1 material adds entrance, and 1-2 solvent adds pipe, 1-3 extracting solution discharge pipe, 1-4 extracting solution return duct, 1-5 journal stirrup, 1-6 hanger；
3-1 cooling water conveying pipe, 3-2 solvent delivery pipe；
4-1 condenser, 4-2 vapor absorption pipe, 4-3 return duct, 4-4 intermediary tank, 4-5 control valve, 4-6 bleed valve, 4-7 branches back to flow tube.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is further detailed.
This detailed description of the invention is only explanation of the invention, is not limitation of the present invention.As long as any change that those skilled in the art are done by after the description having read the present invention is in the range of claims, all will be protected by Patent Law.
As it is shown in figure 1, heat exchange reinforced plant extract tank, including with chuck 2 tank body 1, heat exchanger 3, be positioned at the condenser assembly 4 above described tank body 1.
Described tank body 1 has that material adds entrance 1-1, solvent adds pipe 1-2, extracting solution discharge pipe 1-3, extracting solution return duct 1-4, be arranged at the journal stirrup 1-5 and hanger 1-6 of described tank body 1.It is internal that described extracting solution return duct 1-4 stretches into described tank body 1 from the top of described tank body 1.Described journal stirrup 1-5 is arranged at the sidewall of tank body 1, makes described tank body 1 be set up in floor 9 by described journal stirrup 1-5, makes the bottom of described tank body 1 be suspended under floor 9 simultaneously.
Described heat exchanger 3 includes heat exchanger tube, and described heat exchanger tube is made up of cooling water conveying pipe 3-1 and the solvent delivery pipe 3-2 constituting outer tube constituting inner tube, and described solvent delivery pipe 3-2 and described solvent add pipe 1-2 and connect.
Described condenser assembly 4 includes condenser 4-1, vapor absorption pipe 4-2, is positioned at the condensing tube within condenser 4-1, return duct 4-3, intermediary tank 4-4, control valve 4-5, the excretory duct that are arranged on return duct 4-3 and branches back to flow tube 4-7.It is internal that described vapor absorption pipe 4-2 stretches into described tank body 1 from the top of described tank body 1；Described intermediary tank 4-4 is arranged on described return duct 4-3, and between described condenser 4-1 and described control valve 4-5；Described excretory duct and branch back to flow tube 4-7 and be arranged in parallel, and on described excretory duct, it is provided with bleed valve 4-6.
Described heat exchanger 3 includes that heat exchanger tube and heat-exchanging water tank, described condenser 4-1 include that condensing tube and condensation water tank, described condensation water tank are connected by connecting tube with heat-exchanging water tank, and described connecting tube is provided with valve.
Claims (3)
1. heat exchange reinforced plant extract tank, including the tank body (1) with chuck (2), described tank body (1) has material and adds entrance (1-1), solvent addition pipe (1-2) and extracting solution discharge pipe (1-3), it is characterized in that: also include heat exchanger (3), described heat exchanger (3) includes heat exchanger tube, the solvent delivery pipe (3-2) that described heat exchanger tube is carried pipe (3-1) and composition outer tube by the cooling water constituting inner tube forms, and described solvent delivery pipe (3-2) and described solvent add pipe (1-2) and connect；Also including the condenser assembly (4) being positioned at described tank body (1) top, described condenser assembly includes condenser (4-1), vapor absorption pipe (4-2), is positioned at the internal condensing tube of condenser (4-1), return duct (4-3) and the control valve (4-5) being arranged on return duct (4-3)；It is internal that described vapor absorption pipe (4-2) stretches into described tank body (1) from the top of described tank body (1)；Described heat exchanger (3) includes that heat exchanger tube and heat-exchanging water tank, described condenser (4-1) include that condensing tube and condensation water tank, described condensation water tank are connected by connecting tube with heat-exchanging water tank, and described connecting tube is provided with valve；
Described condenser assembly (4) also includes that intermediary's tank (4-4), described intermediary tank (4-4) are arranged on described return duct (4-3), and is positioned between described condenser (4-1) and described control valve (4-5)；
Described condenser assembly (4) also includes excretory duct and branches back to flow tube (4-7), described excretory duct and branch back to flow tube (4-7) and be arranged in parallel, and is provided with bleed valve (4-6) on described excretory duct；
Also including extracting solution return duct (1-4), it is internal that described extracting solution return duct (1-4) stretches into described tank body (1) from the top of described tank body (1).
Heat exchange the most according to claim 1 reinforced plant extract tank, it is characterised in that: also include journal stirrup (1-5) and the hanger (1-6) being arranged at tank body (1).
Heat exchange the most according to claim 2 reinforced plant extract tank, it is characterized in that: described journal stirrup (1-5) is arranged at the sidewall of tank body (1), make described tank body (1) be set up in floor (9) by described journal stirrup (1-5), make the bottom of described tank body (1) be suspended under floor (9) simultaneously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510108081.1A CN104645662B (en) | 2015-03-12 | 2015-03-12 | Heat exchange reinforced plant extract tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510108081.1A CN104645662B (en) | 2015-03-12 | 2015-03-12 | Heat exchange reinforced plant extract tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104645662A CN104645662A (en) | 2015-05-27 |
| CN104645662B true CN104645662B (en) | 2016-08-17 |
Family
ID=53237608
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510108081.1A Active CN104645662B (en) | 2015-03-12 | 2015-03-12 | Heat exchange reinforced plant extract tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104645662B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112973182A (en) * | 2021-03-27 | 2021-06-18 | 合肥九茗信息科技有限公司 | Extraction process of Chinese medicinal materials |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100350996C (en) * | 2002-06-03 | 2007-11-28 | 财团法人电力中央研究所 | Method for removing water contained in solid using liquid material |
| CN202526937U (en) * | 2012-04-12 | 2012-11-14 | 成都科尔医药技术有限公司 | Dynamic extracting and concentrating integrated device for traditional Chinese medicines |
| CN203220775U (en) * | 2013-04-09 | 2013-10-02 | 西安天行健实业有限公司 | Device for extracting effective components of Chinese herbal medicines |
| CN203816269U (en) * | 2014-03-31 | 2014-09-10 | 四川川大华西药业股份有限公司 | Device for extracting traditional Chinese medicine hippophae rhamnoides extract namely total flavones of hippophae rhamnoides |
| CN203763899U (en) * | 2014-04-22 | 2014-08-13 | 广东世信药业有限公司 | Chinese medicinal herb thermal circulating extracting and concentrating system |
| CN204485364U (en) * | 2015-03-12 | 2015-07-22 | 浙江天草生物科技股份有限公司 | The reinforced plant extract tank of heat exchange |
-
2015
- 2015-03-12 CN CN201510108081.1A patent/CN104645662B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN104645662A (en) | 2015-05-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203568873U (en) | Evaporative concentration device used for treating saline organic wastewater | |
| CN105536277B (en) | A kind of evaporating and concentrating process and device of the cellulose solvent NMMO aqueous solution | |
| RU2011139513A (en) | METHOD AND DEVICE FOR THERMAL HYDROLYSIS OF ORGANIC MATERIAL | |
| CN105964962A (en) | Technological method for continuous casting circulating cooling water and casting billet waste heat utilization and system | |
| CN104383704B (en) | A kind of step heating system to the preheating of gas fractionator inlet feed | |
| CN104645662B (en) | Heat exchange reinforced plant extract tank | |
| CN205216221U (en) | Water vapor recompression vaporization system | |
| CN105271324B (en) | A kind of low pressure exhaust steam recycling system | |
| CN204485364U (en) | The reinforced plant extract tank of heat exchange | |
| CN204485363U (en) | Heat exchange type plant extract tank | |
| CN202066096U (en) | Supercritical direct air-cooling heat-supply network drainage system of heat supply unit | |
| CN201356988Y (en) | Energy-saving type alcohol recovery tower | |
| CN104083887B (en) | Utilize the heating system of fractionator overhead waste heat preheating materials at bottom of tower charging | |
| CN206449629U (en) | A kind of heat recovery system of utilization demineralized water and condensate | |
| CN108654129A (en) | A kind of the eucalyptus oil rectifier unit and processing method of Fractional Collections rectifying liquid | |
| CN207455171U (en) | A kind of air compressor machine atmospheric heat recycling is for liquid chlorine circulating vaporization system | |
| CN104892358A (en) | Ethanol recovery tower heat exchange technology | |
| CN204824178U (en) | Monoammonium phosphate solution evaporation crystallization equipment | |
| CN204522338U (en) | Distillation recovery device | |
| CN104477955B (en) | Live steam condensed water cooling in a kind of alumina producing and heat recovery method | |
| CN203833651U (en) | Distilled water preparation equipment | |
| CN207130215U (en) | A kind of system for producing middle matter washing oil | |
| CN207230696U (en) | A kind of steam-water mixing central heating system | |
| CN206793079U (en) | A kind of device of butanol weight-removing column top gaseous phase waste heat recovery | |
| CN205730418U (en) | A kind of economic benefits and social benefits external-circulation concentrating device of efficient recovery organic solvent |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |