CN204485364U - The reinforced plant extract tank of heat exchange - Google Patents
The reinforced plant extract tank of heat exchange Download PDFInfo
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- CN204485364U CN204485364U CN201520140115.0U CN201520140115U CN204485364U CN 204485364 U CN204485364 U CN 204485364U CN 201520140115 U CN201520140115 U CN 201520140115U CN 204485364 U CN204485364 U CN 204485364U
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Abstract
The utility model relates to the reinforced plant extract tank of a kind of heat exchange, belongs to refluxing extraction equipment technical field.It comprises the tank body with chuck, described tank body has that material adds entrance, solvent adds pipe and extract discharge pipe: also comprise heat exchanger, described heat exchanger comprises heat exchanger tube, described heat exchanger tube is made up of with the solvent delivery pipe forming outer tube the cooling water carrier pipe forming interior pipe, and described solvent delivery pipe adds pipe with described solvent and is connected; Also comprise the condenser assembly be positioned at above described tank body, the control valve that described condenser assembly comprises condenser, vapor absorption pipe, the condenser pipe being positioned at condenser inside, return duct and is arranged on return duct; Described vapor absorption pipe stretches into described tank interior from the top of described tank body.The utility model has fully utilized used heat, for enterprise reduces energy consumption, and has saved the preheating time of supplement solvent, for enterprise adds economic benefit.
Description
Technical field
The utility model relates to the reinforced plant extract tank of a kind of heat exchange, belongs to refluxing extraction equipment technical field.
Background technology
Extracting, concentrating is pharmacy, food, the very important operation of chemical industry.In general use extractor chuck, hot water is as thermal source, and external recirculated cooling water cools.After medicinal material decocts certain hour in extractor, liquid is transported to resin column and carries out purifying.The solvent supplemented subsequently needs to be warming up to the temperature close in tank before entering extractor, and liquid at least needed to be cooled to 40 DEG C before upper prop purifying, and this just relates to the excess loss of heat energy.
Utility model content
The utility model will solve the problems of the technologies described above, thus provides a kind of heat exchange reinforced plant extract tank, and it has energy-conservation advantage.
The technical scheme that the utility model solves the problem is as follows:
The reinforced plant extract tank of heat exchange, comprise the tank body with chuck, described tank body has that material adds entrance, solvent adds pipe and extract discharge pipe, also comprise heat exchanger, described heat exchanger comprises heat exchanger tube, described heat exchanger tube is made up of with the solvent delivery pipe forming outer tube the cooling water carrier pipe forming interior pipe, and described solvent delivery pipe adds pipe with described solvent and is connected; Also comprise the condenser assembly be positioned at above described tank body, the control valve that described condenser assembly comprises condenser, vapor absorption pipe, the condenser pipe being positioned at condenser inside, return duct and is arranged on return duct; Described vapor absorption pipe stretches into described tank interior from the top of described tank body; Described heat exchanger comprises heat exchanger tube and heat-exchanging water tank, and described condenser comprises condenser pipe and condensation water tank, and described condensation water tank is communicated with by tube connector with heat-exchanging water tank, and described tube connector is provided with valve.
Condensed water in condensation water tank is used for making it liquefaction backflow to the steam cooling that tank internal solvent generates, therefore, condensed water in use for some time its temperature can significantly rise, and condensation effect cannot be produced or faint condensation effect can only be produced, and condensed water can heat up to needing the solvent replenished in tank owing to having relatively high temperature.Heat exchanger tube has inner and outer tubes, and interior pipe is used for the conveying compared with hot liquid, and outer tube is used for the conveying of colder liquid, is realized the transmission of temperature by tube wall.And in this technical scheme, heat exchanger tube is except the liquid of interior pipe 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 mode being followed successively by heat-cold-hot from inside to outside, further increase heat transfer effect, final realization supplements the solvent entering tank interior, does not need or only needs to open a small amount of steam in chuck and just can realize the preheating to solvent.
Preferred as technique scheme, described condenser assembly also comprises intermediary's tank, and described intermediary tank is arranged on described return duct, and between described condenser and described control valve.
Intermediary's tank is used for the solvent temporarily storing condensing reflux, and this solvent can be ethanol also can be water, or other conventional organic solvents are as n-hexane etc.
As by control valve one direct-open, then intermediary's tank does not almost have memory action, and this kind of operating mode comes across in continuous extraction process usually.The utility model supports continuous extraction process and traditional extraction technique simultaneously.
Preferred as technique scheme, described condenser assembly also comprises excretory duct and branch return pipe, and described excretory duct and branch return pipe are arranged in parallel, and described excretory duct is provided with bleed valve.
Preferred as technique scheme, also comprises the journal stirrup and hanger that are arranged at tank body.
Preferred as technique scheme, also comprise extract return duct, described extract return duct stretches 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 utility model has following beneficial effect:
The utility model has fully utilized used heat, for enterprise reduces energy consumption, and has saved the preheating time of supplement solvent, for enterprise adds economic benefit;
Condenser assembly of the present utility model, makes solvent be recycled, and saves the consumption of solvent.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
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 extract discharge pipe, 1-4 extract return duct, 1-5 journal stirrup, 1-6 hanger;
3-1 cooling water carrier 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 branch return pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further detailed.
This detailed description of the invention is only to explanation of the present utility model, is not to restriction of the present utility model.As long as any change of those skilled in the art done by after having read description of the present utility model, in the scope of claims, all will be subject to the protection of Patent Law.
As shown in Figure 1, the reinforced plant extract tank of heat exchange, comprises with the tank body 1 of chuck 2, heat exchanger 3, is positioned at condenser assembly 4 above described tank body 1.
Described tank body 1 has that material adds entrance 1-1, solvent adds pipe 1-2, extract discharge pipe 1-3, extract return duct 1-4, the journal stirrup 1-5 being arranged at described tank body 1 and hanger 1-6.Described extract return duct 1-4 stretches into described tank body 1 from the top of described tank body 1 inner.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 comprises heat exchanger tube, and described heat exchanger tube is made up of with the solvent delivery pipe 3-2 forming outer tube the cooling water carrier pipe 3-1 forming interior pipe, and described solvent delivery pipe 3-2 adds pipe 1-2 with described solvent and is connected.
Described condenser assembly 4 comprises condenser 4-1, vapor absorption pipe 4-2, the condenser pipe being positioned at condenser 4-1 inside, return duct 4-3, intermediary tank 4-4, the control valve 4-5 be arranged on return duct 4-3, excretory duct and branch return pipe 4-7.Described vapor absorption pipe 4-2 stretches into described tank body 1 from the top of described tank body 1 inner; 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 return pipe 4-7 are arranged in parallel, and described excretory duct is provided with bleed valve 4-6.
Described heat exchanger 3 comprises heat exchanger tube and heat-exchanging water tank, and described condenser 4-1 comprises condenser pipe and condensation water tank, and described condensation water tank is communicated with by tube connector with heat-exchanging water tank, and described tube connector is provided with valve.
Claims (6)
1. the reinforced plant extract tank of heat exchange, comprise the tank body (1) with chuck (2), described tank body (1) has that material adds entrance (1-1), solvent adds pipe (1-2) and extract discharge pipe (1-3), it is characterized in that: also comprise heat exchanger (3), described heat exchanger (3) comprises heat exchanger tube, described heat exchanger tube is made up of the solvent delivery pipe (3-2) of the cooling water carrier pipe (3-1) and formation outer tube that form interior pipe, and described solvent delivery pipe (3-2) and described solvent add pipe (1-2) and be connected; Also comprise the condenser assembly (4) being positioned at described tank body (1) top, the control valve (4-5) that described condenser assembly comprises condenser (4-1), vapor absorption pipe (4-2), the condenser pipe being positioned at condenser (4-1) inside, return duct (4-3) and is arranged on return duct (4-3); Described vapor absorption pipe (4-2) stretches into described tank body (1) from the top of described tank body (1) inner; Described heat exchanger (3) comprises heat exchanger tube and heat-exchanging water tank, and described condenser (4-1) comprises condenser pipe and condensation water tank, and described condensation water tank is communicated with by tube connector with heat-exchanging water tank, and described tube connector is provided with valve.
2. the reinforced plant extract tank of heat exchange according to claim 1, it is characterized in that: described condenser assembly (4) also comprises intermediary's tank (4-4), described intermediary tank (4-4) is arranged on described return duct (4-3), and is positioned between described condenser (4-1) and described control valve (4-5).
3. the reinforced plant extract tank of heat exchange according to claim 2, it is characterized in that: described condenser assembly (4) also comprises excretory duct and branch return pipe (4-7), described excretory duct and branch return pipe (4-7) are arranged in parallel, and described excretory duct are provided with bleed valve (4-6).
4. the reinforced plant extract tank of heat exchange according to claim 1, is characterized in that: also comprise the journal stirrup (1-5) and hanger (1-6) that are arranged at tank body (1).
5. the reinforced plant extract tank of heat exchange according to claim 1, is characterized in that: also comprise extract return duct (1-4), and described extract return duct (1-4) stretches into described tank body (1) from the top of described tank body (1) inner.
6. the reinforced plant extract tank of heat exchange according to claim 4, 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 |
|---|---|---|---|
| CN201520140115.0U CN204485364U (en) | 2015-03-12 | 2015-03-12 | The reinforced plant extract tank of heat exchange |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520140115.0U CN204485364U (en) | 2015-03-12 | 2015-03-12 | The reinforced plant extract tank of heat exchange |
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| Publication Number | Publication Date |
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| CN204485364U true CN204485364U (en) | 2015-07-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520140115.0U Active CN204485364U (en) | 2015-03-12 | 2015-03-12 | The reinforced plant extract tank of heat exchange |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645662A (en) * | 2015-03-12 | 2015-05-27 | 浙江天草生物科技股份有限公司 | Heat exchanging reinforced plant extraction tank |
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2015
- 2015-03-12 CN CN201520140115.0U patent/CN204485364U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645662A (en) * | 2015-03-12 | 2015-05-27 | 浙江天草生物科技股份有限公司 | Heat exchanging reinforced plant extraction tank |
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| GR01 | Patent grant |