CN207384879U - A kind of alcohol recovery system - Google Patents
A kind of alcohol recovery system Download PDFInfo
- Publication number
- CN207384879U CN207384879U CN201820077486.2U CN201820077486U CN207384879U CN 207384879 U CN207384879 U CN 207384879U CN 201820077486 U CN201820077486 U CN 201820077486U CN 207384879 U CN207384879 U CN 207384879U
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- tank
- pipeline
- extraction
- surge tank
- entrance
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Abstract
The utility model discloses a kind of alcohol recovery systems, it is desirable to provide a kind of alcohol recovery system being used conveniently and safely.It is provided with the extraction of main vacuum manifold and safety valve, concentration tank including upper end, the cooler that entrance is connected with main vacuum manifold, the surge tank that entrance is connected by pipeline with cooler outlet, the collecting tank that entrance is connected by the vacuum cooled surge tank and upper end of pipeline and surge tank outlet connection by pipeline with vacuum cooled surge tank leakage fluid dram；The collecting tank is connected by infusion pump and pipeline with extraction, concentration tank upper end；The safety valve is connected by pipeline with the entrance of vacuum cooled surge tank；The extraction, the outer wall of concentration tank are provided with steam heating jacket, and the extraction, the top of concentration tank are provided with feeding port and close the cover of feeding port；The extraction, the lower end of concentration tank are provided with discharge valve.The utility model is suitable for all kinds of extractions, the alcohol recycle of concentration tank uses.
Description
Technical field
The utility model is related to pharmacy extraction, concentrator technical field, more particularly, to a kind of alcohol recovery system.
Background technology
Solvent of the workshop for production is mainly volatile ethyl alcohol, due to technique particularity, in process of production, big portion
Part alcohol vapor is uncolled using negative pressure production and negative pressure transportation liquid material, during production point post is directly taken out by vacuum
Enter in vacuum pump and recirculated water, cause a large amount of ethyl alcohol losses and there are larger security risks.
Utility model content
The purpose of this utility model is intended to overcome the shortcomings of the prior art, provides a kind of safe and can be effective
Reduce the alcohol recovery system of production cost.
In order to solve the above-mentioned technical problem, the utility model is achieved through the following technical solutions：
A kind of alcohol recovery system, is provided with extraction, the concentration tank of main vacuum manifold and safety valve including upper end, entrance with
The cooler of main vacuum manifold connection, the surge tank that entrance is connected by pipeline with cooler outlet, entrance is by pipeline with delaying
Rush the collection that tank exports the vacuum cooled surge tank of connection and upper end is connected by pipeline with vacuum cooled surge tank leakage fluid dram
Tank；The collecting tank is connected by infusion pump and pipeline with extraction, concentration tank upper end；The safety valve is cold with vacuum by pipeline
But the entrance connection of surge tank；The extraction, the outer wall of concentration tank are provided with steam heating jacket, the extraction, concentration tank
Top is provided with feeding port and closes the cover of feeding port；The extraction, the lower end of concentration tank are provided with discharge valve.
Preferably, the exit of the vacuum cooled surge tank is provided with the drain pipe with valve by threeway.
Preferably, the discharge valve uses operated pneumatic valve.
Preferably, the cooler uses shell and tube cooler.
Preferably, the surge tank uses vertical buffering tank.
Compared with prior art, the utility model has the following advantages that：
After alcohol recycle being carried out by the utility model, alcohol proportion of goods damageds reduction about 20%, about 200,000 yuan of annual earnings increase,
Significantly save production cost.The utility model has many advantages, such as energy-saving and emission-reduction, clean manufacturing, environmental protection, safe.
Description of the drawings
It in order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the structure diagram of the utility model.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of making the creative labor
All other embodiments obtained shall fall within the protection scope of the present invention.
Alcohol recovery system shown in FIG. 1 is provided with extraction, the concentration tank of main vacuum manifold 1 and safety valve 2 including upper end
3, the cooler 4 that entrance is connected with main vacuum manifold 1, entrance passes through pipeline and the surge tank 5 of the outlet of cooler 4 connection, entrance
Pipeline and vacuum cooled surge tank 6 are passed through by the vacuum cooled surge tank 6 and upper end of pipeline and the outlet of surge tank 5 connection
The collecting tank 7 of leakage fluid dram connection；The collecting tank 7 is connected by infusion pump 8 and pipeline with extraction, 3 upper end of concentration tank；The peace
Full valve 2 is connected by pipeline with the entrance of vacuum cooled surge tank 6；The extraction, the outer wall of concentration tank 3 are provided with steam heating
Chuck 9, the extraction, the top of concentration tank 3 are provided with feeding port 10 and close the cover 11 of feeding port 10；It is described to extract, is dense
The lower end of contracting tank 3 is provided with discharge valve 12.
The exit of the vacuum cooled surge tank 6 is provided with the drain pipe 13 with valve by threeway.It can further carry
The rate of recovery of high alcohol.
The discharge valve 12 preferably uses operated pneumatic valve.The cooler 4 preferably uses shell and tube cooler.It is described slow
It rushes tank 5 and preferably uses vertical buffering tank.
The utility model is collected by the alcohol steam for discharging main vacuum manifold and is back to workshop recycling,
Significantly save production cost.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modifications, equivalent replacements and improvements are made should be included in the utility model
Protection domain within.
Claims (5)
1. a kind of alcohol recovery system, it is characterised in that：Upper end is provided with main vacuum manifold（1）And safety valve（2）Carry
It takes, concentration tank（3）, entrance and main vacuum manifold（1）The cooler of connection（4）, entrance passes through pipeline and cooler（4）Outlet connects
The surge tank connect（5）, entrance passes through pipeline and surge tank（5）Export the vacuum cooled surge tank of connection（6）And upper end passes through
Pipeline and vacuum cooled surge tank（6）The collecting tank of leakage fluid dram connection（7）；The collecting tank（7）Pass through infusion pump（8）And pipeline
With extraction, concentration tank（3）Upper end connects；The safety valve（2）Pass through pipeline and vacuum cooled surge tank（6）Entrance connection；
The extraction, concentration tank（3）Outer wall be provided with steam heating jacket（9）, the extraction, concentration tank（3）Top be provided with
Feeding port（10）And closing feeding port（10）Cover（11）；The extraction, concentration tank（3）Lower end be provided with discharge valve
（12）.
2. alcohol recovery system according to claim 1, it is characterised in that：The vacuum cooled surge tank（6）Exit
Drain pipe with valve is provided with by threeway（13）.
3. alcohol recovery system according to claim 1 or claim 2, it is characterised in that：The discharge valve（12）Using pneumatic operated valve
Door.
4. alcohol recovery system according to claim 1 or claim 2, it is characterised in that：The cooler（4）It is cooled down using shell and tube
Device.
5. alcohol recovery system according to claim 1 or claim 2, it is characterised in that：The surge tank（5）Using vertical buffering
Tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820077486.2U CN207384879U (en) | 2018-01-17 | 2018-01-17 | A kind of alcohol recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820077486.2U CN207384879U (en) | 2018-01-17 | 2018-01-17 | A kind of alcohol recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207384879U true CN207384879U (en) | 2018-05-22 |
Family
ID=62324331
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820077486.2U Active CN207384879U (en) | 2018-01-17 | 2018-01-17 | A kind of alcohol recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207384879U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108997173A (en) * | 2018-08-03 | 2018-12-14 | 湖北远大富驰医药化工股份有限公司 | A method of recycling dimethyl suflfate from vacuum gas |
-
2018
- 2018-01-17 CN CN201820077486.2U patent/CN207384879U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108997173A (en) * | 2018-08-03 | 2018-12-14 | 湖北远大富驰医药化工股份有限公司 | A method of recycling dimethyl suflfate from vacuum gas |
| CN108997173B (en) * | 2018-08-03 | 2021-01-01 | 湖北远大富驰医药化工股份有限公司 | Method for recovering dimethyl sulfate from vacuum gas |
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