CN206526526U - A kind of refined terpinol low energy cost vacuum drying device - Google Patents
A kind of refined terpinol low energy cost vacuum drying device Download PDFInfo
- Publication number
- CN206526526U CN206526526U CN201720162544.7U CN201720162544U CN206526526U CN 206526526 U CN206526526 U CN 206526526U CN 201720162544 U CN201720162544 U CN 201720162544U CN 206526526 U CN206526526 U CN 206526526U
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- China
- Prior art keywords
- terpinol
- drying
- refined
- aspiration pump
- collecting duct
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Abstract
The utility model discloses a kind of refined terpinol low energy cost vacuum drying device, including drying, collecting duct and surge drum, having heaters is installed in drying, the side upper end of drying is welded with feed tube, valve is installed, the top of drying is connected by collecting duct is sequentially installed with aspiration pump and condenser pipe on surge drum, collecting duct on feed tube, and aspiration pump is arranged on the side of drying, aspiration pump and heater pass through wire connecting power plug；Drying device of the present utility model is connected drying with surge drum by collecting duct, closed space is formed, terpinol can be made to be carried out in the environment of vacuum, it is to avoid external environmental terpinol, beneficial to refined terpinol, vapor is extracted into condenser pipe and condensed by aspiration pump, can not only dry terpinol, and, vapor can be avoided to be back in drying, drying effect is good, and only two electrical equipments of having heaters and aspiration pump, low consumption.
Description
Technical field
The utility model is related to a kind of Minton dryer, and more particularly to a kind of refined terpinol is dried with low energy cost vacuum
Device.
Background technology
Terpinol is a kind of colourless thick liquid or low melting point clear crystals, 0.9337 DEG C of relative density, 40 DEG C of solidification point,
220.85 DEG C of boiling point, with lilac taste, its formic acid esters and acetic acid esters are prepared available for essence, for senior solvent and are deodorized
Agent.Also it is used in medicine, agricultural chemicals, plastics, soap, ink industry, is the solvent of color on glassware, existing terpinol again
It is interior to contain moisture, therefore, need that terpinol is dried during production, however, existing drying device is sealed
Property it is bad, external environmental terpinol can be made, be unfavorable for refined terpinol.
Utility model content
The utility model proposes a kind of refined terpinol low energy cost vacuum drying device, solve and do in the prior art
Dry device poor sealing, can make external environmental terpinol, the problem of being unfavorable for refined terpinol, of the present utility model dry
Dry device, in the environment of vacuum, to terpinol is dried, drying property is good, can avoid external environmental terpinol,
Beneficial to refined terpinol.
In order to solve the above-mentioned technical problem, the utility model provides following technical scheme：
A kind of refined terpinol low energy cost vacuum drying device of the utility model, including drying, collecting duct and receipts
Collect and having heaters is installed in cylinder, the drying, the side upper end of the drying, which is welded with feed tube, the feed tube, pacifies
Equipped with valve, the top of the drying is connected by collecting duct is sequentially installed with pumping on surge drum, the collecting duct
Pump and condenser pipe, and the aspiration pump is arranged on the side of drying, the aspiration pump and heater connect electricity by wire
Source plug.
As a kind of optimal technical scheme of the present utility model, the side lower end of the surge drum and drying is welded with
Valve is mounted on drain pipe, and two drain pipes.
As a kind of optimal technical scheme of the present utility model, the inlet of the feed tube is funnel type.
As a kind of optimal technical scheme of the present utility model, the side upper end of the condenser pipe is provided with water inlet pipe, institute
The opposite side lower end for stating condenser pipe is provided with outlet pipe.
As a kind of optimal technical scheme of the present utility model, the collecting duct is connected to the top of surge drum.
The beneficial effect that the utility model is reached is：Drying device of the present utility model is by collecting duct by drying
Connected with surge drum, form closed space, terpinol can be made to be carried out in the environment of vacuum, it is to avoid external environmental pine
Oleyl alcohol, beneficial to refined terpinol, heats terpinol by heater, makes the moisture evaporation in terpinol, meanwhile, aspiration pump is by water
Steam is extracted into condenser pipe and condensed, and makes after water vapor condensation, flows in surge drum, can not only dry terpinol, and
And, vapor can be avoided to be back in drying, drying effect is good, and only two electrical equipments of having heaters and aspiration pump,
Power consumption is compared for other drying devices, and consumption is few, is easy to use and is promoted.
Brief description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and constitutes a part for specification, with this practicality
New embodiment is used to explain the utility model together, does not constitute to limitation of the present utility model.In the accompanying drawings：
Fig. 1 is subjective structural representation of the present utility model；
In figure：1st, drying；2nd, heater；3rd, feed tube；4th, valve；5th, drain pipe；6th, collecting duct；7th, surge drum；
8th, aspiration pump；9th, condenser pipe；10th, water inlet pipe；11st, outlet pipe.
Embodiment
Preferred embodiment of the present utility model is illustrated below in conjunction with accompanying drawing, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain the utility model, be not used to limit the utility model.
Embodiment 1
As shown in figure 1, the utility model provides a kind of refined terpinol low energy cost vacuum drying device, including drying
Having heaters 2 is installed in the 1st, collecting duct 6 and surge drum 7, drying 1, is easy to heat terpinol, the side upper end of drying 1
Feed tube 3 is welded with, is easy to import terpinol in drying 1, valve 4 is installed on feed tube 3, the top of drying 1 leads to
The connection surge drum 7 of collecting duct 6 is crossed, the vapor being thermally formed can imported into surge drum 7, be easy to do by collecting duct 6
Aspiration pump 8 and condenser pipe 9 are sequentially installed with dry terpinol, collecting duct 6, and aspiration pump 8 is arranged on the side of drying 1,
Aspiration pump 8 and heater 2 pass through wire connecting power plug.
The side lower end of surge drum 7 and drying 1 is welded with drain pipe 5, is easy to export the water and drying of surge drum 7
Valve 4 is mounted on dried terpinol in 1, and two drain pipes 5, when being easy to make to dry, drying device forms closed
Space.
The inlet of feed tube 3 is funnel type, and the feed tube 3 of funnel type is easy to terpinol importeding into drying 1.
The side upper end of condenser pipe 9 is provided with water inlet pipe 10, and the opposite side lower end of condenser pipe 9 is provided with outlet pipe 11, just
In making condensed water be flowed in the tube wall of condenser pipe 9, consequently facilitating condensed steam, collecting duct 6 is connected to the top of surge drum 7
End.
Specifically, in use, by feed tube 3, terpinol is imported in drying 1, the valve 4 closed on feed tube 3,
The attaching plug of aspiration pump 8 and heater 2 is inserted into power supply, is powered, the heating terpinol of heater 2, because the boiling point of terpinol
Higher than the boiling point of water, it therefore, it can the water evaporation in terpinol, the vapor after evaporation passes through the condensation on collecting duct 6
Pipe 9 is condensed, afterwards, into surge drum 7, and vapor is extracted into condenser pipe 9 by the aspiration pump 8 on collecting duct 6
Row condensation, can not only dry terpinol, furthermore, it is possible to avoid vapor from being back in drying 1, drying effect is good, and only
8 two electrical equipments of having heaters 2 and aspiration pump, power consumption is compared for other drying devices, and consumption is few, is easy to use and is pushed away
Extensively.
Drying device of the present utility model is connected drying 1 with surge drum 7 by collecting duct 6, forms closed sky
Between, terpinol can be made to be carried out in the environment of vacuum, it is to avoid external environmental terpinol, beneficial to refined terpinol, passed through
Heater 2 heats terpinol, makes the moisture evaporation in terpinol, meanwhile, vapor is extracted into condenser pipe 9 and carried out by aspiration pump 8
Condensation, makes after water vapor condensation, flows in surge drum 7, can not only dry terpinol, furthermore, it is possible to avoid vapor from returning
Flow in drying 1, drying effect is good, and only 8 two electrical equipments of having heaters 2 and aspiration pump, power consumption is dry compared to other
For dry device, consumption is few, is easy to use and promotes.
Finally it should be noted that：Preferred embodiment of the present utility model is the foregoing is only, this is not limited to
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Carry out equivalent substitution.It is all it is of the present utility model spirit and principle within, any modification, equivalent substitution and improvements made etc.,
It should be included within protection domain of the present utility model.
Claims (5)
1. a kind of refined terpinol low energy cost vacuum drying device, including drying (1), collecting duct (6) and surge drum
(7), it is characterised in that having heaters (2) is installed in the drying (1), the side upper end of the drying (1) be welded with into
Valve (4) is installed, the top of the drying (1) is connected by collecting duct (6) receives on liquid pipe (3), the feed tube (3)
Collect and be sequentially installed with aspiration pump (8) and condenser pipe (9) on cylinder (7), the collecting duct (6), and the aspiration pump (8) is arranged on
The side of drying (1), the aspiration pump (8) and heater (2) pass through wire connecting power plug.
2. a kind of refined terpinol low energy cost vacuum drying device according to claim 1, it is characterised in that the receipts
The side lower end of collection cylinder (7) and drying (1), which is welded with drain pipe (5), and two drain pipes (5), is mounted on valve
Door (4).
3. a kind of refined terpinol low energy cost vacuum drying device according to claim 1, it is characterised in that it is described enter
The inlet of liquid pipe (3) is funnel type.
4. a kind of refined terpinol low energy cost vacuum drying device according to claim 1, it is characterised in that described cold
The side upper end of solidifying pipe (9) is provided with water inlet pipe (10), and the opposite side lower end of the condenser pipe (9) is provided with outlet pipe (11).
5. a kind of refined terpinol low energy cost vacuum drying device according to claim 1, it is characterised in that the receipts
Collection conduit (6) is connected to the top of surge drum (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720162544.7U CN206526526U (en) | 2017-02-23 | 2017-02-23 | A kind of refined terpinol low energy cost vacuum drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720162544.7U CN206526526U (en) | 2017-02-23 | 2017-02-23 | A kind of refined terpinol low energy cost vacuum drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206526526U true CN206526526U (en) | 2017-09-29 |
Family
ID=59919987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720162544.7U Expired - Fee Related CN206526526U (en) | 2017-02-23 | 2017-02-23 | A kind of refined terpinol low energy cost vacuum drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206526526U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109966769A (en) * | 2019-04-09 | 2019-07-05 | 安庆和兴化工有限责任公司 | A kind of butanediol low-temperature water removal equipment and its application method |
-
2017
- 2017-02-23 CN CN201720162544.7U patent/CN206526526U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109966769A (en) * | 2019-04-09 | 2019-07-05 | 安庆和兴化工有限责任公司 | A kind of butanediol low-temperature water removal equipment and its application method |
| CN109966769B (en) * | 2019-04-09 | 2021-06-04 | 安庆和兴化工有限责任公司 | Butanediol low-temperature water removal equipment and use method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170929 Termination date: 20180223 |