CN206995899U - A kind of energy-efficient distillation still - Google Patents
A kind of energy-efficient distillation still Download PDFInfo
- Publication number
- CN206995899U CN206995899U CN201720760118.3U CN201720760118U CN206995899U CN 206995899 U CN206995899 U CN 206995899U CN 201720760118 U CN201720760118 U CN 201720760118U CN 206995899 U CN206995899 U CN 206995899U
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- distillation still
- chuck
- energy
- steam
- outlet
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Abstract
The utility model discloses a kind of energy-efficient distillation still, belong to distillation technique field.It is low to solve existing distillation still distillation efficiency, distills the problem of cost is high.Described energy-efficient distillation still, including distillation still body, distillation still body exterior is provided with chuck, top is provided with steam (vapor) outlet and charging aperture, and bottom is provided with discharging opening, and described chuck includes upper chuck and lower chuck, upper chuck is arranged on distillation still bodies top, lower chuck is arranged on distillation still body middle and lower part, and steam (vapor) outlet is connected with condenser pipe, and steam (vapor) outlet cross section diameter is gradually reduced by distillation still body to condenser pipe.The utility model distills available for material.
Description
Technical field
A kind of energy-efficient distillation still is the utility model is related to, belongs to distillation technique field.
Background technology
The mode of heating of existing distillation still typically has chuck, semicanal to also have inner coil pipe to heat three kinds of modes, and these three add
Hot mode is typically all to be heated in distillation still middle and lower part, and steam caused by the heating of middle and lower part touches distillation still in uphill process
Wall, steam liquefied are that liquid is back to inside distillation still again, and only small part steam successfully condenses into steam (vapor) outlet, distillation effect
Rate is relatively low.For distillation still in itself for, because heating-up temperature is higher, head temperature is relatively low for middle and lower part, along with steam
A part of heat is taken away in liquefaction causes distillation still middle and lower part and the top temperature difference larger, colds and heat succeed each other and easily causes equipment local stress
Fatigue damage.
Utility model content
The purpose of this utility model is to provide a kind of energy-efficient distillation still, and cost is low, distillation efficiency is high.
Described energy-efficient distillation still, including distillation still body, distillation still body exterior are provided with chuck, and top, which is provided with, steams
Vapor outlet and charging aperture, bottom are provided with discharging opening, and described chuck includes upper chuck and lower chuck, and upper chuck is arranged on distillation still
Bodies top, lower chuck are arranged on distillation still body middle and lower part, and steam (vapor) outlet is connected with condenser pipe, steam (vapor) outlet cross section diameter by
It is gradually reduced at distillation still body to condenser pipe.
Further speaking, the upper Crude product input of described upper chuck is located at the lowest part of upper chuck, upper heating medium
Entrance is in steam (vapor) outlet and distillation still body junction.
Further speaking, the lower heating medium inlet of described lower chuck is in distillation still body middle and upper part, lower heating medium
Outlet is located at distillation still body bottom portion.
Further speaking, described distillation still body interior is additionally provided with liquid level gauge.
Further speaking, described distillation still body exterior is provided with intelligent controller, intelligent controller respectively with lower heating
Medium inlet is connected with lower Crude product input.
Further speaking, described intelligent controller is connected with liquid level gauge.
Further speaking, described distillation still body is additionally provided with agitating device.
The beneficial effects of the utility model compared with prior art：
The utility model distillation still top is provided with chuck, and the heating at the top of distillation still can be achieved, and avoids middle and lower part heating production
Raw steam touches distillation still wall in uphill process, and steam liquefied is that liquid is back to inside distillation still again, is greatly improved
Distillation efficiency, has saved distillation cost, while avoids distillation still middle and lower part and the top temperature difference larger, extends distillation still use
Life-span.Intelligent controller is connected with lower heating medium inlet, lower Crude product input and liquid level gauge respectively, intelligent controller according to
The Liquid level heating medium discrepancy amount of liquid level gauge measurement, the general liquid level for heating medium are higher than the material liquid level in distillation still,
Both will not cause to heat being excessively used for medium causes to waste, and is also unlikely to heat that medium is very few to cause heating incomplete.Intelligence
Controller automatically controls heating medium input quantity and output quantity, and temperature and flow control are more accurate.
Brief description of the drawings
Fig. 1 is the energy-efficient distillation still structural representation of the utility model；
In figure, 1, charging aperture；2nd, upper heating medium inlet；3rd, condenser pipe；4th, steam (vapor) outlet；5th, lower chuck；6th, discharging opening；
7th, lower Crude product input；8th, lower heating medium inlet；9th, upper Crude product input；10th, intelligent controller；11st, liquid level gauge；
12nd, upper chuck；13rd, agitating device；14th, distillation still body.
Embodiment
The utility model is described further with reference to specific embodiment.
Embodiment 1
Described energy-efficient distillation still, including distillation still body 14, the outside of distillation still body 14 are provided with chuck, and top is set
There are steam (vapor) outlet 4 and charging aperture 1, bottom is provided with discharging opening 6, and described chuck includes upper chuck 12 and lower chuck 5, upper chuck 12
Installed in the top of distillation still body 14, lower chuck 5 is arranged on the middle and lower part of distillation still body 14, steam (vapor) outlet 4 and the phase of condenser pipe 3
Even, the cross section diameter of steam (vapor) outlet 4 is gradually reduced by distillation still body 14 to condenser pipe 3.
Embodiment 2
Described energy-efficient distillation still, including distillation still body 14, the outside of distillation still body 14 are provided with chuck, and top is set
There are steam (vapor) outlet 4 and charging aperture 1, bottom is provided with discharging opening 6, and described chuck includes upper chuck 12 and lower chuck 5, upper chuck 12
Installed in the top of distillation still body 14, lower chuck 5 is arranged on the middle and lower part of distillation still body 14, steam (vapor) outlet 4 and the phase of condenser pipe 3
Even, the cross section diameter of steam (vapor) outlet 4 is gradually reduced by distillation still body 14 to condenser pipe 3.The upper heating of described upper chuck 12
Media outlet 9 is located at the lowest part of upper chuck 12, upper heating medium inlet 2 in steam (vapor) outlet 4 and the junction of distillation still body 14,
The lower heating medium inlet 8 of described lower chuck 5 is located at distillation still in the middle and upper part of distillation still body 14, lower Crude product input 7
The bottom of body 14.Liquid level gauge 11 is additionally provided with inside described distillation still body 14, the described outside of distillation still body 14 is provided with intelligence
Energy controller 10, intelligent controller 10 are connected with lower heating medium inlet 8 and lower Crude product input 7 respectively, described intelligence
Controller 10 is connected with liquid level gauge 11, and described distillation still body 14 is additionally provided with agitating device 13.
During work, it would be desirable to which the material of distillation is added in distillation still by charging aperture 1, and liquid level gauge 11 is determined in distillation still
Amount of liquid is sent to intelligent controller 10, and material addition of the intelligent controller 10 in distillation still is entered by lower heating medium
Mouth 8 adds heating medium into lower chuck 5, and controls the lower discharge of Crude product input 7, and the liquid level for typically heating medium is higher than
Material liquid level in distillation still, while heating medium is added into upper chuck 12 by upper heating medium inlet 2, start stirring dress
Put 13 to begin to warm up, steam caused by the heated material of lower chuck 5, rise to distillation still roof, due to the top of distillation still body 14
Provided with upper chuck 12, therefore the head temperature of distillation still body 14 is higher, and steam will not liquefy herein, a large amount of material steams have to
Unique steam (vapor) outlet 4 moves, and steam (vapor) outlet 4 is connected with condenser pipe 3, and steam is liquefied at condenser pipe 3, simultaneously because steam
Outlet 4 tilts down, and liquefied material is unlikely to be back to distillation still, and which greatly enhances distillation efficiency.Distillation is completed to stop
Stirring, heating, the heating medium being vented in upper chuck 12 and lower chuck 5, the steaming in distillation still body 14 is discharged by discharging opening 6
Evaporate residue.
Claims (7)
1. a kind of energy-efficient distillation still, including distillation still body (14), distillation still body (14) is outside to be provided with chuck, and top is set
There are steam (vapor) outlet (4) and charging aperture (1), bottom is provided with discharging opening (6), it is characterised in that：Described chuck includes upper chuck
(12) it is arranged on lower chuck (5), upper chuck (12) at the top of distillation still body (14), lower chuck (5) is arranged on distillation still body
(14) middle and lower part, steam (vapor) outlet (4) are connected with condenser pipe (3), and steam (vapor) outlet (4) cross section diameter is extremely cold by distillation still body (14)
Solidifying pipe (3) place is gradually reduced.
2. energy-efficient distillation still according to claim 1, it is characterised in that：The upper heating of described upper chuck (12) is situated between
Matter outlet (9) is located at the lowest part of upper chuck (12), and upper heating medium inlet (2) is in steam (vapor) outlet (4) and distillation still body
(14) junction.
3. energy-efficient distillation still according to claim 2, it is characterised in that：The lower heating of described lower chuck (5) is situated between
Matter entrance (8) is located at distillation still body (14) bottom in distillation still body (14) middle and upper part, lower Crude product input (7).
4. according to the energy-efficient distillation still described in claim 1-3 any claims, it is characterised in that：Described distillation still
Liquid level gauge (11) is additionally provided with inside body (14).
5. energy-efficient distillation still according to claim 4, it is characterised in that：Set outside described distillation still body (14)
Have an intelligent controller (10), intelligent controller (10) respectively with lower heating medium inlet (8) and lower Crude product input (7) phase
Even.
6. energy-efficient distillation still according to claim 5, it is characterised in that：Described intelligent controller (10) and liquid level
(11) are counted to be connected.
7. energy-efficient distillation still according to claim 6, it is characterised in that：Described distillation still body (14) is additionally provided with
Agitating device (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720760118.3U CN206995899U (en) | 2017-06-27 | 2017-06-27 | A kind of energy-efficient distillation still |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720760118.3U CN206995899U (en) | 2017-06-27 | 2017-06-27 | A kind of energy-efficient distillation still |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206995899U true CN206995899U (en) | 2018-02-13 |
Family
ID=61448946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720760118.3U Expired - Fee Related CN206995899U (en) | 2017-06-27 | 2017-06-27 | A kind of energy-efficient distillation still |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206995899U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109603682A (en) * | 2018-12-12 | 2019-04-12 | 广州道林合成材料有限公司 | De- low molecule equipment and silicone oil preparation method |
| CN110106078A (en) * | 2019-05-15 | 2019-08-09 | 纳来创硕湖北生物科技有限公司 | It is a kind of for producing the liquefying plant and liquifying method of starch sugar |
-
2017
- 2017-06-27 CN CN201720760118.3U patent/CN206995899U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109603682A (en) * | 2018-12-12 | 2019-04-12 | 广州道林合成材料有限公司 | De- low molecule equipment and silicone oil preparation method |
| CN110106078A (en) * | 2019-05-15 | 2019-08-09 | 纳来创硕湖北生物科技有限公司 | It is a kind of for producing the liquefying plant and liquifying method of starch sugar |
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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 |
Granted publication date: 20180213 Termination date: 20180627 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |