CN205516593U - Evaporate and separate formula condensing equipment - Google Patents
Evaporate and separate formula condensing equipment Download PDFInfo
- Publication number
- CN205516593U CN205516593U CN201620072723.7U CN201620072723U CN205516593U CN 205516593 U CN205516593 U CN 205516593U CN 201620072723 U CN201620072723 U CN 201620072723U CN 205516593 U CN205516593 U CN 205516593U
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- CN
- China
- Prior art keywords
- condensation
- chamber
- outer tube
- tank body
- cooling medium
- 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.)
- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides an evaporate and separate formula condensing equipment, including a jar body, a jar body is evaporating chamber, separation chamber and condensation chamber from bottom to top in proper order, and the evaporating chamber is equipped with vapour and liquid separator for steam heating evaporation formula in the separation chamber, be equipped with the condensation outer tube on the condensation chamber, is equipped with heat exchange tube and collecting tank on the condensation outer tube, the utility model discloses the mechanism is simple, and reasonable in design through to steam injection in the evaporating chamber, makes specific material evaporation in jar internal material mixture, and material steam is afterwards through the vapour and liquid separator in the separation chamber, separation and purification, and the material steam after the purification gets into, and the condensation chamber carries out the condensation and becomes liquid to instiling into the collecting tank, passing through material liquid phase export discharge afterwards and collect, the material steam of part for condensing is followed material gas exports and is got rid of, the utility model discloses an evaporate and separate's mode is separated required material from the material mixture, collect through the condensation, and the recovery effect is obvious, and the cost recovery is lower.
Description
Technical field
This utility model relates to a kind of evaporation separate type condensing unit.
Background technology
In feed separation technical field, adding thermal release is the most general a kind of technological means, and in actual separation
During, the steam that material evaporation goes out easily is mixed in other liquid materials, when causing material steam condensation to be reclaimed, purity extreme difference,
Meanwhile, the mode of heating mostly is electric heating type, and the control of heats and the maintenance in later stage are the most difficult and relatively costly,
Then when relating to material recycle, it should avoid high cost as far as possible, and improve recovering effect while reducing cost.
Utility model content
For the problems referred to above, the utility model proposes a kind of evaporation separate type condensing unit.
For solving above technical problem, the technical scheme that this utility model provides is:
A kind of evaporation separate type condensing unit, it is characterised in that include that tank body, described tank body are hollow structure, tank body is certainly
Lower and on be followed successively by vaporization chamber, separation chamber and condensation chamber, described vaporization chamber connects with separation chamber, and vaporization chamber is provided with material and enters
Mouth, steam inlet and condensation-water drain, described separation chamber is separated with condensation chamber by dividing plate, is provided with gas-liquid separation in separation chamber
Device, described gas-liquid separator includes that dividing plate is run through in outlet side, described outlet side, connects condensation chamber；
Described condensation chamber is provided with condensation outer tube, and described condensation outer tube includes connecting end and sealed end, and condensation outer tube passes through
Connecting end to be connected with tank body, and connect condensation chamber, described sealed end is sealing state, and condensation outer tube is provided with cooling medium and enters
Mouth, cooling medium outlet, material gaseous phase outlet, material liquid-phase outlet and heat exchanger tube, described cooling medium import and cooling medium
Exporting the axis about condensation outer tube setting up and down, the two ends of heat exchanger tube export with cooling medium import and cooling medium respectively
Being connected, described material gaseous phase outlet and material liquid-phase outlet are setting up and down about the axis of condensation outer tube；
The connection end of described condensation outer tube is extended with collecting tank, and described collecting tank cross section semicircular in shape, described heat exchanger tube is U
Shape, and stretch into collecting tank, heat exchanger tube is fixed by tube sheet, described tube sheet be positioned at cooling medium import and material gaseous phase outlet it
Between, and vertical with the axis of condensation outer tube；
Further, described tank body is provided with observation window, and described observation window is positioned at separation chamber；
Further, described material inlet is positioned at tank base；
Further, the both sides of described tank body are provided with hanger；
Further, described condensation outer tube Zi connect end to sealed end, in arranging obliquely.
The beneficial effects of the utility model are:
A kind of evaporation separate type condensing unit that the utility model proposes, including tank body, tank body is followed successively by steaming from bottom to top
Sending out room, separation chamber and condensation chamber, vaporization chamber is steam heating evaporation formula, is provided with gas-liquid separator, condensation chamber sets in separation chamber
Having condensation outer tube, condensation outer tube to be provided with heat exchanger tube and collecting tank, this utility model mechanism is simple, reasonable in design, by steaming
Sending out indoor injection steam, make specific material evaporation in the mixtures of materials in tank body, material steam is subsequently by separation chamber
Gas-liquid separator, separate and purify, material steam after purification enters, and condensation chamber carries out being condensed into liquid, and instills liquid collecting
Groove, is discharged by material liquid-phase outlet subsequently and collects, and part is the material steam condensed, and gets rid of from material gaseous phase outlet, this reality
With novel by the way of evaporation separates, being separated by required material, collected by condensation from mixtures of materials, recovering effect is bright
Aobvious, and cost recovery is relatively low.
Accompanying drawing explanation
Fig. 1 this utility model schematic diagram.
Fig. 2 this utility model sectional view.
Detailed description of the invention
Evaporation separate type condensing unit as depicted a kind of, it is characterised in that include tank body 1, described tank body 1 is in hollow
Structure, tank body 1 is followed successively by vaporization chamber 2, separation chamber 3 and condensation chamber 4 from bottom to top, and described vaporization chamber 2 connects with separation chamber 3, steams
Sending out room 2 and be provided with material inlet 5, steam inlet 6 and condensation-water drain 7, described separation chamber 3 is by dividing plate 8 and condensation chamber 4 points
Every, it being provided with gas-liquid separator 9 in separation chamber 3, described gas-liquid separator 9 includes that dividing plate is run through in outlet side 10, described outlet side 10
8, connect condensation chamber 4；
Described condensation chamber 4 is provided with condensation outer tube 11, and described condensation outer tube 11 includes connecting end 12 and sealed end 13, condensation
Outer tube 11 is connected with tank body 1 by connecting end 12, and connects condensation chamber 4, and described sealed end 13 is sealing state, condenses outer tube 11
It is provided with cooling medium import 14, cooling medium outlet 15, material gaseous phase outlet 16, material liquid-phase outlet 17 and heat exchanger tube 18,
Described cooling medium import 14 and cooling medium outlet 15 are setting up and down about the axis of condensation outer tube 11, the two of heat exchanger tube 18
End exports 15 with cooling medium import 14 and cooling medium respectively and is connected, described material gaseous phase outlet 16 and material liquid-phase outlet 17
Axis about condensation outer tube 11 is setting up and down；
The connection end 12 of described condensation outer tube 11 is extended with collecting tank 19, and described collecting tank 19 cross section semicircular in shape is described
Heat exchanger tube 18 takes the shape of the letter U, and stretches into collecting tank 19, and heat exchanger tube 18 is fixed by tube sheet 20, and described tube sheet 20 is positioned at cooling medium and enters
Between mouth 14 and material gaseous phase outlet 16 and vertical with the axis of condensation outer tube 11；
Further, described tank body 1 is provided with observation window 21, and described observation window 21 is positioned at separation chamber 3；
Further, described material inlet 5 is positioned at bottom tank body 1；
Further, the both sides of described tank body 1 are provided with hanger 22；
Further, described condensation outer tube 11 Zi connect end 12 to sealed end 13, in arranging obliquely.
A kind of evaporation separate type condensing unit that the utility model proposes, including tank body, tank body is followed successively by steaming from bottom to top
Sending out room, separation chamber and condensation chamber, vaporization chamber is steam heating evaporation formula, is provided with gas-liquid separator, condensation chamber sets in separation chamber
Having condensation outer tube, condensation outer tube to be provided with heat exchanger tube and collecting tank, this utility model mechanism is simple, reasonable in design, by steaming
Sending out indoor injection steam, make specific material evaporation in the mixtures of materials in tank body, material steam is subsequently by separation chamber
Gas-liquid separator, separate and purify, material steam after purification enters, and condensation chamber carries out being condensed into liquid, and instills liquid collecting
Groove, is discharged by material liquid-phase outlet subsequently and collects, and part is the material steam condensed, and gets rid of from material gaseous phase outlet, this reality
With novel by the way of evaporation separates, being separated by required material, collected by condensation from mixtures of materials, recovering effect is bright
Aobvious, and cost recovery is relatively low.
The above, only this utility model preferably detailed description of the invention, but protection domain of the present utility model is not
Being confined to this, any those familiar with the art, in the technical scope that this utility model discloses, can readily occur in
Change or replacement, all should contain in protection domain of the present utility model.Therefore, protection domain of the present utility model should be with
The protection domain of claims is as the criterion.
Claims (5)
1. one kind evaporation separate type condensing unit, it is characterised in that include that tank body, described tank body are hollow structure, tank body under
Being followed successively by vaporization chamber, separation chamber and condensation chamber on and, described vaporization chamber connects with separation chamber, vaporization chamber be provided with material inlet,
Steam inlet and condensation-water drain, described separation chamber is separated with condensation chamber by dividing plate, is provided with gas-liquid separator, institute in separation chamber
State gas-liquid separator and include that dividing plate is run through in outlet side, described outlet side, connect condensation chamber；
Described condensation chamber is provided with condensation outer tube, and described condensation outer tube includes connecting end and sealed end, and condensation outer tube is by connecting
End is connected with tank body, and connects condensation chamber, and described sealed end is sealing state, condenses outer tube and is provided with cooling medium import, cold
Solidifying media outlet, material gaseous phase outlet, material liquid-phase outlet and heat exchanger tube, described cooling medium import and cooling medium outlet are closed
Setting up and down in the axis of condensation outer tube, the two ends of heat exchanger tube export with cooling medium import and cooling medium respectively and are connected,
Described material gaseous phase outlet and material liquid-phase outlet are setting up and down about the axis of condensation outer tube；
The connection end of described condensation outer tube is extended with collecting tank, described collecting tank cross section semicircular in shape, and described heat exchanger tube takes the shape of the letter U,
And stretch into collecting tank, heat exchanger tube is fixed by tube sheet, described tube sheet between cooling medium import and material gaseous phase outlet, and
Vertical with the axis of condensation outer tube.
2. a kind of evaporation separate type condensing unit as claimed in claim 1, it is characterised in that described tank body is provided with observation
Window, described observation window is positioned at separation chamber.
3. a kind of evaporation separate type condensing unit as claimed in claim 1, it is characterised in that described material inlet is positioned at tank body
Bottom.
4. a kind of evaporation separate type condensing unit as claimed in claim 1, it is characterised in that the both sides of described tank body are provided with hangs
Ear.
5. a kind of evaporation separate type condensing unit as claimed in claim 1, it is characterised in that described condensation outer tube is from connecting end
To sealed end, in arranging obliquely.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620072723.7U CN205516593U (en) | 2016-01-26 | 2016-01-26 | Evaporate and separate formula condensing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620072723.7U CN205516593U (en) | 2016-01-26 | 2016-01-26 | Evaporate and separate formula condensing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205516593U true CN205516593U (en) | 2016-08-31 |
Family
ID=56769564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620072723.7U Expired - Fee Related CN205516593U (en) | 2016-01-26 | 2016-01-26 | Evaporate and separate formula condensing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205516593U (en) |
-
2016
- 2016-01-26 CN CN201620072723.7U patent/CN205516593U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20200126 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |