CN201429340Y - condenser - Google Patents
condenser Download PDFInfo
- Publication number
- CN201429340Y CN201429340Y CN2009200913546U CN200920091354U CN201429340Y CN 201429340 Y CN201429340 Y CN 201429340Y CN 2009200913546 U CN2009200913546 U CN 2009200913546U CN 200920091354 U CN200920091354 U CN 200920091354U CN 201429340 Y CN201429340 Y CN 201429340Y
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- CN
- China
- Prior art keywords
- solvent
- pipe
- condensing
- steam
- chamber
- 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 discloses a condenser, which comprises a condensing chamber, wherein a solvent condensing pipe is arranged in the inner cavity of the condensing chamber; a steam inlet is formed at the upper end of the condensing chamber; a steam admission pipe extending from the steam inlet into the inner cavity of the condensing chamber is communicated with the upper end of the solvent condensing pipe; a solvent recovering pipe extending out of the condensing chamber is arranged at the lower part of the solvent condensing pipe; and a condensing water pipe with a water inlet and a water outlet is wound between the inner wall of the condensing chamber and the outer wall of the solvent condensing pipe. The condenser is characterized in that the solvent steam from the steam and water separating chamber enters the solvent condensing pipe through the steam inlet at the upper end of the condensing chamber and the steam admission pipe; the condensation water enters the condensing water pipewound on the outer wall through the water inlet so as to cool the solvent steam in the solvent condensing pipe; and the solvent is recovered into the solvent recovering bottle through the solvent recovering pipe after vaporous solvent is converted into liquid solvent. The utility model has more reasonable structure and more sufficient condensing effect; and the solvent recovering rate can be greatly improved and the manufacturing cost can be reduced as well.
Description
Technical field
The utility model relates to the medicine and the concentrator of chemical industry, especially relates to the used condenser of solvent recovery when treating that concentrated solution is concentrated.
Background technology
In treating the process that concentrated solution concentrates, solvent participates in its overall process that concentrates, and after waiting to concentrate end-of-job, the solvent that is heated into steam will be separated with treating concentrated solution in condenser, and it will be reused after reclaiming.The condenser that tradition is used is because the air intake of steam is opened in the bottom, and condensation effect is bad, has directly influenced solvent recovering yield.
The utility model content
The purpose of this utility model is to provide the condenser that a kind of condensation effect is abundant, solvent recovering rate is high.
For achieving the above object, the utility model can be taked following technical proposals:
Condenser described in the utility model, comprise condensation chamber, be provided with the solvent condenses pipe in the described condensation chamber inner chamber, be provided with air intake in described condensation chamber upper end, the steam inlet pipe that extends in the condensation chamber inner chamber from described air intake is connected with the upper end of solvent condenses pipe; Be provided with the solvent recovery pipe that extends outside the condensation chamber in the bottom of described solvent condenses pipe; Coiling has the condensate pipe that has entery and delivery port between described condensation chamber inwall and solvent condenses pipe outer wall.
Described condensate pipe is inside and outside two-layer arrangement setting.
Described solvent condenses pipe is the alternate special-shaped body of diameter thickness.
Advantage of the present utility model is that the solvent vapo(u)r that will come out from the vapor-liquid separation chamber air intake by the condensation chamber upper end is in steam inlet pipe enters the solvent condenses pipe, condensed water enters in the condensate pipe that is coiled on its outer wall from water inlet the solvent vapo(u)r in the solvent condenses pipe is cooled off, solvent becomes liquid state by steam state after condensation, receives to the solvent recovery bottle through the solvent recovery pipe.The utility model structure is more reasonable, and condensation effect is more abundant, can improve solvent recovering rate greatly, reduces production costs.
With two-layer arrangement setting inside and outside the condensate pipe, can be more abundant to the condensation of solvent vapo(u)r.
The solvent condenses pipe is adopted the alternate special-shaped body of diameter thickness, can satisfy the requirement of steam throttle flow, improve solvent recovering rate.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 be Figure 1A-A to the sectional structure schematic diagram.
The specific embodiment
As shown in Figure 1, 2, condenser described in the utility model, comprise condensation chamber 1, be provided with the alternate special-shaped solvent condenses pipe 2 of diameter thickness in described condensation chamber 1 inner chamber, be provided with air intake in described condensation chamber 1 upper end, the steam inlet pipe 3 that extends in condensation chamber 1 inner chamber from described air intake is connected with the upper end of solvent condenses pipe 2; Be provided with the solvent recovery pipe 4 that extends outside the condensation chamber 1 in the bottom of described solvent condenses pipe 2; Coiling has the condensate pipe 7 that has entery and delivery port 5,6 between described condensation chamber 1 inwall and solvent condenses pipe 2 outer walls, and for increasing condensation effect, described condensate pipe 7 is inside and outside two-layer arrangement setting.
The air intake of steam inlet pipe 3 is connected with the steam (vapor) outlet of the vapor-liquid separation chamber of concentrator, during operation, vacuum by condenser, air pressure conversion mouthfuls 8 convert condensation chamber to vacuum state (0.08MPa), the air intake of solvent vapo(u)r by condensation chamber 1 upper end is in steam inlet pipe 3 enters solvent condenses pipe 2, condensed water enters in the condensate pipe 7 that is coiled on its outer wall from water inlet 5 solvent vapo(u)r is cooled off, and solvent becomes liquid state by steam state after condensation; During tapping, convert condensation chamber to atmospheric pressure state, liquid solvent is received to the solvent recovery bottle through the solvent recovery pipe.
Claims (3)
1, a kind of condenser, comprise condensation chamber (1), it is characterized in that: be provided with solvent condenses pipe (2) in described condensation chamber (1) inner chamber, be provided with air intake in described condensation chamber (1) upper end, the steam inlet pipe (3) that extends in condensation chamber (1) inner chamber from described air intake is connected with the upper end of solvent condenses pipe (2); Be provided with the solvent recovery pipe (4) that extends outside the condensation chamber (1) in the bottom of described solvent condenses pipe (2); Coiling has the condensate pipe (7) that has entery and delivery port (5,6) between described condensation chamber (1) inwall and solvent condenses pipe (2) outer wall.
2, condenser according to claim 1 is characterized in that: described condensate pipe (7) is inside and outside two-layer arrangement setting.
3, condenser according to claim 1 and 2.It is characterized in that: described solvent condenses pipe (2) is the alternate special-shaped body of diameter thickness.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200913546U CN201429340Y (en) | 2009-07-08 | 2009-07-08 | condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200913546U CN201429340Y (en) | 2009-07-08 | 2009-07-08 | condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201429340Y true CN201429340Y (en) | 2010-03-24 |
Family
ID=42033079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200913546U Expired - Fee Related CN201429340Y (en) | 2009-07-08 | 2009-07-08 | condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201429340Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102809304A (en) * | 2012-05-04 | 2012-12-05 | 上海理工大学 | Glass cooling condenser |
-
2009
- 2009-07-08 CN CN2009200913546U patent/CN201429340Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102809304A (en) * | 2012-05-04 | 2012-12-05 | 上海理工大学 | Glass cooling condenser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100324 Termination date: 20100708 |