CN202315340U - Continuous vacuum decompression concentrator - Google Patents
Continuous vacuum decompression concentrator Download PDFInfo
- Publication number
- CN202315340U CN202315340U CN2011204750140U CN201120475014U CN202315340U CN 202315340 U CN202315340 U CN 202315340U CN 2011204750140 U CN2011204750140 U CN 2011204750140U CN 201120475014 U CN201120475014 U CN 201120475014U CN 202315340 U CN202315340 U CN 202315340U
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- CN
- China
- Prior art keywords
- evaporation
- heating tank
- vacuum decompression
- feed liquid
- continuous vacuum
- 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
A continuous vacuum decompression concentrator mainly resolves the problem that an existing vacuum decompression concentrator is long in feed liquid evaporation time and low in production efficiency. The continuous vacuum decompression concentrator comprises an evaporation heating tank (1), a steam-liquid separator (2) and a condenser (3) which are sequentially connected. The outer wall of the evaporation heating tank (1) is provided with a jacket (4) filled with high-temperature steam. A feed liquid inlet (5) is disposed above the evaporation heating tank (1). The continuous vacuum decompression concentrator is characterized in that a heating device (6) is disposed at the position of the feed liquid inlet (5) in the evaporation heating tank (1), and feed liquid is preheated by the heating device (6). The continuous vacuum decompression concentrator effectively shortens time for feed liquid evaporation during continuous production, and has the advantages of being simple in structure and high in production efficiency.
Description
Technical field
The utility model relates to a kind of inspissator, is specifically related to a kind of continuous vacuum decompression inspissator.
Background technology
Need feed liquid be concentrated in industries such as pharmacy, food, chemical industry, the vacuum decompression inspissator is a kind of concentrator that generally adopts.Existing vacuum decompression inspissator mainly is made up of evaporation heating tank, vapour liquid separator and condenser; Evaporation heating tank, vapour liquid separator and condenser connect successively; Feed liquid after vaporization vapour phase after vapor-liquid separation gets into condenser, and then obtains the higher feed liquid of concentration.The outer wall of evaporation heating tank is provided with chuck, in chuck, feeds high-temperature steam, in order to the feed liquid heating, vacuumizes in the evaporation heating tank, has reduced feed liquid boiling point (vapourizing temperature), and feed liquid just can be vaporized in lower temperature, has improved the heat energy utilization rate.There is following defective in this vacuum decompression inspissator: when serialization was produced, the time that gets into the feed liquid vaporization in the evaporation heating tank was longer, and production efficiency is low, is difficult to satisfy the demand of modern enterprise High-efficient Production.
The utility model content
For the deficiency that time is long, production efficiency is low that overcomes existing vacuum decompression inspissator feed liquid vaporization; The utility model provides a kind of continuous vacuum decompression inspissator; This continuous vacuum decompression inspissator has shortened the time of feed liquid vaporization when serialization is produced effectively, has characteristics simple in structure and that production efficiency is high.
The technical scheme of the utility model is: this continuous vacuum decompression inspissator comprises evaporation heating tank, vapour liquid separator and the condenser that links to each other successively; The outer wall of evaporation heating tank is provided with the chuck that feeds high-temperature steam; The top of evaporation heating tank is provided with liquor inlet; The liquor inlet place is provided with heater in the evaporation heating tank, and feed liquid is by described heater preheating.
Described heater is the heating tube of coiled coil, and the entrance point of heating tube passes and is communicated with high-temperature steam from the sidewall of evaporation heating tank, and the port of export of heating tube communicates with chuck.
The bending downwards of the port of export of described heating tube extends to the bottom of evaporation heating tank.
The utlity model has following beneficial effect: owing to take such scheme, adopt heater that the feed liquid that gets in the evaporation heating tank has been carried out preheating, shortened the time of feed liquid vaporization when serialization is produced effectively, simple in structure, production efficiency is high.
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model.
1-evaporation heating tank among the figure, 2-vapour liquid separator, 3-condenser, 4-chuck, 5-liquor inlet, 6-heater, 61-heating tube, 62-entrance point, the 63-port of export.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further:
By shown in Figure 1; This continuous vacuum decompression inspissator comprises evaporation heating tank 1, vapour liquid separator 2 and the condenser 3 that links to each other successively; The outer wall of evaporation heating tank 1 is provided with the chuck 4 that feeds high-temperature steam; The top of evaporation heating tank 1 is provided with liquor inlet 5, and liquor inlet 5 places are provided with heater 6 in the evaporation heating tank 1, and feed liquid is by described heater 6 preheatings.Heater 6 can be selected electric heating tube, fuelizer, high-temperature steam heating tube etc. for use; Because the feed liquid that adopts 6 pairs of heaters to get in the evaporation heating tank 1 has been carried out preheating; Shortened the time of feed liquid vaporization when serialization is produced effectively, simple in structure, production efficiency is high.
Described heater 6 is the heating tube 61 of coiled coil, and the entrance point 62 of heating tube 61 passes and is communicated with high-temperature steam from the sidewall of evaporation heating tank 1, and the port of export 63 of heating tube 61 communicates with chuck 4.Present embodiment is an optimal way, and heating tube 61 independent external high-temperature steam sources have guaranteed the temperature of heating tube 61, and the port of export 63 of heating tube 61 is connected chucks 4, and the waste heat that utilizes high-temperature steam heats the feed liquid of evaporation heating tank 1, saves the energy.
The port of export 63 bending downwards of described heating tube 61 extends to the bottom of evaporation heating tank 1.The waste heat of the high-temperature steam in the heating tube 61 makes full use of more.
Claims (3)
1. continuous vacuum decompression inspissator; Comprise the evaporation heating tank (1), vapour liquid separator (2) and the condenser (3) that link to each other successively; The outer wall of evaporation heating tank (1) is provided with the chuck (4) that feeds high-temperature steam; The top of evaporation heating tank (1) is provided with liquor inlet (5), it is characterized in that: the evaporation interior liquor inlet of heating tank (1) (5) locates to be provided with heater (6), and feed liquid is by described heater (6) preheating.
2. continuous vacuum decompression inspissator according to claim 1; It is characterized in that: described heater (6) is the heating tube of coiled coil (61); The entrance point (62) of heating tube (61) passes and is communicated with high-temperature steam from the sidewall of evaporation heating tank (1), and the port of export (63) of heating tube (61) communicates with chuck (4).
3. continuous vacuum decompression inspissator according to claim 2 is characterized in that: the bending downwards of the port of export (63) of heating tube (61) extends to the bottom of evaporation heating tank (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204750140U CN202315340U (en) | 2011-11-25 | 2011-11-25 | Continuous vacuum decompression concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204750140U CN202315340U (en) | 2011-11-25 | 2011-11-25 | Continuous vacuum decompression concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202315340U true CN202315340U (en) | 2012-07-11 |
Family
ID=46427343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204750140U Expired - Fee Related CN202315340U (en) | 2011-11-25 | 2011-11-25 | Continuous vacuum decompression concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202315340U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007572A (en) * | 2012-12-19 | 2013-04-03 | 温州市天龙轻工设备有限公司 | Medicine extraction device and technique thereof |
-
2011
- 2011-11-25 CN CN2011204750140U patent/CN202315340U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007572A (en) * | 2012-12-19 | 2013-04-03 | 温州市天龙轻工设备有限公司 | Medicine extraction device and technique thereof |
| CN103007572B (en) * | 2012-12-19 | 2014-08-27 | 王茜南 | Medicine extraction device and technique thereof |
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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: 20120711 Termination date: 20121125 |