CN203886205U - Low-temperature concentrating device - Google Patents
Low-temperature concentrating device Download PDFInfo
- Publication number
- CN203886205U CN203886205U CN201420133716.4U CN201420133716U CN203886205U CN 203886205 U CN203886205 U CN 203886205U CN 201420133716 U CN201420133716 U CN 201420133716U CN 203886205 U CN203886205 U CN 203886205U
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- pump
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- heater
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a low-temperature concentrating device. The low-temperature concentrating device comprises a raw liquid storage tank, a feeding pump, an evaporator, a condenser, a heater, a heat source pump and a vacuum automatic draining tank, wherein the raw liquid storage tank is sequentially connected with the feeding pump and the evaporator by pipelines, the evaporator is provided with a discharged material outlet and a steam outlet, the discharged material outlet is sequentially connected with a circulating pump and the heater by pipelines, the heater is connected with a material circular-processing inlet of the evaporator, a pipeline connected with the discharged material outlet is also connected with a discharging pump, the steam outlet is connected with the condenser, both a hot water inlet and a hot water outlet of the heater are connected with a hot water tank by pipelines, a hot water pump is arranged on a pipeline for connecting the hot water tank with the heater, both a cold water inlet and a cold water outlet of the condenser are connected with a cold water tank by a pipeline, a cold water pump is arranged on a pipeline for connecting the condenser with the cold water tank, the heat source pump is connected with the cold water tank and the hot water tank, a condensed water outlet in the condenser is connected with the vacuum automatic draining tank by a pipeline, and the vacuum automatic draining tank is connected with a condensate pump and a vacuum unit. The low-temperature concentrating device can achieve material concentration at low temperature as low as 24 DEG C.
Description
Technical field
The utility model relates to a kind of low temperature enrichment facility.
Background technology
Tradition enrichment facility is mainly comprised of heating tank, evaporator and drainer; In the upper and lower part of heating tank, set out respectively material mouth and charging aperture, lower end at heating tank connects concentrate baiting valve, steam heat exchanging tube is set in heating tank, the two ends of described steam heat exchanging tube are respectively equipped with vapours import and condensate drain outlet, and described vapours import and condensate drain outlet are separately positioned on the sidewall of heating tank; At evaporator top, be provided with steam outlet, evaporator middle part is provided with the charging aperture being connected with the discharging opening of described heating tank, and evaporator lower end is provided with the discharging opening being connected with the charging aperture of heating tank, and evaporator middle part is provided with stoste charging aperture; On drainer top, be provided with the steam inlet port being connected with the steam outlet of evaporator, the bottom of drainer is provided with and vacuumizes outlet, cooling tube is set in drainer, stretch out at the two ends of described cooling tube respectively autocondensation tank, and be connected in series with cooling tower by intake pump, in the lower end of drainer, condensed water elimination valve is set.But the energy consumption of this enrichment facility is higher, and concentrated heating is temperature required higher, for some, to low temperature, requires high material cannot carry out concentration.
Summary of the invention
In view of the deficiency of background technology, it is low and can carry out at a lower temperature the low temperature enrichment facility of concentration that technical problem to be solved in the utility model is to provide a kind of power consumption of polymer processing.
For this reason, the low temperature enrichment facility that the utility model provides, comprise former liquid storage tank, feed pump, evaporimeter, condenser, heater, thermal source pump and automatic vacuum liquor drainage tank, wherein said former liquid storage tank connects feed pump and evaporimeter successively by pipeline, evaporimeter has discharge outlet and steam (vapor) outlet, discharge outlet connects circulating pump and heater successively by pipeline, heater is processed entrance with the Matter Transfer of evaporimeter and is connected, the pipeline being connected with discharge outlet also connects discharging pump, described steam (vapor) outlet is connected with condenser, the hot water inlet of described heater is all connected with boiler by pipeline with hot water outlet, on the pipeline of connection boiler and heater, dispose heat-exchanger pump, the cold water inlet of described condenser is all connected with cold water storage cistern by pipeline with cooling water outlet, on the pipeline that condenser is connected with cold water storage cistern, be provided with water supply pump, described thermal source pump connects cold water storage cistern and boiler, condensed water liquid outlet in described condenser is connected with automatic vacuum liquor drainage tank by pipeline, automatic vacuum liquor drainage tank is connected with vacuum unit with condensate pump.
In the utility model, adopt thermal source pump to connect cold water storage cistern and boiler, make evaporimeter hot water used and condenser cold water used can under the processing of thermal source pump, carry out energy exchange, thereby reduced the energy loss of condenser and evaporimeter, and make heating-up temperature lower, in actual treatment, generally reach 24 degrees Celsius.
Accompanying drawing explanation
The low temperature enrichment facility structural representation that Fig. 1 provides for the utility model.
The specific embodiment
As shown in Figure 1, the low temperature enrichment facility that the utility model provides, comprise former liquid storage tank 1, feed pump 2, evaporimeter 3, condenser 4, heater 5, thermal source pump and automatic vacuum liquor drainage tank 6, wherein said former liquid storage tank 1 connects feed pump 2 and evaporimeter 3 successively by pipeline, evaporimeter 3 has discharge outlet 7 and steam (vapor) outlet 8, discharge outlet 7 connects circulating pump 9 and heater 5 successively by pipeline, heater 5 is processed entrance 19 with the Matter Transfer of evaporimeter 3 and is connected, also connect discharging pump 10 with discharge outlet 7 pipelines that are connected, described steam (vapor) outlet 8 is connected with condenser 4, evaporimeter 3 is provided with demister 11 with condenser 4 junctions, the foam that demister 11 can produce material evaporation is removed, the hot water inlet 12 of described heater 5 is all connected with boiler 14 by pipeline with hot water outlet 13, on the pipeline of connection boiler 14 and heater 5, dispose heat-exchanger pump 15, the cold water inlet of described condenser 4 is all connected with cold water storage cistern 16 by pipeline with cooling water outlet, on the pipeline that condenser 4 is connected with cold water storage cistern 16, be provided with water supply pump 17, described thermal source pump connects cold water storage cistern 16 and boiler 14, cold water storage cistern 16 and boiler 14 are co-located in a casing in the present embodiment, condensed water liquid outlet in described condenser 4 is connected with automatic vacuum liquor drainage tank 6 by pipeline, automatic vacuum liquor drainage tank 6 is connected with vacuum unit with condensate pump 18.
Describe the workflow of the low temperature enrichment facility that the utility model provides: a below in detail, material is dropped into former liquid storage tank, by feed pump 2, be transported in evaporimeter 3; B, after the evaporation process of evaporimeter 3, unevaporated material is transported in heater 5 and heats through circulating pump 9, and be again transported to and in evaporimeter 3, carry out evaporation process, heater 5 is connected with boiler 14, and by boiler 14, provided the heat energy of heating, part can be discharged by discharging pump 10 through the material of heating for multiple times evaporation, and the material being evaporated enters condensation in condenser after by demister; The condensed water forming in c, condenser is transported in automatic vacuum liquor drainage tank 6 by pipeline, wherein condenser is connected and provides cooling source by cold water storage cistern with cold water storage cistern 16 circulations, and automatic vacuum liquor drainage tank 6 impels material to be transferred by suction function by connecting vacuum unit.In whole flow process, heater hot water and condenser cold water used used can carry out energy exchange under the processing of thermal source pump.
Claims (1)
1. a low temperature enrichment facility, comprise former liquid storage tank, feed pump, evaporimeter, condenser, heater, thermal source pump and automatic vacuum liquor drainage tank, wherein said former liquid storage tank connects feed pump and evaporimeter successively by pipeline, evaporimeter has discharge outlet and steam (vapor) outlet, discharge outlet connects circulating pump and heater successively by pipeline, heater is processed entrance with the Matter Transfer of evaporimeter and is connected, described steam (vapor) outlet is connected with condenser, the hot water inlet of described heater is all connected with boiler by pipeline with hot water outlet, on the pipeline of connection boiler and heater, dispose heat-exchanger pump, the cold water inlet of described condenser is all connected with cold water storage cistern by pipeline with cooling water outlet, on the pipeline that condenser is connected with cold water storage cistern, be provided with water supply pump, described thermal source pump connects cold water storage cistern and boiler, condensed water liquid outlet in described condenser is connected with automatic vacuum liquor drainage tank by pipeline, automatic vacuum liquor drainage tank is connected with vacuum unit with condensate pump, it is characterized in that: the pipeline being connected with discharge outlet also connects discharging pump, described evaporimeter and condenser junction are provided with demister.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420133716.4U CN203886205U (en) | 2014-03-24 | 2014-03-24 | Low-temperature concentrating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420133716.4U CN203886205U (en) | 2014-03-24 | 2014-03-24 | Low-temperature concentrating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203886205U true CN203886205U (en) | 2014-10-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420133716.4U Expired - Fee Related CN203886205U (en) | 2014-03-24 | 2014-03-24 | Low-temperature concentrating device |
Country Status (1)
| Country | Link |
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| CN (1) | CN203886205U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104436722A (en) * | 2014-12-04 | 2015-03-25 | 宜昌三峡制药有限公司 | Concentration system and concentration method applied to extraction process of isoleucine |
| CN106730937A (en) * | 2016-12-01 | 2017-05-31 | 叶春穗 | Intelligent low-temperature enrichment facility |
| CN106823418A (en) * | 2016-12-01 | 2017-06-13 | 叶春穗 | Efficient low temperature concentration device |
| CN111974015A (en) * | 2020-09-15 | 2020-11-24 | 江西臻强新能源有限公司 | Negative pressure concentration total heat type evaporation recovery system |
-
2014
- 2014-03-24 CN CN201420133716.4U patent/CN203886205U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104436722A (en) * | 2014-12-04 | 2015-03-25 | 宜昌三峡制药有限公司 | Concentration system and concentration method applied to extraction process of isoleucine |
| CN104436722B (en) * | 2014-12-04 | 2016-06-29 | 宜昌三峡制药有限公司 | For concentration systems and method in isoleucine extraction process |
| CN106730937A (en) * | 2016-12-01 | 2017-05-31 | 叶春穗 | Intelligent low-temperature enrichment facility |
| CN106823418A (en) * | 2016-12-01 | 2017-06-13 | 叶春穗 | Efficient low temperature concentration device |
| CN106730937B (en) * | 2016-12-01 | 2023-04-18 | 温州正展机械有限公司 | Intelligent low-temperature concentration device |
| CN111974015A (en) * | 2020-09-15 | 2020-11-24 | 江西臻强新能源有限公司 | Negative pressure concentration total heat type evaporation recovery system |
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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: 20141022 Termination date: 20150324 |
|
| EXPY | Termination of patent right or utility model |