CN201921534U - Low-temperature evaporation concentration device - Google Patents
Low-temperature evaporation concentration device Download PDFInfo
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- CN201921534U CN201921534U CN2011200217763U CN201120021776U CN201921534U CN 201921534 U CN201921534 U CN 201921534U CN 2011200217763 U CN2011200217763 U CN 2011200217763U CN 201120021776 U CN201120021776 U CN 201120021776U CN 201921534 U CN201921534 U CN 201921534U
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- evaporimeter
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- 238000001704 evaporation Methods 0.000 title claims abstract description 25
- 230000008020 evaporation Effects 0.000 title claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 230000008676 import Effects 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 10
- 239000000498 cooling water Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a low-temperature evaporation concentration device which mainly solves the technical problems that as a heater of the existing low-temperature evaporation concentration device carries out heating evaporation on feed liquid in a steam heating mode, the relatively cost is higher, heating and evaporating temperature are higher and the like. The low-temperature evaporation concentration device is characterized in that an energy converter is comprised, wherein a cold water tank with cold water inlet and outlet and a hot water tank with hot water inlet and outlet are arranged on the energy converter, the cold water outlet is connected with a condensate liquid inlet, a condensate liquid outlet is connected with the hot water inlet, the hot water outlet is connected with a heating inlet of the heater, and a heating outlet is connected with the cold water inlet. The low-temperature evaporation concentration device has the beneficial effects that as the energy converter is additionally arranged, the feed liquid can be initially heated by utilizing the electric heater in the energy converter, and after the steam is formed, the feed liquid is then heated again by absorbing the heat of the steam, so that the power consumption can be greatly reduced, and the production cost is lowered.
Description
Technical field
The utility model relates to a kind of concentrated installing and is equipped with, and relates to a kind of low-temperature evaporation enrichment facility in particular, is mainly used in fields such as pharmacy, chemical industry, health products or food processing.
Background technology
Existing low-temperature evaporation enrichment facility mainly includes head tank, evaporimeter, condenser and liquid collecting jar, evaporimeter and liquid collecting jar and communicates with vavuum pump, be provided with the material pump in the bottom of evaporimeter, the import of this material pump communicates with evaporimeter, its outlet communicates with the charging mouth of pipe of a heater, and the discharging mouth of pipe of heater links to each other with evaporimeter; After feed liquid in the head tank enters evaporimeter, the feed pipe that the material pump is extracted the feed liquid of evaporimeter out heater via enters to be back to after the heater heating again and forms the circulation heating in the evaporimeter, because the mode of heating of existing heater is by steam material to be heated to finish evaporation, cost is higher relatively like this.
Summary of the invention
For adopting Electric heating, the heater that solves existing low-temperature evaporation enrichment facility feed liquid is carried out heating evaporation, its cost higher relatively and heating and evaporating temperature high-technology problem; The utility model provides a kind of low-temperature evaporation enrichment facility, and this device not only can guarantee the heating evaporation of feed liquid, simultaneously, also can reduce power consumption, reduces cost.
For solving above technical problem, the technical scheme that the utility model is taked is a kind of low-temperature evaporation enrichment facility, it includes head tank, evaporimeter, heater, condenser and liquid collecting jar, head tank links to each other with evaporimeter, heater is provided with liquor inlet, material liquid outlet, heating import and heating outlet, at described base of evaporator feed pump is installed, and the import of feed pump links to each other with evaporimeter, outlet links to each other with the liquor inlet of heater, and the material liquid outlet of heater links to each other with evaporimeter; Condenser is provided with steam import and export and condensate liquid import and export, and steam-gas inlet links to each other with evaporimeter, and vapor outlet port links to each other with the liquid collecting jar, and described evaporimeter links to each other with vavuum pump respectively with the liquid collecting jar; It is characterized in that also including energy converter, this energy converter is provided with the cold water storage cistern and the boiler of band hot water or cold water import and export, cooling water outlet links to each other with the condensate liquid import, condensate outlet links to each other with hot water inlet, hot water outlet links to each other with the heating import of heater, and the heating outlet links to each other with cooling water inlet.
Further, described energy converter is a water resource heat pump.
The beneficial effects of the utility model are to add energy converter, utilize the interior electric heater of energy converter that feed liquid is carried out initial heating and get final product, after feed liquid forms steam, again feed liquid is heated by the heat that absorbs steam, can reduce power consumption greatly like this, reduce production costs.
Description of drawings
Fig. 1 is the structural representation of a kind of low-temperature evaporation enrichment facility of the utility model embodiment.
The specific embodiment
Below in conjunction with accompanying drawing the utility model embodiment is described further:
As shown in Figure 1, a kind of low-temperature evaporation enrichment facility of the utility model, it includes head tank 1, evaporimeter 2, heater 3, condenser 4 and liquid collecting jar 5, head tank 1 links to each other with evaporimeter 2, heater 3 is provided with liquor inlet 31, material liquid outlet 32, heating import 33 and heating outlet 34, in described evaporimeter 2 bottoms feed pump 6 is installed, and the import of feed pump 6 links to each other with evaporimeter 2, outlet links to each other with the liquor inlet 31 of heater 3, and the material liquid outlet 32 of heater 3 links to each other with evaporimeter 2; Condenser 4 is provided with steam import and export and condensate liquid import and export 41,42, and steam-gas inlet links to each other with evaporimeter 2, and vapor outlet port links to each other with liquid collecting jar 5, and described evaporimeter 2 links to each other with vavuum pump respectively with liquid collecting jar 5; For the heater 3 that solves existing low-temperature evaporation enrichment facility adopts Electric heating that feed liquid is carried out heating evaporation, its cost higher relatively and heating and evaporating temperature high-technology problem, for reducing energy consumption, reduce cost, this low temperature enrichment facility includes and also includes energy converter 7, this energy converter 7 is provided with band cold water and advances, outlet 71,72 and hot water advance, outlet 73,74 cold water storage cistern and boiler, cooling water outlet 72 links to each other with condensate liquid import 41, condensate outlet 42 links to each other with hot water inlet 73, hot water outlet 74 links to each other with the heating import 33 of heater 3, and heating outlet 34 links to each other with cooling water inlet 71; Add energy converter 7, by the heater in the boiler water is heated and enters heater 3 in the feed liquid through heater 3 is heated in when work through hot water outlet 74, heating import 33, when feed liquid heater via 3 its heat that absorbs water the temperature of water is reduced and through heating export 34, cooling water inlet 71 is back in the cold water storage cistern in the energy converter 7; Separate the formation steam and enter evaporimeter 2 row evaporations after the feed liquid heating, and enter condenser 4 and cool off, reduction is back in energy converter 7 cold water storage cisterns and the water that heats in the boiler is to the feed liquid temperature after heating, and through cooling water outlet 72, condensate liquid import 41 enters in the condenser 4 to be carried out condensation to steam and makes steam form the globule to enter liquid collecting jar 5, and the water in the cold water storage cistern is carrying out steam in the process of condensation, thereby the heat that absorbs steam raises coolant-temperature gage and is back in the boiler, and once more through hot water outlet 74,33 pairs of feed liquids of heating import add thermosetting heat cycles and cool cycles; Adopt this structure, only need utilize energy converter 7 interior electric heaters that feed liquid is carried out initial heating and get final product, after feed liquid forms steam, again feed liquid be heated by the heat that absorbs steam, can reduce power consumption greatly like this, reduce production costs.
In the present embodiment, described energy converter 7 is a water resource heat pump.
The foregoing description should not be considered as restriction of the present utility model, but any improvement of doing based on spirit of the present utility model, all should be within protection domain of the present utility model.
Claims (2)
1. low-temperature evaporation enrichment facility, it includes head tank, evaporimeter, heater, condenser and liquid collecting jar, head tank links to each other with evaporimeter, heater is provided with liquor inlet, material liquid outlet, heating import and heating outlet, at described base of evaporator feed pump is installed, the import of feed pump links to each other with evaporimeter, and outlet links to each other with the liquor inlet of heater, and the material liquid outlet of heater links to each other with evaporimeter; Condenser is provided with steam import and export and condensate liquid import and export, and steam-gas inlet links to each other with evaporimeter, and vapor outlet port links to each other with the liquid collecting jar, and described evaporimeter links to each other with vavuum pump respectively with the liquid collecting jar; It is characterized in that also including energy converter, this energy converter is provided with the cold water storage cistern and the boiler of band hot water or cold water import and export, cooling water outlet links to each other with the condensate liquid import, condensate outlet links to each other with hot water inlet, hot water outlet links to each other with the heating import of heater, and the heating outlet links to each other with cooling water inlet.
2. a kind of low-temperature evaporation enrichment facility according to claim 1 is characterized in that described energy converter is a water resource heat pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200217763U CN201921534U (en) | 2011-01-22 | 2011-01-22 | Low-temperature evaporation concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200217763U CN201921534U (en) | 2011-01-22 | 2011-01-22 | Low-temperature evaporation concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201921534U true CN201921534U (en) | 2011-08-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200217763U Expired - Fee Related CN201921534U (en) | 2011-01-22 | 2011-01-22 | Low-temperature evaporation concentration device |
Country Status (1)
| Country | Link |
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| CN (1) | CN201921534U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102500115A (en) * | 2011-10-21 | 2012-06-20 | 上海亿华科技有限公司 | Energy-conservation evaporating plant of liquid-distributing ring type compressor |
| CN102553275A (en) * | 2012-03-16 | 2012-07-11 | 瑞安市四方药化机械有限公司 | Normal temperature evaporation concentrator |
| CN104587690A (en) * | 2015-02-06 | 2015-05-06 | 江阴市江中设备制造有限公司 | Low temperature concentration system |
| CN105381618A (en) * | 2015-12-01 | 2016-03-09 | 浙江凯迪药化机械有限公司 | Low temperature separation and concentration device |
| CN106730944A (en) * | 2017-01-18 | 2017-05-31 | 浙江天联机械有限公司 | From source formula heat pump inspissator |
| CN107213660A (en) * | 2017-07-22 | 2017-09-29 | 黑龙江大三源乳品机械有限公司 | Low temperature concentration and evaporation system |
| CN110755862A (en) * | 2019-11-25 | 2020-02-07 | 湖南安化芙蓉山茶业有限责任公司 | Vacuum concentration device and energy-saving efficient tea juice concentration system |
| CN111544908A (en) * | 2019-02-12 | 2020-08-18 | 义铠科技股份有限公司 | Energy-saving concentration system |
-
2011
- 2011-01-22 CN CN2011200217763U patent/CN201921534U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102500115A (en) * | 2011-10-21 | 2012-06-20 | 上海亿华科技有限公司 | Energy-conservation evaporating plant of liquid-distributing ring type compressor |
| CN102553275A (en) * | 2012-03-16 | 2012-07-11 | 瑞安市四方药化机械有限公司 | Normal temperature evaporation concentrator |
| CN104587690A (en) * | 2015-02-06 | 2015-05-06 | 江阴市江中设备制造有限公司 | Low temperature concentration system |
| CN104587690B (en) * | 2015-02-06 | 2016-01-27 | 江阴市江中设备制造有限公司 | A kind of low temperature concentration systems |
| CN105381618A (en) * | 2015-12-01 | 2016-03-09 | 浙江凯迪药化机械有限公司 | Low temperature separation and concentration device |
| CN106730944A (en) * | 2017-01-18 | 2017-05-31 | 浙江天联机械有限公司 | From source formula heat pump inspissator |
| CN107213660A (en) * | 2017-07-22 | 2017-09-29 | 黑龙江大三源乳品机械有限公司 | Low temperature concentration and evaporation system |
| CN111544908A (en) * | 2019-02-12 | 2020-08-18 | 义铠科技股份有限公司 | Energy-saving concentration system |
| CN111544908B (en) * | 2019-02-12 | 2022-03-04 | 义铠科技股份有限公司 | Energy-saving concentration system |
| CN110755862A (en) * | 2019-11-25 | 2020-02-07 | 湖南安化芙蓉山茶业有限责任公司 | Vacuum concentration device and energy-saving efficient tea juice concentration system |
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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: 20110810 Termination date: 20140122 |