CN207950689U - Thermo-compression evaporation concentrator - Google Patents
Thermo-compression evaporation concentrator Download PDFInfo
- Publication number
- CN207950689U CN207950689U CN201820152550.9U CN201820152550U CN207950689U CN 207950689 U CN207950689 U CN 207950689U CN 201820152550 U CN201820152550 U CN 201820152550U CN 207950689 U CN207950689 U CN 207950689U
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- Prior art keywords
- evaporator
- economizer
- thermo
- condenser
- utility
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- 238000001704 evaporation Methods 0.000 title claims abstract description 30
- 230000008020 evaporation Effects 0.000 title claims abstract description 25
- 238000007906 compression Methods 0.000 title claims abstract description 18
- 239000000463 material Substances 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 12
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 239000002918 waste heat Substances 0.000 abstract description 5
- 238000001816 cooling Methods 0.000 abstract description 4
- 238000010792 warming Methods 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000010687 lubricating oil Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides thermo-compression evaporation concentrator, including evaporator, knockout drum, economizer, condenser and freon compressore, the freon compressore is connected with the evaporator, the knockout drum is connected with the evaporator and economizer respectively, the economizer is connected with the condenser, the condenser side is additionally provided with a vacuum pump, the utility model utilizes the cooling and warming principle of heat pump, the waste heat generated in recyclable evaporation process reduces the energy consumption in evaporating concentration process.
Description
Technical field
The utility model is related to efficient concentration fields, and in particular to arrive thermo-compression evaporation concentrator.
Background technology
Currently, the production technologies such as chemical industry generate a small amount of high pollution water daily, high pollution water contains heavy metal, and salinity is high
Pollute sexual element.It is unable to reach discharge standard by water treatment technology.In machinery production industry, will produce daily a large amount of discarded
Lubricating oil when lubricating oil is by filtering reuse, due to containing moisture content in lubricating oil, reduces lubricants performance, reuse lubricating oil is past
Toward there are quality problems.
Utility model content
For the prior art there are above-mentioned deficiency, the utility model provides thermo-compression evaporation concentrator, utilizes heat pump
Cooling and warming principle, the waste heat generated in recyclable evaporation process reduces the energy consumption in evaporating concentration process.
The technical solution of the utility model is thermo-compression evaporation concentrator, including evaporator, knockout drum, economizer,
Condenser and freon compressore, the freon compressore are connected with the evaporator, the knockout drum respectively with institute
It states evaporator with economizer to be connected, the economizer is connected with the condenser, and the condenser side is additionally provided with a vacuum
Pump.
Above-mentioned thermo-compression evaporation concentrator, wherein the feed inlet of the economizer is connected with material, for material
Preheating, discharge port are connected with evaporator, and the air inlet of the evaporator is connected with the freon compressore, adds to material
Heat.
Above-mentioned thermo-compression evaporation concentrator, wherein the feed inlet phase of the discharge port of the evaporator and knockout drum
Even, material is evaporated, the material after the knockout drum separation is connected with the evaporation feed liquor mouth.
Above-mentioned thermo-compression evaporation concentrator, wherein the air inlet of steam and economizer that the knockout drum is isolated
Mouth is connected.
Above-mentioned thermo-compression evaporation concentrator, wherein the gas outlet of the economizer is connected with the condenser.
Thermo-compression evaporation concentrator provided by the utility model has the advantages that：1, the cooling and warming of heat pump is utilized
Principle, the waste heat generated in recyclable evaporation process reduce the energy consumption in evaporating concentration process.
Description of the drawings
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, the utility model and its spy
Sign, shape and advantage will become more apparent upon.Identical label indicates identical part in whole attached drawings.Not deliberately according to
Ratio draws attached drawing, it is preferred that emphasis is shows the purport of the utility model.
Fig. 1 is the structural schematic diagram of thermo-compression evaporation concentrator provided by the utility model；
Specific implementation mode
In the following description, a large amount of concrete details are given more thoroughly to manage in order to provide to the utility model
Solution.It is, however, obvious to a person skilled in the art that the utility model may not need it is one or more of these thin
It saves and is carried out.In other examples, in order to avoid obscuring with the utility model, for more well known in the art
Technical characteristic is not described.
In order to thoroughly understand the utility model, detailed step and detailed structure will be proposed in following description,
To illustrate the technical solution of the utility model.The preferred embodiment of the utility model is described in detail as follows, however in addition to these
Detailed description is outer, and the utility model can also have other embodiment.
Shown in referring to Fig.1, the utility model provides thermo-compression evaporation concentrator, including evaporator 1, knockout drum 2,
Economizer 3, condenser 4 and freon compressore 5, freon compressore 5 are connected with evaporator 1, knockout drum 2 respectively with steaming
Hair device 1 is connected with economizer 3, and economizer 3 is connected with condenser 4, and 4 side of condenser is additionally provided with a vacuum pump 6.This practicality is new
The operation principle of type is：Material into evaporator 1, is added after the preheating of economizer 3 by the exhaust of freon compressore 5
Heat, meanwhile, exhaust condensation in evaporator 1 of freon compressore 5.Material after being heated in evaporator 1 is in gas-liquid point
From being detached in tank 2, the material after gas-liquid separation enters back into circulating-heating in evaporator 1 and evaporates, until reaching the dense of setting
Degree, the steam that knockout drum 2 is isolated, which enters in economizer 3, preheats material, enters back into condenser 4, condensed
Condensed water is discharged in water discharge system 9.Vacuum pump 6 is to maintain the negative pressure state of system, to ensure that material can be in system
It being evaporated at lower temperature, the utility model utilizes the cooling and warming principle of heat pump, the waste heat generated in recyclable evaporation process,
Reduce the energy consumption in evaporating concentration process.
Shown in referring to Fig.1,3 one end of economizer is connected with an inlet valve 7, and 1 lower end of evaporator is connected with an outlet valve 8, uses
It is excluded in the material after concentration.
In the utility model one in preferred but unrestricted embodiment, the feed inlet of economizer 3 is connected with material, for pair
The preheating of material, discharge port are connected with evaporator 1, and the air inlet of evaporator 1 is connected with freon compressore 5, are carried out to material
Heating.
In the utility model one in preferred but unrestricted embodiment, the discharge port of evaporator 1 and knockout drum 2 into
Material mouth is connected, and is evaporated to material, and the material after knockout drum 2 detaches is connected with 1 feed inlet of the evaporator, carries out again
Secondary concentration.
In the utility model one in preferred but unrestricted embodiment, steam and economizer 3 that knockout drum 2 is isolated
Air inlet be connected, for preheating to material.The gas outlet of economizer 3 is connected with the condenser.The utility model utilizes
The waste heat generated in recyclable evaporation process can reduce the energy consumption in evaporating concentration process.
The preferred embodiment of the utility model is described above.It is to be appreciated that the utility model not office
It is limited to above-mentioned particular implementation, wherein the equipment and structure be not described in detail to the greatest extent are construed as with the common side in this field
Formula is practiced；Any technical person familiar with the field all may be used in the case where not departing from technical solutions of the utility model ambit
Many possible changes and modifications are made to technical solutions of the utility model using the methods and technical content of the disclosure above, or are repaiied
It is changed to the equivalent embodiment of equivalent variations, this has no effect on the substantive content of the utility model.Therefore, every without departing from this practicality
The content of new technique scheme, any simple modification made to the above embodiment of foundation the technical essence of the utility model, etc.
With variation and modification, still fall within technical solutions of the utility model protection in the range of.
Claims (5)
1. thermo-compression evaporation concentrator, which is characterized in that including evaporator, knockout drum, economizer, condenser and freon
Compressor, the freon compressore are connected with the evaporator, the knockout drum respectively with the evaporator and economy
Device is connected, and the economizer is connected with the condenser, and the condenser side is additionally provided with a vacuum pump.
2. thermo-compression evaporation concentrator as described in claim 1, which is characterized in that the feed inlet of the economizer and material phase
Even, for the preheating to material, discharge port is connected with evaporator, the air inlet of the evaporator and the freon compressore phase
Even, material is heated.
3. thermo-compression evaporation concentrator as claimed in claim 2, which is characterized in that the discharge port of the evaporator and gas-liquid point
Feed inlet from tank is connected, and is evaporated to material, the material after the knockout drum separation and the evaporation feed liquor mouth
It is connected.
4. thermo-compression evaporation concentrator as claimed in claim 3, which is characterized in that the steam that the knockout drum is isolated
It is connected with the air inlet of economizer.
5. thermo-compression evaporation concentrator as claimed in claim 4, which is characterized in that the gas outlet of the economizer with it is described cold
Condenser is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820152550.9U CN207950689U (en) | 2018-01-30 | 2018-01-30 | Thermo-compression evaporation concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820152550.9U CN207950689U (en) | 2018-01-30 | 2018-01-30 | Thermo-compression evaporation concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207950689U true CN207950689U (en) | 2018-10-12 |
Family
ID=63735914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820152550.9U Expired - Fee Related CN207950689U (en) | 2018-01-30 | 2018-01-30 | Thermo-compression evaporation concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207950689U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237553A (en) * | 2019-05-28 | 2019-09-17 | 上海环球制冷设备有限公司 | A kind of solution condensing device and its implementation |
| CN111111239A (en) * | 2020-01-15 | 2020-05-08 | 上海敏杰制药机械有限公司 | Energy-saving heat pump evaporation concentration automatic control system |
| CN111470483A (en) * | 2020-06-05 | 2020-07-31 | 于龙 | Utilize freon to concentrate system as cold and hot carrier's nitric acid |
-
2018
- 2018-01-30 CN CN201820152550.9U patent/CN207950689U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237553A (en) * | 2019-05-28 | 2019-09-17 | 上海环球制冷设备有限公司 | A kind of solution condensing device and its implementation |
| CN111111239A (en) * | 2020-01-15 | 2020-05-08 | 上海敏杰制药机械有限公司 | Energy-saving heat pump evaporation concentration automatic control system |
| CN111470483A (en) * | 2020-06-05 | 2020-07-31 | 于龙 | Utilize freon to concentrate system as cold and hot carrier's nitric acid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220907 Address after: Room 408, Building 8, China Textile City Cross-border E-commerce Industrial Park, Huashe Street, Keqiao District, Shaoxing City, Zhejiang Province Patentee after: Zhejiang Retuo Energy Saving Technology Co.,Ltd. Address before: Room 562, No. 1, Lane 202, Maosheng Road, Dongjing Town, Songjiang District, Shanghai, 201619 Patentee before: SHANGHAI MERIT ENERGY TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181012 |
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| CF01 | Termination of patent right due to non-payment of annual fee |