CN111285422A - Integrated form MVR evaporation concentration device - Google Patents
Integrated form MVR evaporation concentration device Download PDFInfo
- Publication number
- CN111285422A CN111285422A CN202010094085.XA CN202010094085A CN111285422A CN 111285422 A CN111285422 A CN 111285422A CN 202010094085 A CN202010094085 A CN 202010094085A CN 111285422 A CN111285422 A CN 111285422A
- Authority
- CN
- China
- Prior art keywords
- cavity
- raw material
- water
- heat exchange
- separator
- 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.)
- Granted
Links
- 238000001704 evaporation Methods 0.000 title claims abstract description 13
- 230000008020 evaporation Effects 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 102
- 239000002994 raw material Substances 0.000 claims abstract description 43
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 239000012141 concentrate Substances 0.000 claims abstract description 7
- 239000011552 falling film Substances 0.000 claims description 4
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 239000013589 supplement Substances 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 6
- 238000004065 wastewater treatment Methods 0.000 description 3
- 238000005485 electric heating Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention provides an integrated MVR evaporation concentration device, which comprises a device shell, wherein the lower end of the device shell is provided with a booster pump, the booster pump is arranged in a raw material water cavity, heated raw material water is pumped into a separator cavity, a heat exchange tube cavity is connected with the raw material water cavity and the separator cavity, and two ends of a heat exchange tube are respectively connected with the separator cavity and the raw material water cavity and are used for evaporation heat exchange and partial raw material liquid backflow; the compressor is installed to device casing upper end, and the steam pressure boost that produces in the compressor will the separator, and the exhaust passage through setting up in the device casing gets into the heat transfer lumen, and the comdenstion water after the heat transfer passes through comdenstion water channel and gets into the comdenstion water chamber, sets up the comdenstion water export in the comdenstion water chamber, and the raw materials water chamber sets up the concentrate export. The invention supplements the heat loss of the system with auxiliary heating, has no external pipeline connection, and realizes the microminiaturization of the MVR system; the booster pump has low power consumption and high heat transfer efficiency; the heat exchange area is low, and the heat exchange efficiency in the evaporation-condenser is high; fully retrieves the comdenstion water heat, and the system is efficient.
Description
Technical Field
The invention relates to an integrated MVR evaporation and concentration device, and belongs to the technical field of wastewater treatment.
Background
The industrial salt-containing wastewater is mainly treated by a membrane method and an evaporation method, the membrane method is not suitable for treating the high salt-containing wastewater, the multi-effect evaporation system has high energy consumption, and a Mechanical Vapor Recompression (MVR) system is a main technical means for solving the problem at present. The MVR system comprises an evaporation-condenser, a compressor, a pump and other components, and can directly concentrate and purify waste water (sewage enters, clean water and concentrated solution exits).
For MVR systems in the fields of industrial wastewater treatment, material concentration and the like, the treatment capacity is generally more than 0.5t/h, a centrifugal compressor or a screw compressor is adopted, so that the occupied area of equipment is large, wherein the equipment such as the compressor, a heat exchanger, a pump and the like are connected by pipeline valves, the structural integration degree is low, the heat loss of a pipeline is large, the MVR system is not suitable for the treatment of micro-flow wastewater and environments with high requirements on installation space, and the MVR system cannot meet the requirements in the treatment of micro-flow wastewater in machine tool wastewater, electroplating workshops and the like. Therefore, compactness and high efficiency are the problems faced by the MVR system, and an MVR device with high integration level and compact structure is urgently needed in the micro-flow wastewater treatment.
Disclosure of Invention
In order to overcome the problems, the invention provides an integrated MVR evaporation concentration device, provides an integrated compact structure and solves the technical problem that an MVR system cannot be miniaturized.
In order to solve the problems in the prior art, the invention adopts the technical scheme that: an integrated MVR evaporation concentration device comprises a device shell, wherein a booster pump is arranged at the lower end of the device shell, the booster pump is arranged in a raw material water cavity, heated raw material water is pumped into a separator cavity, a heat exchange tube cavity is connected with the raw material water cavity and the separator cavity, and two ends of a heat exchange tube are respectively connected with the separator cavity and the raw material water cavity and are used for evaporation heat exchange and partial raw material liquid backflow; the compressor is installed to device casing upper end, and the steam pressure boost that produces in the compressor will the separator, and the exhaust passage through setting up in the device casing gets into the heat transfer lumen, and the comdenstion water after the heat transfer passes through comdenstion water channel and gets into the comdenstion water chamber, sets up the comdenstion water export in the comdenstion water chamber, and the raw materials water chamber sets up the concentrate export.
Furthermore, the comdenstion water chamber encircles outside the raw materials water chamber, and the inlet tube penetrates the comdenstion water chamber wall and is located this cavity, and coils the preheating coil connection outside the raw materials water chamber, and the water inlet in raw materials water chamber is connected to the other end of preheating coil, and comdenstion water chamber upper end is through comdenstion water wash port and heat transfer lumen intercommunication.
Furthermore, the compressor is installed in the exhaust chamber, the compressor is connected with a compressor motor located outside the exhaust chamber, a demister is arranged between the compressor and the separator cavity, the exhaust chamber is arranged around the separator cavity, the exhaust chamber is communicated with one end of the exhaust chamber through an exhaust through hole, and the other end of the exhaust chamber is communicated with the heat exchange tube cavity through a heat exchange through hole.
Furthermore, the booster pump is connected with a booster pump motor positioned outside the raw material water cavity.
Further, an electric heater is arranged in the raw material water cavity.
Furthermore, the booster pump is connected with a falling film type liquid lifting pipe penetrating through the heat exchange pipe cavity, and heated raw material water is pumped into the separator cavity through the liquid lifting pipe.
The beneficial technical effects of the invention are as follows: the integrated structure of the compressor, the evaporation-condenser and the circulating pump is adopted, and external pipelines are not needed to be connected among the devices, so that the microminiaturization of the MVR system is realized; a falling film type liquid lifting pipe is adopted in the middle of the evaporator and the condenser, so that the power consumption of the pump can be reduced, and the heat transfer efficiency is improved; the exhaust passage chamber reduces the superheat degree of steam at the outlet of the compressor, improves the heat exchange efficiency in the evaporation-condenser and reduces the heat exchange area; a preheating coil is arranged in the condensed water chamber, raw water enters the raw water cavity after passing through the preheating coil, the heat of the condensed water is fully recovered, and the system efficiency is improved; and an electric heating aid is arranged for preheating the system during starting to supplement the heat loss of the system.
Drawings
The technical solution of the present invention is described in detail below with reference to the accompanying drawings.
FIG. 1 is a schematic structural view of the present invention;
in the figure: 1. the device comprises a water inlet pipe, 2, a condensate water drain hole, 3, a liquid lifting pipe, 4, a heat exchange pipe cavity, 5, a separator cavity, 6, a demister, 7, a compressor, 8, a compressor motor, 9, an exhaust chamber, 10, an exhaust through hole, 11, an exhaust passage chamber, 12, a heat exchange through hole, 13, a condensate water cavity, 14, a condensate water outlet, 15, a concentrate outlet, 16, a booster pump motor, 17, a booster pump, 18, a raw material water cavity, 19, an electric heater, 20 and a preheating coil pipe.
Detailed Description
As shown in fig. 1, the integrated MVR evaporation concentration device comprises a device shell, wherein a booster pump 17 is installed at the lower end of the device shell, the booster pump 17 is installed in a raw material water cavity 18, heated raw material water is pumped into a separator cavity 5, a heat exchange tube cavity 4 is connected with the raw material water cavity 18 and the separator cavity 5, and two ends of a heat exchange tube are respectively connected with the separator cavity 18 and the raw material water cavity 5 and used for heat exchange reflux; the compressor 7 is installed at the upper end of the device shell, the compressor 7 pressurizes steam generated in the separator, the steam enters the heat exchange tube cavity 4 through an exhaust passage arranged in the device shell, condensed water of heat exchange enters the condensed water cavity 13 through the condensed water passage, a condensed water outlet 14 is arranged in the condensed water cavity 13, and a concentrated solution outlet 15 is arranged in the raw material water cavity 18.
As a preferred design, the condensed water cavity 13 surrounds the raw material water cavity 18, the water inlet pipe 1 penetrates through the wall of the condensed water cavity and is positioned in the cavity, the preheating coil 20 wound outside the raw material water cavity is connected, the other end of the preheating coil 20 is connected with the water inlet of the raw material water cavity 18, and the upper end of the condensed water cavity 13 is communicated with the heat exchange pipe cavity 4 through the condensed water drain hole 2.
As a preferable design, the compressor 7 is arranged in the exhaust chamber 9, the compressor 7 is connected with a compressor motor 8 positioned outside the exhaust chamber, a demister 6 is arranged between the compressor 7 and the separator cavity 5, an exhaust chamber 11 is arranged outside the separator cavity 5 in a surrounding manner, the exhaust chamber 9 is communicated with one end of the exhaust chamber 11 through an exhaust through hole 10, and the other end of the exhaust chamber 11 is communicated with the heat exchange tube cavity 4 through a heat exchange through hole 12.
As a preferable design, the booster pump 17 is connected with a booster pump motor 16 which is positioned outside the raw water cavity.
In a preferred design, an electric heater 19 is arranged in the raw water cavity 18.
In a preferred design, the booster pump 17 is connected to the lift tube 3 extending through the heat exchange tube chamber 4, and the heated raw water is pumped into the separator chamber 5 through the lift tube 3.
Raw material water enters the raw material water cavity 18 from the water inlet pipe 1 after passing through the preheating coil 20, enters the separator cavity 5 along the liquid lifting pipe 3 after being pressurized by the booster pump 17, and returns to the raw material water cavity 18 along the heat exchange pipe after being uniformly distributed. Steam generated in the separator cavity 5 enters the compressor 7 after foam is removed by the foam remover 6, high-temperature and high-pressure steam obtained after pressurization by the compressor 7 enters the exhaust passage chamber 11 through the exhaust through hole 10, then enters the heat exchange tube cavity 4 through the heat exchange through hole 12 and heats raw material water in the heat exchange tube, and condensed water obtained after heat exchange enters the condensed water cavity 13 along the condensed water drain hole 2 and then is discharged out of the device through the condensed water outlet 14. The concentrate produced at the bottom of the feed water chamber exits the apparatus through a concentrate outlet 15. The exhaust chamber 11 recovers the exhaust heat of the compressor, reduces the superheat degree of steam entering the outer side of the heat exchange tube, improves the heat exchange efficiency, reduces the size of an evaporation-condenser, and the preheating coil 20 recovers the condensed water heat in the condensed water cavity 13 for preheating raw water.
Compared with the prior art, the invention has the following characteristics:
1. the invention adopts the integrated structure of the compressor, the evaporation-condenser, the circulating pump and the like, and the equipment does not need to be connected by an external pipeline, thereby realizing the microminiaturization of the MVR system.
2. The falling film type liquid lifting pipe is adopted in the middle of the evaporator and the condenser, so that the power consumption of the pump can be reduced, and the heat transfer efficiency is improved.
3. The exhaust passage chamber is arranged for reducing the superheat degree of steam at the outlet of the compressor, improving the heat exchange efficiency in the evaporation-condenser and reducing the heat exchange area.
4. The preheating coil is arranged in the condensed water chamber, raw water enters the raw water cavity after passing through the preheating coil, the heat of the condensed water is fully recovered, and the system efficiency is improved.
5. The electric heating is arranged for assisting in preheating the system during starting, and the heat loss of the system can be supplemented.
The above description is only for the specific embodiments of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and the technical solutions and their concepts should be equivalent or changed within the technical scope of the present invention.
Claims (6)
1. An integrated form MVR evaporation concentration device, includes the device casing, its characterized in that: the lower end of the device shell is provided with a booster pump, the booster pump is arranged in a raw material water cavity, heated raw material water is pumped into a separator cavity, a heat exchange tube cavity is connected with the raw material water cavity and the separator cavity, and two ends of a heat exchange tube are respectively connected with the separator cavity and the raw material water cavity and are used for evaporation heat exchange and partial raw material liquid backflow; the compressor is installed to device casing upper end, and the steam pressure boost that produces in the compressor will the separator, and the exhaust passage through setting up in the device casing gets into the heat transfer lumen, and the comdenstion water after the heat transfer passes through comdenstion water channel and gets into the comdenstion water chamber, sets up the comdenstion water export in the comdenstion water chamber, and the raw materials water chamber sets up the concentrate export.
2. The integrated MVR evaporative concentration device of claim 1, wherein: the condensed water cavity surrounds the raw material water cavity, the water inlet pipe penetrates through the condensed water cavity wall and is located in the condensed water cavity, the condensed water cavity is coiled outside the raw material water cavity and is connected with the preheating coil, the other end of the preheating coil is connected with the water inlet of the raw material water cavity, and the upper end of the condensed water cavity is communicated with the heat exchange cavity through a condensed water drain hole.
3. The integrated MVR evaporative concentration device of claim 1, wherein: the compressor is installed in the exhaust chamber, the compressor is connected with a compressor motor located outside the exhaust chamber, a demister is arranged between the compressor and the separator cavity, an exhaust chamber is arranged around the separator cavity, the exhaust chamber is communicated with one end of the exhaust chamber through an exhaust through hole, and the other end of the exhaust chamber is communicated with the heat exchange tube cavity through a heat exchange through hole.
4. The integrated MVR evaporative concentration device of claim 1, wherein: the booster pump is connected with a booster pump motor positioned outside the raw material water cavity.
5. The integrated MVR evaporative concentration device of claim 1, wherein: an electric heater is arranged in the raw material water cavity.
6. The integrated MVR evaporative concentration device of claim 1, wherein: the booster pump is connected with a falling film type liquid lifting pipe penetrating through the heat exchange pipe cavity, and heated raw material water is pumped into the separator cavity through the liquid lifting pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010094085.XA CN111285422B (en) | 2020-02-15 | 2020-02-15 | Integrated form MVR evaporation concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010094085.XA CN111285422B (en) | 2020-02-15 | 2020-02-15 | Integrated form MVR evaporation concentration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111285422A true CN111285422A (en) | 2020-06-16 |
| CN111285422B CN111285422B (en) | 2022-04-12 |
Family
ID=71017958
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010094085.XA Active CN111285422B (en) | 2020-02-15 | 2020-02-15 | Integrated form MVR evaporation concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111285422B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113262512A (en) * | 2021-07-06 | 2021-08-17 | 山东意威尔环境科技有限公司 | Disc type film distribution evaporator |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09173047A (en) * | 1995-12-28 | 1997-07-08 | Satsuma Shuzo Kk | Simplex distillation equipment using steam ejector |
| CN2705219Y (en) * | 2004-05-20 | 2005-06-22 | 淄博华周制药设备有限公司 | Double section type screen separating evaporator |
| CN201978514U (en) * | 2010-04-22 | 2011-09-21 | 姜广义 | Forced reverse circulating evaporator for steam |
| US20120193213A1 (en) * | 2011-01-27 | 2012-08-02 | Kemex Ltd. | Compact Evaporator for Modular Portable SAGD Process |
| CN202777833U (en) * | 2012-01-19 | 2013-03-13 | 重庆远达水务有限公司 | Mechanical vapor recompression evaporator |
| CN102989181A (en) * | 2012-12-17 | 2013-03-27 | 李锦龙 | Compound type monomer multi-effect steam mechanical recompression evaporator |
| KR20150118446A (en) * | 2014-04-14 | 2015-10-22 | 선테코 유한회사 | Distillation system using multi stage stripper capable of integrated operation and reduction of steam consumption |
| CN106582056A (en) * | 2016-12-26 | 2017-04-26 | 江苏乐科节能科技股份有限公司 | Double-stroke forced circulation type heat exchange and crystallization integrated device and working method thereof |
| CN206512053U (en) * | 2017-01-10 | 2017-09-22 | 山东大学 | Based on the organic brine waste processing system for being evaporated in vacuo simultaneous heat energy utilization |
| KR101791621B1 (en) * | 2016-06-30 | 2017-11-20 | 한국해양과학기술원 | Apparatus of membrane distillation desalination and concentrating extraction from seawater using heat pump |
| CN108635900A (en) * | 2018-05-26 | 2018-10-12 | 江苏源拓环境科技有限公司 | A kind of compact micro-pressure-difference push in circulating and evaporating concentration and crystallization apparatus |
| CN207970468U (en) * | 2018-02-11 | 2018-10-16 | 哈尔滨理工大学 | A kind of MVR evaporation concentration systems |
| CN108686393A (en) * | 2018-07-15 | 2018-10-23 | 湖北开元化工科技股份有限公司 | Concentration technology in ammonium sulfate waste water MVR evaporation and crystallization system processing procedures |
| CN109707638A (en) * | 2019-01-30 | 2019-05-03 | 青岛科技大学 | A kind of bearing and seal integrated small miniature centrifugal compressors |
| CN209848345U (en) * | 2019-04-17 | 2019-12-27 | 武汉宏澳绿色能源工程有限责任公司 | Internal circulation falling film evaporator and MVR evaporation system |
-
2020
- 2020-02-15 CN CN202010094085.XA patent/CN111285422B/en active Active
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09173047A (en) * | 1995-12-28 | 1997-07-08 | Satsuma Shuzo Kk | Simplex distillation equipment using steam ejector |
| CN2705219Y (en) * | 2004-05-20 | 2005-06-22 | 淄博华周制药设备有限公司 | Double section type screen separating evaporator |
| CN201978514U (en) * | 2010-04-22 | 2011-09-21 | 姜广义 | Forced reverse circulating evaporator for steam |
| US20120193213A1 (en) * | 2011-01-27 | 2012-08-02 | Kemex Ltd. | Compact Evaporator for Modular Portable SAGD Process |
| CN202777833U (en) * | 2012-01-19 | 2013-03-13 | 重庆远达水务有限公司 | Mechanical vapor recompression evaporator |
| CN102989181A (en) * | 2012-12-17 | 2013-03-27 | 李锦龙 | Compound type monomer multi-effect steam mechanical recompression evaporator |
| KR20150118446A (en) * | 2014-04-14 | 2015-10-22 | 선테코 유한회사 | Distillation system using multi stage stripper capable of integrated operation and reduction of steam consumption |
| KR101791621B1 (en) * | 2016-06-30 | 2017-11-20 | 한국해양과학기술원 | Apparatus of membrane distillation desalination and concentrating extraction from seawater using heat pump |
| CN106582056A (en) * | 2016-12-26 | 2017-04-26 | 江苏乐科节能科技股份有限公司 | Double-stroke forced circulation type heat exchange and crystallization integrated device and working method thereof |
| CN206512053U (en) * | 2017-01-10 | 2017-09-22 | 山东大学 | Based on the organic brine waste processing system for being evaporated in vacuo simultaneous heat energy utilization |
| CN207970468U (en) * | 2018-02-11 | 2018-10-16 | 哈尔滨理工大学 | A kind of MVR evaporation concentration systems |
| CN108635900A (en) * | 2018-05-26 | 2018-10-12 | 江苏源拓环境科技有限公司 | A kind of compact micro-pressure-difference push in circulating and evaporating concentration and crystallization apparatus |
| CN108686393A (en) * | 2018-07-15 | 2018-10-23 | 湖北开元化工科技股份有限公司 | Concentration technology in ammonium sulfate waste water MVR evaporation and crystallization system processing procedures |
| CN109707638A (en) * | 2019-01-30 | 2019-05-03 | 青岛科技大学 | A kind of bearing and seal integrated small miniature centrifugal compressors |
| CN209848345U (en) * | 2019-04-17 | 2019-12-27 | 武汉宏澳绿色能源工程有限责任公司 | Internal circulation falling film evaporator and MVR evaporation system |
Non-Patent Citations (4)
| Title |
|---|
| 王佳琪等: "机械蒸汽再压缩蒸发系统优化设计", 《化工时刊》 * |
| 田素根等: "涡旋压缩机技术研究进展与发展趋势", 《制冷与空调》 * |
| 赵磊: "乳品MVR（机械蒸汽再压缩）蒸发器设计", 《中国优秀博硕士学位论文全文数据库(硕士)工程科技Ⅰ辑》 * |
| 马秉骞: "《化工设备》", 31 August 2004, 化学工业出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113262512A (en) * | 2021-07-06 | 2021-08-17 | 山东意威尔环境科技有限公司 | Disc type film distribution evaporator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111285422B (en) | 2022-04-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102219273B (en) | Solar and thermocompression vapor-compression distillation type water purifying device | |
| CN204384910U (en) | A kind of heat pump waste disposal plant | |
| EA004968B1 (en) | Process and plant for multi-stage desalination of water | |
| CN108751302A (en) | A kind of vacuum and low temperature evaporating separation device and sewage water treatment method | |
| CN109855151B (en) | Geothermal heating system combining absorption heat pump with vacuum flash evaporation | |
| CN103058438B (en) | Hot film coupling seawater desalination system | |
| CN111285422B (en) | Integrated form MVR evaporation concentration device | |
| CN205035108U (en) | A light water condenser for sea water desalination device | |
| CN109095535A (en) | Sewage evaporation enrichment facility and its operating method | |
| CN113697882B (en) | Heat pump water treatment system and working method | |
| JP4139597B2 (en) | Desalination equipment | |
| CN111111451B (en) | Reduced pressure multi-effect membrane distillation method and device thereof | |
| CN209635926U (en) | Falling film evaporation couples absorption refrigeration high-salt sewage processing equipment | |
| CN111747473B (en) | Waste heat and residual pressure energy evaporation concentration equipment and method | |
| CN112919565B (en) | Solar energy-hot spring-heat pump coupling multistage membrane distillation water treatment system and method | |
| CN206430354U (en) | A kind of drinking equipment | |
| JP2024502218A (en) | Separation tower and method for treating condensate | |
| CN210645170U (en) | Double-effect external circulation evaporator | |
| CN1776285A (en) | Method for prevent vibration of water return pipeline for alumina plant | |
| CN111777126A (en) | Device and method for treating salt-containing wastewater by using flue gas waste heat | |
| CN212174496U (en) | Chemical nickel waste liquid treatment equipment | |
| CN216785765U (en) | Heat exchange evaporation industrial sewage treatment system with efficient cyclic concentration | |
| CN108529806A (en) | A kind of reverse osmosis concentrated water zero discharge low energy consumption device of coking wastewater and processing method | |
| CN216203272U (en) | Device for heating reverse osmosis inlet water temperature by using continuous sewage discharge of boiler | |
| CN219283302U (en) | Periodic sewage heat recovery device for drum boiler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |