CN203954703U - A kind of MVR evaporation concentration equipment for organic solvent evaporation industry - Google Patents
A kind of MVR evaporation concentration equipment for organic solvent evaporation industry Download PDFInfo
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- CN203954703U CN203954703U CN201420320321.5U CN201420320321U CN203954703U CN 203954703 U CN203954703 U CN 203954703U CN 201420320321 U CN201420320321 U CN 201420320321U CN 203954703 U CN203954703 U CN 203954703U
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- evaporimeter
- organic solvent
- water
- separator
- concentration equipment
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- 239000003960 organic solvent Substances 0.000 title claims abstract description 21
- 238000001704 evaporation Methods 0.000 title claims abstract description 15
- 238000000935 solvent evaporation Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000008234 soft water Substances 0.000 claims abstract description 23
- 238000007906 compression Methods 0.000 claims abstract description 17
- 239000005416 organic matter Substances 0.000 claims abstract description 17
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 230000005494 condensation Effects 0.000 claims abstract description 4
- 238000009833 condensation Methods 0.000 claims abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 4
- 241000282376 Panthera tigris Species 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 238000005039 chemical industry Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Abstract
The utility model relates to a kind of MVR evaporation concentration equipment, relate in particular to a kind of MVR evaporation concentration equipment for organic solvent evaporation industry, comprise centrifugal vapour compression machine, be connected to organic matter evaporimeter and separator, soft water evaporimeter, discharging pump, water tank and the PLC switch board of this compressor two-port.The beneficial effects of the utility model have been to provide a set of complete MVR evaporation concentration equipment for organic solvent evaporation industry, and by the water heat exchange in organic steam and soft water evaporimeter, the water after being heated enters separator, becomes indirect steam; Both save condensation water, reduced again energy consumption.
Description
Technical field
The utility model relates to a kind of MVR evaporation concentration equipment, relates in particular to a kind of MVR evaporation concentration equipment for organic solvent evaporation industry.
Background technology
MVR evaporimeter is the abbreviation of English (Mechanical Vapor Recompression), is referred to as " mechanical steam recompression " evaporimeter.MVR is a kind of any steam source that do not need, the mechanical compressor that the energy that can again utilize the indirect steam self producing is power, can reduce the technology that the energy relies on to external world, it is a kind of novel high-efficiency and energy-saving evaporation equipment developing in the world nineteen sixties.As far back as the sixties, Germany and France have successfully been applied to this technology the industries such as chemical industry, pharmacy, papermaking, sewage disposal, desalinization.
The development of World Economics and the blast of population, the contradiction between the limited energy and unlimited use, becomes increasingly conspicuous, and energy problem has become the focus of World Economics contradiction.For China, along with rapid development of economy, energy problem is more outstanding, has become economic development road blocking tiger.Concrete in organic solvent evaporation industry, the energy that evaporates in a large number organic solvent consumption is the important cost in solvent recovery.
Utility model content
The technical problems to be solved in the utility model is: a kind of MVR evaporation concentration equipment for organic solvent evaporation industry is provided.
For solving the problems of the technologies described above, the utility model provides following technical scheme: function of mechanical steam recompression evaporation concentration equipment in a kind of organic solvent evaporation industry, is characterized in that comprising centrifugal vapour compression machine, is connected to organic matter evaporimeter and separator, soft water evaporimeter, discharging pump, water tank and the PLC switch board of this compressor two-port; Described organic matter evaporimeter and soft water evaporimeter interconnect; Soft water evaporimeter is connected with separator; Separator is connected with centrifugal vapour compression machine again; Described centrifugal vapour compression machine, evaporimeter, separator are connected with PLC switch board and are all controlled; Water tank is connected with organic matter evaporimeter, and water tank is connected with soft water evaporimeter again; Intermediate water steam in described separator enters centrifugal vapour compression machine, and through the saturated vapours of centrifugal vapour compression machine boil down to, vapours enters organic matter evaporimeter, with organic solvent heat exchange, becomes condensed water and enters water tank; Organic solvent in organic matter evaporimeter is heated and becomes organic vapor and enter soft water evaporimeter, the water heat exchange in organic vapor and soft water evaporimeter, and the water after being heated enters separator, becomes indirect steam; Soft water base of evaporator is connected to discharging pump, and the organic solvent of condensation is extracted out.
The beneficial effects of the utility model have been to provide a set of complete MVR evaporation concentration equipment for organic solvent evaporation industry, have advantages of as follows: 1. low energy consumption, low operating cost; 2. floor space is little; 3. public work is supporting few; 4. operate steadily, automaticity is high; 5. without primary steam; 6. can, 40 ℃ of following evaporations, be particularly suitable for heat sensitive material; 7. by the water heat exchange in organic steam and soft water evaporimeter, the water after being heated enters separator, becomes indirect steam; Success is the evaporation and concentration for organic solvent by MVR technology.
Accompanying drawing explanation
Fig. 1 is the structural representation of the specific embodiment of middle function of mechanical steam recompression evaporation concentration equipment in the utility model organic solvent evaporation industry.
Reference numeral: 1. centrifugal vapour compression machine; 2. organic matter evaporimeter; 3. separator; 4. soft water evaporimeter; 5. discharging pump; 6. water tank.
The specific embodiment
Fig. 1 has shown function of mechanical steam recompression evaporation concentration equipment in a kind of organic solvent evaporation industry of the utility model, it is characterized in that comprising centrifugal vapour compression machine 1, is connected to organic matter evaporimeter 2 and separator 3, soft water evaporimeter 4, discharging pump 5, water tank 6 and the PLC switch board of this compressor two-port; Described organic matter evaporimeter 2 and soft water evaporimeter 4 interconnect; Soft water evaporimeter 4 is connected with separator 3; Separator 3 is connected with centrifugal vapour compression machine 1 again; Described centrifugal vapour compression machine 1, organic matter evaporimeter 2, separator 3 are connected with PLC switch board and are all controlled; Water tank 6 is connected with organic matter evaporimeter 2, and water tank 6 is connected with soft water evaporimeter 4 again; Intermediate water steam in described separator 3 enters centrifugal vapour compression machine 1, and through the saturated vapours of centrifugal vapour compression machine 1 boil down to, vapours enters organic matter evaporimeter 2, with organic solvent heat exchange, becomes condensed water and enters water tank 6; Organic solvent in organic matter evaporimeter 2 is heated and becomes organic vapor and enter soft water evaporimeter 4, the water heat exchange in organic vapor and soft water evaporimeter 4, and the water after being heated enters separator 3, becomes indirect steam; Soft water evaporimeter 4 bottoms are connected to discharging pump, and the organic solvent of condensation is extracted out.
Centrifugal vapour compression machine is 5 ton of 10 centrifugal vapour compression machine of degree type that Lianyang Dewei Touping Machine Co., Ltd. produces; PLC switch board is produced by Lianyang Dewei Touping Machine Co., Ltd. equally.
More than show and only described principal character of the present utility model and main points.Those skilled in the art should understand, and the utility model is not restricted to the described embodiments.Do not departing under the prerequisite of inventive point and protection domain, the utility model also has various variations, and these changes and improvements all will fall in the claimed scope of the utility model.
Claims (1)
1. a function of mechanical steam recompression evaporation concentration equipment in organic solvent evaporation industry, is characterized in that comprising centrifugal vapour compression machine (1), is connected to organic matter evaporimeter (2) and separator (3), soft water evaporimeter (4), discharging pump (5), water tank (6) and the PLC switch board of this compressor two-port; Described organic matter evaporimeter (2) and soft water evaporimeter (4) interconnect; Soft water evaporimeter (4) is connected with separator (3); Separator (3) is connected with centrifugal vapour compression machine (1) again; Described centrifugal vapour compression machine (1), organic matter evaporimeter (2), separator (3) are connected with PLC switch board and are all controlled; Water tank (6) is connected with organic matter evaporimeter (2), and water tank (6) is connected with soft water evaporimeter (4) again; Soft water evaporimeter (4) bottom is connected to discharging pump, and the organic solvent of condensation is extracted out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420320321.5U CN203954703U (en) | 2014-06-16 | 2014-06-16 | A kind of MVR evaporation concentration equipment for organic solvent evaporation industry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420320321.5U CN203954703U (en) | 2014-06-16 | 2014-06-16 | A kind of MVR evaporation concentration equipment for organic solvent evaporation industry |
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| Publication Number | Publication Date |
|---|---|
| CN203954703U true CN203954703U (en) | 2014-11-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420320321.5U Active CN203954703U (en) | 2014-06-16 | 2014-06-16 | A kind of MVR evaporation concentration equipment for organic solvent evaporation industry |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104958917A (en) * | 2015-06-01 | 2015-10-07 | 杜明生 | Air medium preheating starting MVR evaporation system |
| CN105363227A (en) * | 2015-12-02 | 2016-03-02 | 中国科学院理化技术研究所 | Mechanical vapor recompression system and mechanical vapor recompression method based on system |
| CN105854339A (en) * | 2016-05-12 | 2016-08-17 | 江阴市江中设备制造有限公司 | MVR (mechanical vapor recompression) evaporative crystallizer with scale removing and preventing functions |
| CN106237642A (en) * | 2015-06-04 | 2016-12-21 | 河北化大科技有限公司 | A kind of industrial process saves the technology of energy consumption |
| WO2020095132A1 (en) * | 2018-10-30 | 2020-05-14 | Thermax Limited | A thermal evaporation system for seprating solute from a solute-solvent mixture |
-
2014
- 2014-06-16 CN CN201420320321.5U patent/CN203954703U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104958917A (en) * | 2015-06-01 | 2015-10-07 | 杜明生 | Air medium preheating starting MVR evaporation system |
| CN104958917B (en) * | 2015-06-01 | 2018-10-30 | 杜明生 | Air dielectric pipeline start up by preheating MVR vapo(u)rization systems |
| CN106237642A (en) * | 2015-06-04 | 2016-12-21 | 河北化大科技有限公司 | A kind of industrial process saves the technology of energy consumption |
| CN105363227A (en) * | 2015-12-02 | 2016-03-02 | 中国科学院理化技术研究所 | Mechanical vapor recompression system and mechanical vapor recompression method based on system |
| CN105854339A (en) * | 2016-05-12 | 2016-08-17 | 江阴市江中设备制造有限公司 | MVR (mechanical vapor recompression) evaporative crystallizer with scale removing and preventing functions |
| WO2020095132A1 (en) * | 2018-10-30 | 2020-05-14 | Thermax Limited | A thermal evaporation system for seprating solute from a solute-solvent mixture |
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