CN203724789U - MVR (mechanical vapor recompression) evaporation system - Google Patents
MVR (mechanical vapor recompression) evaporation system Download PDFInfo
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- CN203724789U CN203724789U CN201420077812.1U CN201420077812U CN203724789U CN 203724789 U CN203724789 U CN 203724789U CN 201420077812 U CN201420077812 U CN 201420077812U CN 203724789 U CN203724789 U CN 203724789U
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Abstract
The utility model discloses an MVR (mechanical vapor recompression) evaporation system which is characterized by comprising a feeding pump, a preheating device, a condensate pump, a condensate tank, a condenser, a compressor, a material circulating pump, an evaporator and a discharging pump, wherein the feeding pump is connected with a first inlet of the condenser through a first outlet of the preheating device; the condensate pump is connected with a first inlet of the evaporator through a first outlet of the condensate tank; an outlet of the condenser is connected with a second inlet of the evaporator through the material circulating pump; a first outlet of the evaporator is connected with the discharging pump; and the compressor is arranged between the condenser and the evaporator and is connected with a second inlet of the condenser and a second outlet of the evaporator respectively. The MVR evaporation system provided by the utility model can reuse secondary steam and can adjust the system pressure ratio.
Description
Technical field
The utility model relates to a kind of MVR vapo(u)rization system.
Background technology
Traditional evaporimeter is as low in single-action or multi-effect evaporator exist the thermal efficiency, power consumption is large, operating cost is high, some row such as waste resource are not enough, but also can produce carbon dioxide, the pernicious gases such as sulfur dioxide, bring a lot of adverse influences to social economy and human development, in addition, MVR system evaporation operating mode is easy to be subject to fluctuate such as feeding temperature, small sample perturbations such as condensed water level variation and departing from of heating cycle occurs, affect it and accurately controlled applying in the evaporation technology process of operating mode at needs, especially at accurate chemical field, as the industry preparation of nanometer silver nitrate, the industrial evaporation of sodium peroxydisulfate etc.
Summary of the invention
In view of the deficiency of background technology, technical problem to be solved in the utility model is to provide and a kind ofly can reuses indirect steam and MVR vapo(u)rization system that can regulating system pressure ratio.
For this reason, the MVR vapo(u)rization system that the utility model provides comprises feed pump, preheating device, condensate pump, condensate draining, condenser, compressor, Matter Transfer pump, evaporimeter and discharging pump, described feed pump is connected with the first entrance of condenser through the first outlet of preheating device, described condensate pump is connected with the first entrance of evaporimeter through the first outlet of condensate draining, the outlet of described condenser is connected with the second entrance of evaporimeter through Matter Transfer pump, the first outlet of described evaporimeter is connected with discharging pump, described compressor is located between condenser and evaporimeter and respectively and is connected with the second entrance of condenser and the second outlet of evaporimeter.
The utility model has the advantages that: the indirect steam that 1, can produce MVR vapo(u)rization system reuses; 2, compressor adopts high temperature water spray and two kinds of water spray modes of low temperature water spray, has regulated water-spraying evaporation amount in the utilization that has ensured condensation water residual heat, regulates thus the actual pressure ratio of compressor, reaches and regulates MVR system pressure ratio object.
Brief description of the drawings
The structural representation of the MVR vapo(u)rization system that Fig. 1 provides for the utility model.
Detailed description of the invention
As shown in Figure 1, the MVR vapo(u)rization system that the utility model provides comprises feed pump 1, preheating device 2, condensate pump 3, condensate draining 4, condenser 5, compressor 6, Matter Transfer pump 7, evaporimeter 8 and discharging pump 9, described feed pump 1 is connected with the first entrance 51 of condenser 5 through the first outlet 21 of preheating device 2, described condensate pump 3 is connected with the first entrance 81 of evaporimeter 8 through the first outlet 41 of condensate draining 4, the outlet 52 of described condenser 5 is connected with the second entrance 82 of evaporimeter 8 through Matter Transfer pump 7, the first outlet 83 of described evaporimeter 8 is connected with discharging pump 9, described compressor 6 is located between condenser 5 and evaporimeter 8 and respectively and is connected with the second entrance 53 of condenser 5 and the second outlet 84 of evaporimeter 8, preheating device 2 is provided with the second outlet 22 and low-temp. spraying water pump 10 is passed through in the second outlet 22 successively, the first valve 11 is connected with compressor 6, the second outlet 42 of condensate draining 4 is successively through high-temperature water pump 12, the second valve 13 is connected with compressor 6.
In the present embodiment, when the 8 vapour-liquid temperature difference of evaporimeter in system excessive, illustrative system pressure ratio is excessive, depart from normal pressure ratio, now open the low-temp. spraying water yield that the first valve 11 strengthens compressor 6, the energy that compressor 6 is injected is mainly used in eliminating the degree of supercooling of water spray, and only there is a small amount of water-spraying evaporation, even there is the condensation of part indirect steam, due to compressor 6 exhaust end of a period constancies of volume, but the minimizing of water vapour quality, compression process is insufficient, pressure ratio is less than theoretical pressure ratio, reaches the effect that reduces pressure ratio.Otherwise, in the time that system pressure ratio is too small, open the high temperature injection flow rate of the second valve increase compressor 6, the energy that compressor 6 is injected is mainly used in making water-spraying evaporation, produces more water-spraying evaporation steam, and pressure ratio is greater than theoretical pressure ratio, reaches the effect that improves pressure ratio.
Claims (2)
1. a MVR vapo(u)rization system, it is characterized in that: comprise feed pump, preheating device, condensate pump, condensate draining, condenser, compressor, Matter Transfer pump, evaporimeter and discharging pump, described feed pump is connected with the first entrance of condenser through the first outlet of preheating device, described condensate pump is connected with the first entrance of evaporimeter through the first outlet of condensate draining, the outlet of described condenser is connected with the second entrance of evaporimeter through Matter Transfer pump, the first outlet of described evaporimeter is connected with discharging pump, described compressor is located between condenser and evaporimeter and respectively and is connected with the second entrance of condenser and the second outlet of evaporimeter.
2. MVR vapo(u)rization system according to claim 1, it is characterized in that: described preheating device is provided with the second outlet and the second outlet is connected with compressor through low-temp. spraying water pump, the first valve successively, the second outlet of described condensate draining is connected with compressor through high-temperature water pump, the second valve successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420077812.1U CN203724789U (en) | 2014-02-24 | 2014-02-24 | MVR (mechanical vapor recompression) evaporation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420077812.1U CN203724789U (en) | 2014-02-24 | 2014-02-24 | MVR (mechanical vapor recompression) evaporation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203724789U true CN203724789U (en) | 2014-07-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420077812.1U Expired - Fee Related CN203724789U (en) | 2014-02-24 | 2014-02-24 | MVR (mechanical vapor recompression) evaporation system |
Country Status (1)
| Country | Link |
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| CN (1) | CN203724789U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104707349A (en) * | 2015-02-05 | 2015-06-17 | 中国科学院理化技术研究所 | Plate evaporator type MVR heat pump evaporation system |
| CN106474756A (en) * | 2016-10-13 | 2017-03-08 | 南京创贝高速传动机械有限公司 | A kind of energy-efficient MVR vaporising device |
-
2014
- 2014-02-24 CN CN201420077812.1U patent/CN203724789U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104707349A (en) * | 2015-02-05 | 2015-06-17 | 中国科学院理化技术研究所 | Plate evaporator type MVR heat pump evaporation system |
| CN106474756A (en) * | 2016-10-13 | 2017-03-08 | 南京创贝高速传动机械有限公司 | A kind of energy-efficient MVR vaporising device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANGHAI CHENJI INVESTMENT CONSULTING CO., LTD. Free format text: FORMER OWNER: WENZHOU TIANLONG LIGHT INDUSTRY EQUIPMENT CO., LTD. Effective date: 20150908 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150908 Address after: 201100 Shanghai city Minhang District Fanghe Road No. 1088 building sixth room 2024 Patentee after: Shanghai morning Cci Capital Ltd Address before: 325000 No. 2, No. 529, 15, Binhai Park, Wenzhou economic and Technological Development Zone, Zhejiang Patentee before: Wenzhou Tianlong Light Industry Equipment Co., Ltd. |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151127 Address after: 201799, No. 4501, Lane 18, Shanghai Qing Ping Road, Qingpu, Shanghai Patentee after: Shanghai Lvzhouyuan Perfume Co., Ltd. Address before: 201100 Shanghai city Minhang District Fanghe Road No. 1088 building sixth room 2024 Patentee before: Shanghai morning Cci Capital Ltd |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140723 Termination date: 20170224 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |