CN104406334A - Sprinkling falling film type evaporator and liquid level control method thereof - Google Patents
Sprinkling falling film type evaporator and liquid level control method thereof Download PDFInfo
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- CN104406334A CN104406334A CN201410638421.7A CN201410638421A CN104406334A CN 104406334 A CN104406334 A CN 104406334A CN 201410638421 A CN201410638421 A CN 201410638421A CN 104406334 A CN104406334 A CN 104406334A
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- refrigerant
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- falling film
- evaporation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
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- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a sprinkling falling film type evaporator and a liquid level control method thereof. The sprinkling falling film type evaporator comprises a cylinder body, a plurality of falling film type evaporation heat exchange pipes, a gaseous refrigerant outlet, an oil return outlet, and a refrigerant flowing guide plate assembly, wherein a gaseous refrigerant exchanges heat with the falling film type evaporation heat exchange pipes, and then enters the gaseous refrigerant outlet through the refrigerant flowing guide plate assembly. The sprinkling falling film type evaporator has the advantages that the integral energy efficiency ratio is high, the cost is low, the sprinkling speed is high, the heat exchange coefficient is high, the sprinkling coverage range is large, the distribution of sprinkling amount is uniform, the utilization rate of heat exchange area is high, the heat exchange material is saved, and the heat exchange effect is improved; the integral heat exchange property is good, the unit energy efficiency ratio is high, and the unit running is stable and reliable; the national energy-saving and emission-reduction policies are met, the economic and social benefits are higher, and the sprinkling falling film type evaporation device is worthy of being widely popularized.
Description
Technical field
The present invention relates to a kind of downward film evaporator, particularly relate to a kind of spray downward film evaporator and liquid level controlling method thereof.
Background technology
Current handpiece Water Chilling Units is existing adopts dripping type downward film evaporator, being dripped by the distribution of liquid refrigerant pours on heat exchanger tube, liquid film is formed on heat exchanger tube surface, heat exchanger tube is made to form membranaceous evaporation, because heat exchanger tube surface cold-producing medium belongs to flow regime, cold-producing medium static phase ratio cold with the table of traditional flooded evaporator, the coefficient of heat transfer promotes, simultaneously, because heat exchanger tube table cold-producing medium adopts membranaceous pouring, cold-producing medium is adopted to compare around infiltration than flooded evaporator heat exchanger tube, refrigerant charge in evaporimeter greatly reduces, also improve the concentration of lubricating oil in cold-producing medium simultaneously, make unit oil return more convenient, theoretical performance is more excellent compared with flooded evaporator.
But traditional dripping type downward film evaporator adopts dripping type, and cold-producing medium oozes from drip hole, ooze speed slow, heat exchange series is low.And a pouring is little in the coverage on heat exchanger tube surface, and the cold-producing medium be assigned to from inlet drip hole is at a distance few, the cold-producing medium that the drip hole of nearly inlet is assigned to is many, because heat exchanger is larger, the residing position of drip hole is larger from inlet range deviation, dripping of heat exchanger tube surface is easily caused to drench maldistribution, the cold-producing medium easily causing part heat exchanger tube surface to distribute too much cannot not evaporate completely, part heat exchanger tube surface is but distributed less than cold-producing medium, without evaporation effect, thus make traditional dripping type downward film evaporator, part heat exchange area is only had to work, heat exchange area utilization rate is low, waste a large amount of and heat exchange material, and in fact do not tell on, overall heat exchange poor performance, unit eer is low.
Downward film evaporator kind is in the market many, but overall performance is general, complete machine Energy Efficiency Ratio is low, most of falling film evaporator unit performance in the market and Energy Efficiency Ratio flooded evaporator unit also poor, actual realization differs greatly with theory, cannot its theoretic advantage actual, cause the process of the popularization slow.
Application number be 200610118931.7 Chinese patent " jet flow circulated sprinkling falling-film evaporator " disclose a kind of jet flow circulated sprinkling falling-film evaporator, comprise evaporator shell, be arranged on the gas vent on evaporator shell top, be disposed axially in the heat-exchanging tube bundle in evaporator shell, distributor, gas-liquid separator, distributor is positioned at above heat-exchanging tube bundle, and gas-liquid separator is between distributor and gas vent, also comprise a jet pump, the entrance of the high-pressure refrigerant of this jet pump is communicated with condenser, circulating refrigerant entrance is communicated with bottom evaporator shell, mix refrigerant outlet is communicated with described distributor.This patent utilization pump realizes spray, and power consumption is large, cost is high, non-uniform spraying.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, provide the spray downward film evaporator that a kind of complete machine Energy Efficiency Ratio is high, cost is low, another object of the present invention is to provide the liquid level controlling method of described spray downward film evaporator.
Above-mentioned purpose of the present invention is achieved by following technical solution:
A kind of spray downward film evaporator, comprise cylindrical shell, falling film type evaporation heat exchanger tube, gaseous refrigerant outlet and oil return outlet, also comprise flow of refrigerant deflector sub-assembly, enter gaseous refrigerant with the gas refrigerant after the heat exchange of multiple falling film type evaporation heat exchanger tube by described flow of refrigerant deflector sub-assembly and export.The present invention reduces the use of falling film type evaporation heat exchanger tube dexterously by the combination of flow of refrigerant deflector sub-assembly, and can reach more efficiently evaporation effect.
Further, described flow of refrigerant deflector sub-assembly comprises falling film evaporation baffle upper plate, full liquid evaporation baffle upper plate and falling film evaporation side deflector, one end of described full liquid evaporation baffle upper plate is connected with falling film evaporation side deflector is vertical, the other end is connected with cylindrical shell, described falling film evaporation baffle upper plate one end is divided equally distribution plate with refrigerant distributor and is connected, and the other end evaporates baffle upper plate with full liquid and is connected with the vertical link of falling film evaporation side deflector.
Described falling film evaporation baffle upper plate, full liquid evaporation baffle upper plate and falling film evaporation side deflector are provided with multiple refrigerant passing hole.Described falling film evaporation side deflector prevents liquid refrigerant to be sprayed onto region without pipe, and described falling film evaporation baffle upper plate and full liquid evaporation baffle upper plate prevent liquid refrigerant to be inhaled into gaseous refrigerant outlet, in order to avoid damage compressor due to pressure difference.
Preferably, described refrigerant passing holes is polygonal, round, ellipse or sub-elliptical type.Described refrigerant passing holes arrangement mode is in-line arrangement or fork row.
Described falling film evaporation side deflector and falling film evaporation baffle upper plate surround falling liquid film district, and described cylinder body bottom is provided with full liquid zone, and described falling liquid film district and full liquid zone are covered with many falling film type evaporation heat exchanger tubes.
Preferably, described falling film type evaporation heat exchanger tube axially fork row arrangement or the arrangement of axial in-line arrangement.Be the chilled water of flowing in described falling film type evaporation heat exchange tube, be the cold-producing medium of falling liquid film outside pipe, in pipe, outer fluid carries out heat exchange by heat exchanger tube.
Further, also comprise fountain refrigerant distributing system and refrigerant liquid level controlling system, uniform refrigerant is dispersed on multiple falling film type evaporation heat exchanger tube by described fountain refrigerant distributing system, and described refrigerant liquid level controlling system controls the liquid level of full liquid zone.The present invention improves spray refrigerant flow rates by spray and strengthens spray area, promotes heat transfer effect; Adopt pressure drop averaging type separatory, promote separatory all property, promote evaporation effect; Increase refrigerant liquid level controlling system, prevent compressor liquid hammer, promote unit reliability.
Further, described fountain refrigerant distributing system comprises the cold-producing medium feed tube being located at cylindrical shell upper end, the refrigerant distributor upper cover plate be connected with cold-producing medium feed tube and refrigerant distributor and divides equally distribution plate, described refrigerant distributor is divided equally distribution plate and is provided with multiple aperture, and described cold-producing medium speedup disperser is the cold-producing medium speedup divergent nozzle that multiple aperture is installed.
Preferably, cold-producing medium speedup divergent nozzle is that reducing pipe adds increaser or Venturi tube or increaser.The radial section of described cold-producing medium speedup divergent nozzle is circle, subcircular, triangle or polygon, and the equivalent diameter of nozzle exit orifice is greater than the equivalent diameter of inlet hole.
Described refrigerant liquid level controlling system comprises liquid level control sensor mounting cylinder, liquid level communicating pipe, liquid level sensor and refrigerant flow control expansion valve, described liquid level control sensor mounting cylinder is by being connected with the full liquid zone of cylinder body bottom liquid level communicating pipe, be provided with liquid level sensor in described liquid level control sensor mounting cylinder, described refrigerant flow control expansion valve outlet is connected with cold-producing medium feed tube.
Described flow of refrigerant process of falling spray downward film evaporator is, low-pressure gas-liquid two-phase mixtures cold-producing medium is formed by the throttling of refrigerant flow control expansion valve from condenser high pressure refrigerant liquid out, then entered by cold-producing medium feed tube and be full of refrigerant distributor upper cover plate and refrigerant distributor and divide equally the space that distribution plate connects to form, divide equally by refrigerant distributor a large amount of cold-producing medium speedup divergent nozzles distributed in distribution plate and aperture uniform distribution is installed enters cold-producing medium speedup divergent nozzle.When enter cold-producing medium speedup divergent nozzle be reducing pipe add increaser or Venturi tube time, cold-producing medium is uniformly dispersed and is assigned on falling film type district evaporating heat-exchanging pipe after middle reducing is accelerated; When spray spout is increaser, cold-producing medium is uniformly dispersed and is assigned on falling film type district evaporating heat-exchanging pipe after increaser, progressively drop to lower floor's falling film evaporation pipe by upper strata falling film type evaporation pipe is membranaceous, meanwhile, carry out heat exchange with chilled water in the pipe of falling film type district evaporating heat-exchanging pipe.Now, the chilled water heat of vaporization that some refrigerant absorbs in evaporating heat-exchanging pipe forms refrigerant vapour, and gets back to compressor air suction mouth from the opening of falling film evaporation baffle upper plate and falling film evaporation side deflector by entering gaseous refrigerant outlet; The unevaporated liquid refrigerant of part enters the full liquid zone of cylinder body bottom, with the further heat exchange of full liquid zone evaporating heat-exchanging pipe, absorb the chilled water heat in full liquid zone evaporating heat-exchanging pipe, and evaporation forms refrigerant vapour, cross from the opening of full liquid evaporation baffle upper plate and enter gaseous refrigerant outlet and get back to compressor air suction mouth, thus obtain low temperature chilled water.
The liquid level controlling method of described spray downward film evaporator, as the actual liquid level Y that liquid level sensor is measured
actual< Y
settingtime, increase refrigerant flow control expansion valve opening, strengthen the flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual=Y
settingtime, keep refrigerant flow control expansion valve opening, keep the stability of flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual> Y
settingtime, reduce refrigerant flow control expansion valve opening, reduce the flow entering downward film evaporator cold-producing medium.Thus ensure that downward film evaporator all has suitable liquid level, ensures that it normally runs at any time.
Compared with prior art, beneficial effect of the present invention is as follows:
1, complete machine Energy Efficiency Ratio is high, cost is low.The present invention is separated out falling liquid film district by flow of refrigerant deflector sub-assembly, reduces the quantity of falling film type evaporation heat exchanger tube on the one hand, about reducing half, reduces costs, improves usefulness than the heat exchanger tube of general existing downward film evaporator; Liquid refrigerant can be prevented on the one hand to be sprayed onto region without pipe, or to be inhaled into gaseous refrigerant outlet, in order to avoid damage compressor due to pressure difference;
2, improve spray refrigerant flow rates and strengthen spray area, promoting heat transfer effect, uniform liquid refrigerant.
The present invention adopts fountain to design, and utilizes reducing pipe to add the designs of nozzles mode of increaser, Venturi tube or increaser, and cold-producing medium flows through smallest cross-sectional place flow velocity and naturally rises, and the speed of the cold-producing medium spray of heat exchanging tube-surface is fast, and the coefficient of heat transfer is high.Simultaneously, from the increaser after smallest cross-sectional, make dispersion and the ejection of uniform refrigerant, the coverage sprayed on heat exchanger tube surface is large, and efficiency covers heat exchanger tube surface completely, make all heat exchanger tube surfaces all can spray cold-producing medium, the utilization effect of heat exchange area is high, while saving material heat exchange material, improves heat transfer effect, overall heat exchange performance is good, and unit eer is high.
3, adopt pressure drop averaging type separatory, promote separatory all property, promote evaporation effect
The present invention adopts pressure drop averaging type separatory, owing to there is certain pressure drop, cold-producing medium cannot be unobstructed by the nozzle at nearly inlet place, ensure that and all can be assigned to enough cold-producing mediums with the nozzle in the place of inlet different distance, be evenly distributed in each heat exchanger tube surface, the utilization effect of heat exchange area is high, while saving material heat exchange material, improve heat transfer effect, overall heat exchange performance is good, and unit eer is high.
4, increase liquid level controlling method, prevent compressor liquid hammer, promote unit reliability
Present invention employs rational liquid level controlling method, ensure the liquid level process full-liquid type evaporating area of cold-producing medium in downward film evaporator, the liquid level in device that avoids evaporating is too high, the heat exchanger tube in dipped falling film type evaporation district, make this region heat exchanger tube cannot Falling film heat transfer, also can prevent too high refrigerant level simultaneously, make compressor easy inhalant liquid state cold-producing medium and the liquid hammer that produces, promote complete machine heat exchange property and reliability.
Accompanying drawing explanation
Fig. 1 is spray downward film evaporator front view;
Fig. 2 is spray downward film evaporator left view;
Fig. 3 is spray downward film evaporator top view;
Wherein, 1, cylindrical shell; 21, cold-producing medium feed tube; 22, refrigerant distributor upper cover plate; 23, refrigerant distributor divides equally distribution plate; 24, cold-producing medium speedup divergent nozzle; 3, falling film type evaporation heat exchanger tube; 41, falling film evaporation baffle upper plate; 42, full liquid evaporation baffle upper plate; 43, falling film evaporation side deflector; 5, gaseous refrigerant outlet; 6, refrigerant liquid level controlling system; 61, liquid level control sensor mounting cylinder; 62, liquid level communicating pipe; 63, liquid level sensor; 64, refrigerant flow control expansion valve 7, oil return outlet.
Detailed description of the invention
Below in conjunction with Figure of description and specific embodiment the present invention made and elaborating further, but embodiment does not limit in any form the present invention.
Embodiment 1
A kind of spray downward film evaporator, comprises cylindrical shell 1, fountain refrigerant distributing system, flow of refrigerant deflector sub-assembly, refrigerant liquid level controlling system, falling film type evaporation heat exchanger tube 3, gaseous refrigerant outlet 5 and oil return outlet 7.
Described fountain refrigerant distributing system comprises the cold-producing medium feed tube 21 being located at cylindrical shell upper end, the refrigerant distributor upper cover plate 22 be connected with cold-producing medium feed tube 21 and refrigerant distributor and divides equally distribution plate 23, described refrigerant distributor is divided equally distribution plate 23 and is provided with multiple aperture, and described cold-producing medium speedup disperser is the cold-producing medium speedup divergent nozzle 41 that multiple aperture is installed.Described cold-producing medium speedup divergent nozzle 41 adds increaser or Venturi tube or increaser for reducing pipe.The radial section of described cold-producing medium speedup divergent nozzle 41 is circle, subcircular, triangle or polygon, and the equivalent diameter of nozzle exit orifice is greater than the equivalent diameter of inlet hole.
Described flow of refrigerant deflector sub-assembly comprises falling film evaporation baffle upper plate 41, full liquid evaporation baffle upper plate 42 and falling film evaporation side deflector 43, one end of described full liquid evaporation baffle upper plate 42 is connected with falling film evaporation side deflector 43 is vertical, the other end is connected with cylindrical shell 1, described falling film evaporation baffle upper plate 41 one end is divided equally distribution plate 23 with refrigerant distributor and is connected, and the other end evaporates baffle upper plate 42 with full liquid and is connected with the vertical link of falling film evaporation side deflector 43.Described falling film evaporation baffle upper plate 41, full liquid evaporation baffle upper plate 42 and falling film evaporation side deflector 43 are provided with multiple refrigerant passing hole.Gas refrigerant after heat exchange enters gaseous refrigerant outlet by described opening.Described refrigerant passing holes is square, and arrangement mode is in-line arrangement.
Described falling film type evaporation heat exchanger tube 3 comprises falling film type district evaporating heat-exchanging pipe and full liquid zone evaporating heat-exchanging pipe, and described falling film type evaporation heat exchanger tube is fork row arrangement or the arrangement of axial in-line arrangement axially.Refrigerant distributor is divided equally distribution plate 23, falling film evaporation baffle upper plate 41 and falling film evaporation side deflector 43 and is defined falling liquid film district.Described falling film type evaporation heat exchanger tube 3 is the chilled water of flowing in managing, and is the cold-producing medium of falling liquid film outside pipe, and the interior outer fluid of pipe carries out heat exchange by heat exchanger tube.
Described refrigerant liquid level controlling system comprises liquid level control sensor mounting cylinder 61, liquid level communicating pipe 62, liquid level sensor 63 and refrigerant flow control expansion valve 64, described liquid level control sensor mounting cylinder 61 is by being connected with the full liquid zone bottom cylindrical shell 1 liquid level communicating pipe 62, be provided with liquid level sensor 63 in described liquid level control sensor mounting cylinder 61, described refrigerant flow control expansion valve 64 outlet is connected with cold-producing medium feed tube 21.
Cylindrical shell 1 upper end is located in described gaseous refrigerant outlet 5, and described oil return outlet 7 is located at bottom cylindrical shell 1 and is connected with full liquid zone.
Described flow of refrigerant process of falling spray downward film evaporator is, low-pressure gas-liquid two-phase mixtures cold-producing medium is formed by refrigerant flow control expansion valve 64 throttling from condenser high pressure refrigerant liquid out, then entered by cold-producing medium feed tube 21 and be full of refrigerant distributor upper cover plate 22 and refrigerant distributor and divide equally the space that distribution plate 23 connects to form, divide equally a large amount of cold-producing medium speedup divergent nozzles of distribution in distribution plate 23 by refrigerant distributor and aperture uniform distribution is installed enters cold-producing medium speedup divergent nozzle 24.When enter cold-producing medium speedup divergent nozzle be reducing pipe add increaser or Venturi tube time, cold-producing medium is uniformly dispersed and is assigned on falling film type district evaporating heat-exchanging pipe after middle reducing is accelerated; When spray spout is increaser, cold-producing medium is uniformly dispersed and is assigned on falling film type district evaporating heat-exchanging pipe after increaser, progressively drop to lower floor's falling film evaporation pipe by upper strata falling film type evaporation pipe is membranaceous, meanwhile, carry out heat exchange with chilled water in the pipe of falling film type district evaporating heat-exchanging pipe.Now, the chilled water heat of vaporization that some refrigerant absorbs in evaporating heat-exchanging pipe forms refrigerant vapour, and gets back to compressor air suction mouth from the opening of falling film evaporation baffle upper plate 41 and falling film evaporation side deflector 43 by entering gaseous refrigerant outlet 5; The unevaporated liquid refrigerant of part enters the full liquid zone bottom cylindrical shell 1, with the further heat exchange of full liquid zone evaporating heat-exchanging pipe, absorb the chilled water heat in full liquid zone evaporating heat-exchanging pipe, and evaporation forms refrigerant vapour, cross from the opening of full liquid evaporation baffle upper plate 42 and enter gaseous refrigerant outlet 5 and get back to compressor air suction mouth, thus obtain low temperature chilled water.
The liquid level controlling method of described spray downward film evaporator, as the actual liquid level Y that liquid level sensor 63 is measured
actual< Y
settingtime, increase refrigerant flow control expansion valve 64 aperture, strengthen the flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual=Y
settingtime, keep refrigerant flow control expansion valve 64 aperture, keep the stability of flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual> Y
settingtime, reduce refrigerant flow control expansion valve 64 aperture, reduce the flow entering downward film evaporator cold-producing medium.
Claims (10)
1. a spray downward film evaporator, comprise cylindrical shell, falling film type evaporation heat exchanger tube, gaseous refrigerant outlet and oil return outlet, it is characterized in that, also comprise flow of refrigerant deflector sub-assembly, enter gaseous refrigerant with the gas refrigerant after the heat exchange of multiple falling film type evaporation heat exchanger tube by described flow of refrigerant deflector sub-assembly and export.
2. spray downward film evaporator according to claim 1, it is characterized in that, described flow of refrigerant deflector sub-assembly comprises falling film evaporation baffle upper plate, full liquid evaporation baffle upper plate and falling film evaporation side deflector, one end of described full liquid evaporation baffle upper plate is connected with falling film evaporation side deflector is vertical, the other end is connected with cylindrical shell, described falling film evaporation baffle upper plate one end is divided equally distribution plate with refrigerant distributor and is connected, and the other end evaporates baffle upper plate with full liquid and is connected with the vertical link of falling film evaporation side deflector.
3. spray downward film evaporator according to claim 2, it is characterized in that, described falling film evaporation baffle upper plate, full liquid evaporation baffle upper plate and falling film evaporation side deflector are provided with multiple refrigerant passing hole.
4. spray downward film evaporator according to claim 3, it is characterized in that, described refrigerant passing holes is polygonal, round, ellipse or sub-elliptical type.
5. spray downward film evaporator according to claim 3, it is characterized in that, described refrigerant passing holes arrangement mode is in-line arrangement or fork row.
6. spray downward film evaporator according to claim 2, it is characterized in that, described falling film evaporation side deflector and falling film evaporation baffle upper plate surround falling liquid film district, and described cylinder body bottom is provided with full liquid zone, and described falling liquid film district and full liquid zone are covered with many falling film type evaporation heat exchanger tubes.
7. spray downward film evaporator according to claim 6, it is characterized in that, described falling film type evaporation heat exchanger tube is fork row arrangement or the arrangement of axial in-line arrangement axially.
8. spray downward film evaporator according to claim 1, it is characterized in that, also comprise fountain refrigerant distributing system and refrigerant liquid level controlling system, uniform refrigerant is dispersed on multiple falling film type evaporation heat exchanger tube by described fountain refrigerant distributing system, and described refrigerant liquid level controlling system controls the liquid level of full liquid zone.
9. spray downward film evaporator according to claim 8, it is characterized in that, described refrigerant liquid level controlling system comprises liquid level control sensor mounting cylinder, liquid level communicating pipe, liquid level sensor and refrigerant flow control expansion valve, described liquid level control sensor mounting cylinder is by being connected with the full liquid zone of cylinder body bottom liquid level communicating pipe, be provided with liquid level sensor in described liquid level control sensor mounting cylinder, described refrigerant flow control expansion valve outlet is connected with cold-producing medium feed tube.
10. spray downward film evaporator according to claim 9, it is characterized in that, described refrigerant liquid level controlling system liquid level controlling method is as follows:
As the actual liquid level Y that liquid level sensor is measured
actual< Y
settingtime, increase refrigerant flow control expansion valve opening, strengthen the flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual=Y
settingtime, keep refrigerant flow control expansion valve opening, keep the stability of flow entering downward film evaporator cold-producing medium; As actual liquid level Y
actual> Y
settingtime, reduce refrigerant flow control expansion valve opening, reduce the flow entering downward film evaporator cold-producing medium.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410638421.7A CN104406334B (en) | 2014-11-13 | 2014-11-13 | One kind spray downward film evaporator and its liquid level controlling method |
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|---|---|---|---|
| CN201410638421.7A CN104406334B (en) | 2014-11-13 | 2014-11-13 | One kind spray downward film evaporator and its liquid level controlling method |
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| CN104406334A true CN104406334A (en) | 2015-03-11 |
| CN104406334B CN104406334B (en) | 2017-08-11 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105387653A (en) * | 2015-12-21 | 2016-03-09 | 重庆美的通用制冷设备有限公司 | Evaporator and water chilling unit having same |
| CN109140835A (en) * | 2018-08-07 | 2019-01-04 | 南京恒标斯瑞冷冻机械制造有限公司 | A kind of downward film evaporator |
| CN113357850A (en) * | 2021-06-23 | 2021-09-07 | 特灵空调系统(中国)有限公司 | Evaporator and water chilling unit |
| CN116294303A (en) * | 2023-04-04 | 2023-06-23 | 南京瀚杰制冷科技有限公司 | Method for improving heat exchange efficiency of falling film evaporator and evaporator device thereof |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6868695B1 (en) * | 2004-04-13 | 2005-03-22 | American Standard International Inc. | Flow distributor and baffle system for a falling film evaporator |
| CN101052854A (en) * | 2004-10-13 | 2007-10-10 | 约克国际公司 | Falling film evaporator |
| CN101191683A (en) * | 2006-11-30 | 2008-06-04 | 上海海事大学 | Jet flow circulated sprinkling falling-film evaporator |
| CN101907375A (en) * | 2008-01-11 | 2010-12-08 | 江森自控科技公司 | Heat exchanger |
| CN102472589A (en) * | 2009-07-22 | 2012-05-23 | 江森自控科技公司 | Compact evaporator for chillers |
| CN103925749A (en) * | 2013-12-30 | 2014-07-16 | 麦克维尔空调制冷(武汉)有限公司 | Falling film evaporator |
-
2014
- 2014-11-13 CN CN201410638421.7A patent/CN104406334B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6868695B1 (en) * | 2004-04-13 | 2005-03-22 | American Standard International Inc. | Flow distributor and baffle system for a falling film evaporator |
| CN101052854A (en) * | 2004-10-13 | 2007-10-10 | 约克国际公司 | Falling film evaporator |
| CN101191683A (en) * | 2006-11-30 | 2008-06-04 | 上海海事大学 | Jet flow circulated sprinkling falling-film evaporator |
| CN101907375A (en) * | 2008-01-11 | 2010-12-08 | 江森自控科技公司 | Heat exchanger |
| CN102472589A (en) * | 2009-07-22 | 2012-05-23 | 江森自控科技公司 | Compact evaporator for chillers |
| CN103925749A (en) * | 2013-12-30 | 2014-07-16 | 麦克维尔空调制冷(武汉)有限公司 | Falling film evaporator |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105387653A (en) * | 2015-12-21 | 2016-03-09 | 重庆美的通用制冷设备有限公司 | Evaporator and water chilling unit having same |
| CN105387653B (en) * | 2015-12-21 | 2018-02-06 | 重庆美的通用制冷设备有限公司 | Evaporator and there are its handpiece Water Chilling Units |
| CN109140835A (en) * | 2018-08-07 | 2019-01-04 | 南京恒标斯瑞冷冻机械制造有限公司 | A kind of downward film evaporator |
| CN109140835B (en) * | 2018-08-07 | 2023-04-18 | 南京恒标斯瑞冷冻机械制造有限公司 | Falling film evaporator |
| CN113357850A (en) * | 2021-06-23 | 2021-09-07 | 特灵空调系统(中国)有限公司 | Evaporator and water chilling unit |
| CN113357850B (en) * | 2021-06-23 | 2023-08-25 | 特灵空调系统(中国)有限公司 | Evaporator and water chilling unit |
| CN116294303A (en) * | 2023-04-04 | 2023-06-23 | 南京瀚杰制冷科技有限公司 | Method for improving heat exchange efficiency of falling film evaporator and evaporator device thereof |
| CN116294303B (en) * | 2023-04-04 | 2024-03-19 | 南京瀚杰制冷科技有限公司 | Method for improving heat exchange efficiency of falling film evaporator and evaporator device thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104406334B (en) | 2017-08-11 |
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Address after: 528313 Shunde City, Foshan province Chencun town machinery and equipment Park, No. ten, No. Road, No. 8 Applicant after: GUANGDONG SHENLING AIR-CONDITIONING EQUIPMENT CO., LTD. Address before: 528313 Shunde City, Foshan province Chencun town machinery and equipment Park, No. ten, No. Road, No. 8 Applicant before: Guangdong Shenling Air Conditioning Equipment Co., Ltd. |
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