CN202083252U - Evaporative condenser - Google Patents
Evaporative condenser Download PDFInfo
- Publication number
- CN202083252U CN202083252U CN2011201329395U CN201120132939U CN202083252U CN 202083252 U CN202083252 U CN 202083252U CN 2011201329395 U CN2011201329395 U CN 2011201329395U CN 201120132939 U CN201120132939 U CN 201120132939U CN 202083252 U CN202083252 U CN 202083252U
- Authority
- CN
- China
- Prior art keywords
- water
- heat exchange
- pvc heat
- casing
- box body
- 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.)
- Expired - Fee Related
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to an evaporative condenser. A main body is a box body, a fan is mounted on the left side of the upper end of the box body, a flow guider is arranged at an opening on the right side of the upper end of the box body, and a circulating water pump is arranged on the left side of the outer part of the box body; a water spraying system, a condensing coil pipe and a PVC (polyvinyl chloride) heat exchange layer, which correspond to the inner part of the box body, are sequentially arranged at the lower end of the fan; a gaseous state cryogen inlet and liquid state cryogen outlets are respectively formed at the upper end and the lower end of the condensing coil pipe; and a water collecting groove formed at the bottom of the box body is connected with the circulating water pump through an internal pipeline. The evaporative condenser is characterized in that a water collecting box is arranged on the right side of the condensing coil pipe; an air guide plate, which is parallel to the side edge of the PVC heat exchange layer, is arranged on the left side of the PVC heat exchange layer; and a water eliminator, which is parallel to the side edge of the PVC heat exchange layer, is arranged on the right side of the PVC heat exchange layer. The evaporative condenser has the advantages that the structural connection is compact, and water saved by 80 percent in a condensation cycle, so that the condensation cost is greatly reduced.
Description
Technical field
The utility model relates to a kind of water and air that utilizes as cooling medium, utilizes the latent heat of vaporization effect of water to finish the evaporative condenser of refrigeration.
Background technology
At present, be applied to chemical industry, be used for the lower the temperature instrument of cooling of reacted solution is adopted shell and tube condenser and cooling tower, water pump and cooling recirculation system of pond composition usually, being used in the shell and tube condenser reduced temperature, take away the water of heat, need enter shell and tube condenser again after with the water suction cooling tower in the pond by water pump.The condensation effect complexity of this structure needs to consume a large amount of moisture in the process of condensation, and whole equipment takies local big, is unfavorable for laying of other affiliated facilities, and the financial cost of condensation process is very high.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of saving water source, reduces production costs and play the rational evaporative condenser of whole facility layout.
The technical scheme in the invention for solving the technical problem is: a kind of evaporative condenser, main body are casing, in the left side of casing upper end blower fan are housed, and the right openings place of casing upper end is provided with an air deflector, and the casing outer left side is provided with a water circulating pump; The inside of corresponding casing is sequentially with water-spray system, condenser coil and PVC heat exchange layers in the blower fan lower end; The upper and lower end of condenser coil offers gaseous state cryogen inlet and liquid refrigerant outlet respectively; The bottom of casing offers water leg, water leg links to each other with water circulating pump by internal pipeline, the right side of described condenser coil is provided with one and receives water tank, be provided with a wind deflector in the left side of PVC heat exchange layers, wind deflector is parallel with the side of PVC heat exchange layers, the right side of PVC heat exchange layers is provided with a water fender, and water fender is parallel with the side of PVC heat exchange layers.
For the ease of blower fan the water in the water-spray system is injected fast, improve the flow velocity of water, single coil pipe is oval in the described condenser coil, and condenser coil tilts along refrigerant flow direction.
Play condensation in order better to absorb, the water that is vaporized can recycle the water in the whole system, described PVC heat exchange layers and bottom half at an angle, angular range is spent 60 °～80.
The beneficial effects of the utility model are: after adopting this structure, condensation effect is better, and the water that plays cooling effect is recycled, and has saved water resource.Overall structure is convenient to the installation of other infrastructure, has reduced production cost.
Description of drawings
Fig. 1 is a schematic internal view of the present utility model;
Among the figure: 1, casing 2, water collection device 3, air deflector 4, water-spray system 5, blower fan 6, gaseous state cryogen inlet 7, condenser coil 8, liquid refrigerant outlet 9, water circulating pump 10, wind deflector 11, PVC heat exchange layers 12, water fender 13, water leg.
The specific embodiment
A kind of evaporative condenser of Fig. 1, main body are casing 1, in the left side of casing 1 upper end blower fan 5 are housed, and the right openings place of casing 1 upper end is provided with an air deflector 3, and the casing outer left side is provided with a water circulating pump 9; The inside of corresponding casing 1 is sequentially with water-spray system 4, condenser coil 7 and PVC heat exchange layers 11 in blower fan 5 lower ends; The upper and lower end of condenser coil 7 offers gaseous state cryogen inlet 6 and liquid refrigerant outlet 8 respectively; The bottom of casing 1 offers water leg 13, water leg 13 links to each other with water circulating pump 9 by internal pipeline, it is characterized in that: the right side of described condenser coil 7 is provided with one and receives water tank 2, be provided with a wind deflector 10 in the left side of PVC heat exchange layers 11, wind deflector 10 is parallel with the side of PVC heat exchange layers 11, the right side of PVC heat exchange layers 11 is provided with a water fender 12, and water fender 12 is parallel with the side of PVC heat exchange layers 11.
Single coil pipe is oval in the described condenser coil 7, and condenser coil 7 tilts along refrigerant flow direction.
Described PVC heat exchange layers 11 and casing 1 bottom at an angle, angular range is at 60 °～80 degree.
The gaseous state cryogen is blasted in the inlet body 1 by blower fan 5, water-spray system 4 and air outside high-temperature gas cold-producing medium in the condenser coil 7 and the condenser coil 7 carry out heat exchange, be condensed into liquid state gradually by gaseous state, the superpower wind-force of blower fan 5 makes shower water cover condenser coil 7 surfaces fully, so also reduced the fouling on the coil pipe, condensed water flows down fast along the coil pipe of ellipse.Temperature raises behind shower water and the absorption of air heat, the water of part becomes gaseous state by liquid state, takes away a large amount of heats by evaporation latent heat, finishes condensation effect, water in the hot-air is stopped by water fender 12, and collect in the PVC heat exchange layers 11, the chilled air cools that the water in the PVC heat exchange layers 11 is flow through, temperature reduces, enter in the water leg 13, water in the water leg 13 is recycled water pump 9 by inner water tube and draws back, and enters once more in the water-spray system 4, reaches recycling effect with this.
After adopting this structure, make full use of air-cooledly, improve heat exchanger effectiveness, reduce water consumption, using water wisely, present water consumption be before 20%.Whole compact conformation has increased the space of laying of other facilities, has reduced production cost.
Claims (3)
1. evaporative condenser, main body is casing (1), in the left side of casing (1) upper end blower fan (5) is housed, and the right openings place of casing (1) upper end is provided with an air deflector (3), and the casing outer left side is provided with a water circulating pump (9); The inside of corresponding casing (1) is sequentially with water-spray system (4), condenser coil (7) and PVC heat exchange layers (11) in blower fan (5) lower end; The upper and lower end of condenser coil (7) offers gaseous state cryogen inlet (6) and liquid refrigerant outlet (8) respectively; The bottom of casing (1) offers water leg (13), water leg (13) links to each other with water circulating pump (9) by internal pipeline, it is characterized in that: the right side of described condenser coil (7) is provided with one and receives water tank (2), be provided with a wind deflector (10) in the left side of PVC heat exchange layers (11), wind deflector (10) is parallel with the side of PVC heat exchange layers (11), the right side of PVC heat exchange layers (11) is provided with a water fender (12), and water fender (12) is parallel with the side of PVC heat exchange layers (11).
2. evaporative condenser according to claim 1 is characterized in that: coil pipe single in the described condenser coil (7) is for oval, and condenser coil (7) tilts along refrigerant flow direction.
3. evaporative condenser according to claim 1 is characterized in that: at an angle, angular range is at 60 °～80 degree bottom casing (1) for described PVC heat exchange layers (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201329395U CN202083252U (en) | 2011-04-29 | 2011-04-29 | Evaporative condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201329395U CN202083252U (en) | 2011-04-29 | 2011-04-29 | Evaporative condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202083252U true CN202083252U (en) | 2011-12-21 |
Family
ID=45343878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201329395U Expired - Fee Related CN202083252U (en) | 2011-04-29 | 2011-04-29 | Evaporative condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202083252U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102305554A (en) * | 2011-04-29 | 2012-01-04 | 苏州市吴赣药业有限公司 | Evaporation condenser |
| CN102589336A (en) * | 2012-03-27 | 2012-07-18 | 无锡市豫达换热器有限公司 | Wet-type air cooling alcohol condensation heat exchanger |
| CN106323044A (en) * | 2016-09-18 | 2017-01-11 | 河北炫坤节能科技股份有限公司 | Spray falling-film device |
-
2011
- 2011-04-29 CN CN2011201329395U patent/CN202083252U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102305554A (en) * | 2011-04-29 | 2012-01-04 | 苏州市吴赣药业有限公司 | Evaporation condenser |
| CN102589336A (en) * | 2012-03-27 | 2012-07-18 | 无锡市豫达换热器有限公司 | Wet-type air cooling alcohol condensation heat exchanger |
| CN106323044A (en) * | 2016-09-18 | 2017-01-11 | 河北炫坤节能科技股份有限公司 | Spray falling-film device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201152648Y (en) | Falling film evaporative cooling refrigeration set | |
| CN202853021U (en) | Buried tube and tubular indirect and direct three-stage composite type evaporative cooling air conditioning unit | |
| CN203893703U (en) | Evaporative cooler closed circulating cooling water device for thermal power plant | |
| CN203116193U (en) | Water chilling unit with combined direct-type evaporative coolers and evaporative condenser | |
| CN104848583A (en) | Lithium bromide absorption type evaporative cooling and dehumidifying air conditioning system for air compressor | |
| CN108444146A (en) | A kind of marine air-conditioning system and refrigerating method based on lithium bromide-water | |
| CN107120876A (en) | A kind of high-efficiency evaporation type condenser | |
| CN202083252U (en) | Evaporative condenser | |
| CN201497089U (en) | Evaporative condensing computer room air conditioner | |
| CN204757209U (en) | Lithium bromide of uniting with air compressor absorbs formula evaporation cooling dehumidification air conditioning system | |
| CN104457317A (en) | Stand-pipe indirect-direct two-stage evaporative cooling tower | |
| CN205261805U (en) | Evaporation formula condensing equipment based on separated heat pipe precooling | |
| CN102305554A (en) | Evaporation condenser | |
| CN103453605B (en) | The power plant vaporation-type condensing plant of indirectly-direct combination | |
| CN204255132U (en) | Bushing type composite condensation cooling device | |
| CN211953332U (en) | Energy-saving and water-saving efficient evaporative condenser | |
| CN203478483U (en) | Composite evaporating and condensing device suitable for power plant | |
| CN203216313U (en) | Tube indirect evaporative cooler with water film expanding plates | |
| CN204301556U (en) | A kind of nested type double tower body double flash evaporation cooling tower | |
| CN103629858A (en) | Direct-evaporation-type mine air return source heat pump system with spray dedusting function | |
| CN109764435A (en) | A kind of cooling water cooler cooling system of the evaporation with cold recovery | |
| CN203116192U (en) | Soil source auxiliary plate-fin indirect-direct two-stage evaporative cooling air conditioner unit | |
| CN210267814U (en) | Fin type air-cooled condenser | |
| CN202032791U (en) | An absorption heat pump evaporator structure for recovering low pressure steam waste heat | |
| CN203798185U (en) | Novel shell and tube evaporative condenser |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111221 Termination date: 20180429 |