CN105627787A - Full-evaporation air cooling condenser and using method thereof - Google Patents
Full-evaporation air cooling condenser and using method thereof Download PDFInfo
- Publication number
- CN105627787A CN105627787A CN201410581249.6A CN201410581249A CN105627787A CN 105627787 A CN105627787 A CN 105627787A CN 201410581249 A CN201410581249 A CN 201410581249A CN 105627787 A CN105627787 A CN 105627787A
- Authority
- CN
- China
- Prior art keywords
- air
- water
- tube bank
- finned tube
- tube
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to the field of condensers taking air or water as cooling medium and particularly relates to a full-evaporation air cooling condenser. The full-evaporation air cooling condenser comprises a bracket (1) and a water spraying tube (2) and is characterized by further comprising a tube bundle assembly (3), a water retaining plate (4) and a fan (5), wherein 1%-5% of slope is arranged between a finned tube bundle (33) and a horizontal line; the tube bundle assembly (3) is arranged under a spraying opening (21). A using method of the full-evaporation air cooling condenser is characterized by being successively implemented by the following steps: a medium to be cooled flows into the full-evaporation air cooling condenser from a medium inlet (31) of the tube bundle assembly (3), the air blows into the full-evaporation air cooling condenser from a louver window (7), and cooling water flows into the full-evaporation air cooling condenser from the water inlet end of the water spraying tube (2). The full-evaporation air cooling condenser is high in heat exchange efficiency, high in cooling speed and wide in range of application, and has an effect of purifying the environment air.
Description
Technical field
The present invention relates to application of air or water condensation (cooling) the device field as cooling medium, be specially a kind of pervaporation air cooling tubes condenser and using method thereof.
Background technology
The chiller of employing air or water is conventional heat-exchange apparatus, implements cooling for fluid medium. Current chiller, or it is air-cooled to utilize blower fan air blast to implement, or utilize spray equipment water spray to implement water-cooled. Air-cooled pattern device is simple, but rate of cooling is slow; Water-cooled pattern make use of the high specific heat of water, can obtain stronger cooling effect, but water consumption is many, power consumption height, and has discharge of wastewater, and environment is had pollution.
Summary of the invention
In order to overcome the defect of prior art, it is provided that a kind of heat exchanger effectiveness is high, rate of cooling chiller fast, environment amenable, the invention discloses a kind of pervaporation air cooling tubes condenser and using method thereof.
The present invention reaches goal of the invention by following technical solution:
A kind of pervaporation air cooling tubes condenser, including support and sparge pipe, sparge pipe is fixed on support, sparge pipe is provided with mouth spray, it is characterized in that: also include tube bank assembly, water fender and blower fan, tube bank assembly is by medium inlet, not condensing media outlet, finned tube tube bank and condensed fluid media outlet composition, it is provided with the gradient of 1%��5% between finned tube tube bank and horizontal line to be beneficial to condensed fluid and flow to condensed fluid media outlet from medium inlet, medium inlet, condensing media outlet is not sealedly connected on bottom and the top of fixing bobbin carriage, condensed fluid media outlet is sealedly connected on the bottom of floating bobbin carriage, tube bank assembly is located at the lower section of mouth spray, water fender is above tube bank assembly and sparge pipe, shutter, blower fan is fixed on the top of support, and the air outlet of blower fan faces toward air, it is provided with hydraulic barrier in fixing bobbin carriage to separate inlet feed and the outlet of not condensing, is provided with in floating bobbin carriage and the backflow column plate of finned tube tube bank correspondence position, above backflow column plate, fills filler, to increase gas-to-liquid contact surface area.
Described pervaporation air cooling tubes condenser, it is characterized in that: also include flow controller, flow controller includes electromagnetic valve, temperature sensor and controller, controller connects electromagnetic valve and temperature sensor respectively by order wire, electromagnetic valve is connected in sparge pipe, the temperature probe of temperature sensor is located at media outlet place, and any one in single-chip microcomputer, single board computer, microcomputer and Programmable Logic Controller selected by controller.
Described pervaporation air cooling tubes condenser, is characterized in that: induced air type blower fan selected by blower fan, adopts direct-connection transmission when leaving air temp is not higher than 70 DEG C, adopts belt transmission when leaving air temp is higher than 70 DEG C. It is condensed by flowing through finned tube tube bank bottom by cold vapour phase medium, condensed fluid flows out from condensed fluid media outlet, non-condensing rise through backflow column plate and filler flow through finned tube tube bank top carry out deep condensation, new lime set and not condensing is produced after deep condensation, condensing is not discharged through not condensing media outlet, new lime set is back to the not solidifying gas exchange of the filler in floating bobbin carriage and backflow column plate and rising, in order to reduce the yield of the liquid phase component content liquid phase fraction to increase by 2%��5% in vapour phase, condensation is made to reclaim more thorough; When the present invention is used for cooling down, medium inlet and the same substance that media outlet is that temperature is different; During for condensing, condensing media outlet is not vapour phase, and condensed fluid media outlet is liquid phase.
The present invention have condensation, separation, supercool, purify function.
By cold medium from medium inlet to not condensing media outlet when the present invention is for cooling procedure, adopts the mode of bottom in and top out, and condensed fluid media outlet is closed as sewage draining exit.
Medium to be cooled flows into from the medium inlet of tube bank assembly, flow out from media outlet after finned tube is restrained, air is blown into by the side of shutter, and cooling water flows into from the water intake end of sparge pipe, and the finned tube spraying to tube bank assembly through mouth spray is restrained and heat exchange occurs; The cooling water that air sprays when finned tube is restrained and from finned tube tube bank top mouth spray carries out heat exchange, water (flow) direction is perpendicular with the exchanged form of air-flow direction intersects, decline by row on finned tube is restrained from the cooling water of mouth spray ejection, continuous and air carries out heat exchange, until all evaporating, water vapour after evaporation, under the effect of blower fan, is restrained the water fender of inner side, then is discharged into air by top with air through finned tube.
In order to improve cooling effectiveness and reduce water content consumption, it is also possible to add flow controller, the controller of flow controller is previously entered the temperature threshold value T at media outlet place0, temperature sensor detect the actual temperature T of media outlet in real time, as T��T0Time, controller controls closed electromagnetic valve, now only relies on blower fan air blast cooling, and the present invention is in energy-conservation dry-running pattern; As T > T0Time, controller controls electromagnetic valve and opens, now rely on blower fan air blast cooling and sparge pipe water-spraying control simultaneously, the present invention is in high effect forced refrigerating mode, the flow of cooling water is implemented to control by controlling the opening angle of electromagnetic valve according to the temperature of media outlet by controller, under normal circumstances, spray and lower cool down water through and the heat exchange of medium after all flash to steam, without sewage discharge.
The present invention, with water and air for cooling medium, utilizes air to absorb shower water at tube bank assembly finned tube outer surface and evaporates the heat taking away in cooled (condensation) medium. During work, shower water is delivered to through controlling valve in the spray header of tube bank assembly section upper, is sprayed at finned tube outer surface uniformly through nozzle; Shower water is dispersed on huge external surface area, and abundant and air carries out mass transfer and evaporation, takes away medium heat in pipe. Entered from the adapter of tube bank assembly bottom by cold medium, be assigned in each finned tube. In finned tube, the heat of medium is transmitted to fin by tube wall, being fully contacted at fin outer surface moisture film and air, making water film evaporation, thus realizing the exchange of heat. Become humid air after air and water coke slurry, axial id fan be discharged into air from equipment top, it does not have the shower water evaporated is dropped on next row finned tube, continue to contact with fresh air, continue evaporation, it is achieved another heat exchange, until shower water is all evaporated by air. Shower water is automatically controlled by regulating valve, can be automatically adjusted injection flow rate according to operation requirement. Pervaporation air cooler is generally configured to two tube sides, meet temperature difference countercurrent flow principle, for cooling procedure, this equipment need to close the leakage fluid dram of floating bobbin carriage, medium enters finned tube tube bank pre-cooling from fixing bobbin carriage lower inlet, return through floating bobbin carriage and flow into the tube bank of upper fins pipe, flow out from the adapter of fixing bobbin carriage upper outlet after cooling further. For condensation (or containing not condensing) process, being entered finned tube by cold air from fixing bobbin carriage lower inlet and restrain, flow into floating bobbin carriage after preliminary condensation, condensed fluid is discharged from the bottom leakage fluid dram of floating bobbin carriage. Not solidifying portion gas flows upwardly into finned tube tube bank top from floating bobbin carriage and condenses further, on-condensible gas is discharged from the adapter of fixing bobbin carriage upper outlet, the lime set on finned tube tube bank top is back to floating bobbin carriage, swapped by the not solidifying gas of the filler in bobbin carriage and the part of rising, make the further fractional distillation of fixed gas component and lime set component purify. Fractional distillation lime set is discharged from leakage fluid dram bottom floating bobbin carriage together with converging in the lime set restraining bottom with finned tube bottom floating bobbin carriage.
Comparing with common evaporating air cooler, the present invention has more huge area of dissipation in unit volume, compares by heat exchanger tube and is about more than 15 times; Compare with common wet air cooler, present invention improves over spray mode, reach the tube bank of full finned tube permeable, better heat-radiation effect.
The comparison of the present invention and part pattern air cooler is as shown in table 1:
Table 1:
Note: data system is with horizontal dry air cooled heat exchanger for 100 herein, with the ratio of the present invention or surface evaporation air cooler and the identical parameters of horizontal dry air cooled heat exchanger, owing to being the ratio of identical dimension, therefore does not have unit but a cardinar number.
The invention has the beneficial effects as follows: heat exchanger effectiveness is high, rate of cooling is fast, environment is had the effect purifying air, during for condensing, can be applicable to the condensation of the direct-cooled system steam turbine exhaust steam in power plant, can be used for sea, power plant during for cooling down and strangle the indirect air cooling of system or Harmon system and the brilliant gate valve air cooler of high-voltage fence, more can be widely applied to the process liquid in the field such as petrochemical industry, metallurgy high furnace or process gas and the cooling of steam, condensation, separation, cross cold-peace purification.
Accompanying drawing explanation
Fig. 1 is the front view of the present invention;
Fig. 2 is the right view of the present invention;
Fig. 3 is the partial schematic diagram restraining assembly floating tube case end in the present invention;
Fig. 4 is the structural representation of flow controller and tube bank assembly in the present invention.
Detailed description of the invention
The present invention is further illustrated below by way of specific embodiment.
Embodiment 1
A kind of pervaporation air cooling tubes condenser, including support 1, sparge pipe 2, tube bank assembly 33, water fender 4 and blower fan 5, as shown in FIG. 1 to 3, concrete structure is:
Sparge pipe 2 is fixed on support 1, and sparge pipe 2 is provided with mouth spray 21, tube bank assembly 3 is by medium inlet 31, not condensing media outlet 32, finned tube tube bank 33 and condensed fluid media outlet 34 form, it is provided with the gradient of 1%��5% between finned tube tube bank 33 and horizontal line to be beneficial to condensed fluid and flow to condensed fluid media outlet 34 from medium inlet 31, medium inlet 31, condensing media outlet 32 is not sealedly connected on bottom and the top of fixing bobbin carriage 8, condensed fluid media outlet 34 is sealedly connected on the bottom of floating bobbin carriage 9, tube bank assembly 3 is located at the lower section of mouth spray 21, water fender 4 is above tube bank assembly 3 and sparge pipe 2, shutter 7, blower fan 5 is fixed on the top of support 1, and the air outlet of blower fan 5 faces toward air, it is provided with hydraulic barrier in fixing bobbin carriage to separate inlet feed and the outlet of not condensing, is provided with in floating bobbin carriage and the backflow column plate 36 of finned tube tube bank correspondence position, above backflow column plate 36, fills filler 35, to increase gas-to-liquid contact surface area.
In the present embodiment, support 1 adopts the steel of heat dip zinc treating to make, and can tolerate the corrosion under wet environment. Sparge pipe 2 is fixed on support 1; Finned tube tube bank 33 employing bi-metal rolling, it is designed to unit module, can Optional assembling, replacing and cleaning, the design principle of finned tube tube bank 33 is reduce windage, be beneficial to shower water moistening, be beneficial to enhanced heat exchange, prevent in fin surface fouling, be beneficial to the tube bank assembly 3 cleaning on equipment.
In the present embodiment, induced air type blower fan selected by blower fan 5, direct-connection transmission is adopted when leaving air temp is not higher than 70 DEG C, belt transmission is adopted when leaving air temp is higher than 70 DEG C, flowed through finned tube by cold vapour phase medium by medium inlet 31 to restrain 33 bottoms and be condensed, condensed fluid flows out from condensed fluid media outlet 34, non-condensing rise through backflow column plate 36 and filler 35 flow through finned tube tube bank 33 top carry out deep condensation, new lime set and not condensing is produced after deep condensation, condensing is not discharged through not condensing media outlet 32, new lime set is back to the filler 35 in floating bobbin carriage and backflow column plate 36 and the not solidifying gas exchange risen, in order to reduce the yield of the liquid phase component content liquid phase fraction to increase by 2%��5% in vapour phase, condensation is made to reclaim more thorough, when the present embodiment is used for cooling down, medium inlet 31 is the same substance that temperature is different from media outlet 32, during for condensing, condensing media outlet 32 is not vapour phase, and condensed fluid media outlet 34 is liquid phase.
By cold medium from medium inlet 31 to not condensing media outlet 32 when the present embodiment is for cooling procedure, adopts the mode of bottom in and top out, and condensed fluid media outlet 34 is closed as sewage draining exit.
When the present embodiment uses, implement successively as follows:
Medium to be cooled flows into from the medium inlet 31 of tube bank assembly 3, flow out from media outlet after finned tube restrains 33, air is blown into by the side of shutter 7, and cooling water flows into from the water intake end of sparge pipe 2, sprays to the finned tube tube bank 33 of tube bank assembly 3 through mouth spray 21 and heat exchange occurs;
Air is when finned tube restrains 33 and restrains, from finned tube, the cooling water that 33 top mouth sprays 21 spray and carries out heat exchange, water (flow) direction is perpendicular with the exchanged form of air-flow direction intersects, decline by row in finned tube tube bank 33 from the cooling water of mouth spray 21 ejection, continuous and air carries out heat exchange, until all evaporating, water vapour after evaporation, under the effect of blower fan 5, is restrained the water fender 4 inside 33 with air through finned tube, then is discharged into air by top.
Embodiment 2
A kind of pervaporation air cooling tubes condenser, including support 1, sparge pipe 2, tube bank assembly 3, water fender 4 and blower fan 5, also includes flow controller 6, and as shown in figure Fig. 1��Fig. 4, concrete structure is:
Flow controller 6 is as shown in Figure 4, it is made up of electromagnetic valve 61, temperature sensor 62 and controller 63, controller 63 connects electromagnetic valve 61 and temperature sensor 62 respectively by order wire, electromagnetic valve 61 is connected in sparge pipe 2, the temperature probe of temperature sensor 62 is located at media outlet 32 place, any one in single-chip microcomputer, single board computer, microcomputer and Programmable Logic Controller selected by controller 63, and the present embodiment selects single-chip microcomputer. Other structures are all same with embodiment 1.
When the present embodiment uses, the controller 63 of flow controller 6 is previously entered the temperature threshold value T at media outlet 32 place0, temperature sensor 62 detect the actual temperature T of media outlet 32 in real time, as T��T0Time, controller 63 controls electromagnetic valve 61 and cuts out, and now only relies on blower fan 5 air blast cooling, and the present embodiment is in energy-conservation dry-running pattern. Dry-running pattern is the foundation that lectotype selection calculates, and is generally calculated with ambient temperature 30 DEG C for benchmark, and namely when ambient temperature is not higher than 30 DEG C, equipment is properly functioning does not spray water, and compares with other form evaporation air coolers and annual economizes on water more than 80%. Owing to being dry-running, the windage of equipment is less, and under identical device volume, finned tube tube bank is restrained with the light pipe of shower water and compared, and reflection can save energy more than 15% to the power consumption of blower fan 5.
As T > T0Time, controller 63 controls electromagnetic valve 61 and opens, now rely on blower fan 5 air blast cooling and sparge pipe 2 water-spraying control simultaneously, the present embodiment is in high effect forced refrigerating mode, the flow of cooling water is implemented to control by controlling the opening angle of electromagnetic valve 61 according to the temperature of media outlet 32 by controller 63, under normal circumstances, spray and lower cool down water through and the heat exchange of medium after all flash to steam, without sewage discharge, compares with other form evaporation air coolers and can economize on water more than 35%.
Other usings method are all same with embodiment 1.
Claims (5)
1. a pervaporation air cooling tubes condenser, including support (1) and sparge pipe (2), sparge pipe (2) is fixed on support (1), sparge pipe (2) is provided with mouth spray (21), it is characterized in that: also include tube bank assembly (3), water fender (4) and blower fan (5), tube bank assembly (3) is by medium inlet (31), not condensing media outlet (32), finned tube tube bank (33) and condensed fluid media outlet (34) composition, the gradient of 1%��5% it is provided with between finned tube tube bank (33) and horizontal line, medium inlet (31), condensing media outlet (32) is not sealedly connected on bottom and the top of fixing bobbin carriage (8), condensed fluid media outlet (34) is sealedly connected on the bottom of floating bobbin carriage (9), the lower section of mouth spray (21) is located in tube bank assembly (3), water fender (4) is in the top of tube bank assembly (3) and sparge pipe (2), shutter (7), blower fan (5) is fixed on the top of support (1), and the air outlet of blower fan (5) faces toward air, hydraulic barrier it is provided with to separate inlet feed and the outlet of not condensing in fixing bobbin carriage (8), it is provided with in floating bobbin carriage (9) and the backflow column plate (36) of finned tube tube bank correspondence position, fills filler (35) in backflow column plate (36) top.
2. pervaporation air cooling tubes condenser as claimed in claim 1, it is characterized in that: also include flow controller (6), flow controller (6) includes electromagnetic valve (61), temperature sensor (62) and controller (63), controller (63) connects electromagnetic valve (61) and temperature sensor (62) respectively by order wire, electromagnetic valve (61) is connected in sparge pipe (2), the temperature probe of temperature sensor (62) is located at media outlet (32) place, single-chip microcomputer selected by controller (63), single board computer, any one in microcomputer and Programmable Logic Controller.
3. pervaporation air cooling tubes condenser as claimed in claim 1 or 2, it is characterized in that: induced air type blower fan selected by blower fan (5), direct-connection transmission is adopted when leaving air temp is not higher than 70 DEG C, belt transmission is adopted when leaving air temp is higher than 70 DEG C, flowed through finned tube tube bank (33) bottom by cold vapour phase medium by (31) to be condensed, condensed fluid flows out from condensed fluid media outlet (34), non-condensing rise through backflow column plate (36) and filler (35) flow through finned tube restrain (33) top carry out deep condensation, new lime set and not condensing is produced after deep condensation, condensing is not discharged through not condensing media outlet (32), new lime set is back to the filler (35) in floating bobbin carriage (9) and backflow column plate (36) and the not solidifying gas exchange risen.
4. the using method of pervaporation air cooling tubes condenser as claimed in claim 1 or 2, is characterized in that: implement successively as follows:
Medium to be cooled flows into from the medium inlet (31) of tube bank assembly (3), restrain through finned tube and flow out from media outlet after (33), air is blown into by the side of shutter (7), cooling water flows into from the water intake end of sparge pipe (2), sprays to finned tube tube bank (33) of tube bank assembly (3) through mouth spray (21) and heat exchange occurs;
The cooling water that air sprays when finned tube restrains (33) and from finned tube tube bank (33) top mouth spray (21) carries out heat exchange, water (flow) direction is perpendicular with the exchanged form of air-flow direction intersects, the cooling water sprayed from mouth spray (21) declines by row on finned tube tube bank (33), continuous and air carries out heat exchange, until all evaporating, water vapour after evaporation is under the effect of blower fan (5), restrain the water fender (4) of (33) inner side with air through finned tube, then be discharged into air by top.
5. the using method of pervaporation air cooling tubes condenser as claimed in claim 3, is characterized in that: implement successively as follows:
Medium to be cooled flows into from the medium inlet (31) of tube bank assembly (3), restrain through finned tube and flow out from media outlet after (33), air is blown into by the side of shutter (7), cooling water flows into from the water intake end of sparge pipe (2), sprays to finned tube tube bank (33) of tube bank assembly (3) through mouth spray (21) and heat exchange occurs;
The cooling water that air sprays when finned tube restrains (33) and from finned tube tube bank (33) top mouth spray (21) carries out heat exchange, water (flow) direction is perpendicular with the exchanged form of air-flow direction intersects, the cooling water sprayed from mouth spray (21) declines by row on finned tube tube bank (33), continuous and air carries out heat exchange, until all evaporating, water vapour after evaporation is under the effect of blower fan (5), restrain the water fender (4) of (33) inner side with air through finned tube, then be discharged into air by top;
The controller (63) of flow controller (6) is previously entered the temperature threshold value T at media outlet (32) place0, temperature sensor (62) detect the actual temperature T of media outlet (32) in real time, as T��T0Time, controller (63) controls electromagnetic valve (61) and cuts out to enter energy-conservation dry-running pattern, now only relies on blower fan (5) air blast cooling; As T > T0Time, controller (63) controls electromagnetic valve (61) and opens to enter high effect forced refrigerating mode, now rely on blower fan (5) air blast cooling and sparge pipe (2) water-spraying control simultaneously, the flow of cooling water is implemented to control by controlling the opening angle of electromagnetic valve (61) according to the temperature of media outlet (32) by controller (63), spray and lower cooling water through and the heat exchange of medium after all flash to steam after discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410581249.6A CN105627787B (en) | 2014-10-27 | 2014-10-27 | Pervaporation air cooling tubes condenser and its application method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410581249.6A CN105627787B (en) | 2014-10-27 | 2014-10-27 | Pervaporation air cooling tubes condenser and its application method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105627787A true CN105627787A (en) | 2016-06-01 |
| CN105627787B CN105627787B (en) | 2017-11-24 |
Family
ID=56042948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410581249.6A Expired - Fee Related CN105627787B (en) | 2014-10-27 | 2014-10-27 | Pervaporation air cooling tubes condenser and its application method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105627787B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109186281A (en) * | 2018-10-26 | 2019-01-11 | 隆华科技集团（洛阳）股份有限公司 | A kind of compound evaporative heat-exchange device with composite frame structure |
| CN114688890A (en) * | 2022-05-31 | 2022-07-01 | 杭州国能汽轮工程有限公司 | Condenser |
Citations (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3543843A (en) * | 1968-08-20 | 1970-12-01 | Hudson Products Corp | Air cooled condenser apparatus |
| US4141411A (en) * | 1973-06-14 | 1979-02-27 | Kalnin Igor M | Tubular heat exchanger |
| CN1048262A (en) * | 1989-06-21 | 1991-01-02 | 奥马特涡轮(1965)有限公司 | The heat exchanger of condensing vapor containing non-condensable gases |
| CN2504496Y (en) * | 2001-11-08 | 2002-08-07 | 孔繁民 | Sprinkling evaporation cooler |
| CN1975311A (en) * | 2006-09-22 | 2007-06-06 | 清华大学 | Liquid separating air condenser |
| CN101013005A (en) * | 2006-11-24 | 2007-08-08 | 华中科技大学 | Surface evaporation air cooler heat transfer pipe bundle having membrane expanding plate |
| CN101298964A (en) * | 2008-06-27 | 2008-11-05 | 李永堂 | Evaporative type condenser |
| CN201293561Y (en) * | 2008-09-02 | 2009-08-19 | 哈尔滨空调股份有限公司 | Supercooling air cooler |
| US20100108301A1 (en) * | 2008-11-03 | 2010-05-06 | Mitsubishi Heavy Industries, Ltd. | Method for cooling a humid gas and a device for the same |
| CN201488596U (en) * | 2009-05-27 | 2010-05-26 | 北京和海益制冷科技有限公司 | Detachable tube chamber type evaporation-type heat exchanger |
| CN201945200U (en) * | 2010-12-15 | 2011-08-24 | 鞍钢集团工程技术有限公司 | Steam condensation water recovery system |
| CN202274764U (en) * | 2011-10-02 | 2012-06-13 | 哈尔滨空调股份有限公司 | Vertical pervaporation air cooler |
| CN102620597A (en) * | 2012-04-20 | 2012-08-01 | 魏忠信 | Bottom air admission type closed cooling tower |
| CN202470825U (en) * | 2012-02-06 | 2012-10-03 | 潘传洪 | Efficient evaporative air cooler with C-shaped heat exchange tubes |
| CN202675939U (en) * | 2012-07-25 | 2013-01-16 | 潍坊恒安散热器集团有限公司 | Air cooler with thermal compensation mechanism |
| CN202692762U (en) * | 2012-07-11 | 2013-01-23 | 洛阳隆华传热科技股份有限公司 | Evaporative cooling device with low resistance fall |
| WO2013085457A1 (en) * | 2011-12-09 | 2013-06-13 | Saewstroem Yngve | System for controlling the water quality in a cooling system |
| CN103615911A (en) * | 2013-11-26 | 2014-03-05 | 中冶南方工程技术有限公司 | Natural cooler for steam exhaust system of continuous casting machine |
| CN204255134U (en) * | 2014-10-27 | 2015-04-08 | 上海妍杰环境设备有限公司 | Pervaporation air cooling tubes condenser |
-
2014
- 2014-10-27 CN CN201410581249.6A patent/CN105627787B/en not_active Expired - Fee Related
Patent Citations (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3543843A (en) * | 1968-08-20 | 1970-12-01 | Hudson Products Corp | Air cooled condenser apparatus |
| US4141411A (en) * | 1973-06-14 | 1979-02-27 | Kalnin Igor M | Tubular heat exchanger |
| CN1048262A (en) * | 1989-06-21 | 1991-01-02 | 奥马特涡轮(1965)有限公司 | The heat exchanger of condensing vapor containing non-condensable gases |
| CN2504496Y (en) * | 2001-11-08 | 2002-08-07 | 孔繁民 | Sprinkling evaporation cooler |
| CN1975311A (en) * | 2006-09-22 | 2007-06-06 | 清华大学 | Liquid separating air condenser |
| CN101013005A (en) * | 2006-11-24 | 2007-08-08 | 华中科技大学 | Surface evaporation air cooler heat transfer pipe bundle having membrane expanding plate |
| CN101298964A (en) * | 2008-06-27 | 2008-11-05 | 李永堂 | Evaporative type condenser |
| CN201293561Y (en) * | 2008-09-02 | 2009-08-19 | 哈尔滨空调股份有限公司 | Supercooling air cooler |
| US20100108301A1 (en) * | 2008-11-03 | 2010-05-06 | Mitsubishi Heavy Industries, Ltd. | Method for cooling a humid gas and a device for the same |
| CN201488596U (en) * | 2009-05-27 | 2010-05-26 | 北京和海益制冷科技有限公司 | Detachable tube chamber type evaporation-type heat exchanger |
| CN201945200U (en) * | 2010-12-15 | 2011-08-24 | 鞍钢集团工程技术有限公司 | Steam condensation water recovery system |
| CN202274764U (en) * | 2011-10-02 | 2012-06-13 | 哈尔滨空调股份有限公司 | Vertical pervaporation air cooler |
| WO2013085457A1 (en) * | 2011-12-09 | 2013-06-13 | Saewstroem Yngve | System for controlling the water quality in a cooling system |
| CN202470825U (en) * | 2012-02-06 | 2012-10-03 | 潘传洪 | Efficient evaporative air cooler with C-shaped heat exchange tubes |
| CN102620597A (en) * | 2012-04-20 | 2012-08-01 | 魏忠信 | Bottom air admission type closed cooling tower |
| CN202692762U (en) * | 2012-07-11 | 2013-01-23 | 洛阳隆华传热科技股份有限公司 | Evaporative cooling device with low resistance fall |
| CN202675939U (en) * | 2012-07-25 | 2013-01-16 | 潍坊恒安散热器集团有限公司 | Air cooler with thermal compensation mechanism |
| CN103615911A (en) * | 2013-11-26 | 2014-03-05 | 中冶南方工程技术有限公司 | Natural cooler for steam exhaust system of continuous casting machine |
| CN204255134U (en) * | 2014-10-27 | 2015-04-08 | 上海妍杰环境设备有限公司 | Pervaporation air cooling tubes condenser |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109186281A (en) * | 2018-10-26 | 2019-01-11 | 隆华科技集团（洛阳）股份有限公司 | A kind of compound evaporative heat-exchange device with composite frame structure |
| CN114688890A (en) * | 2022-05-31 | 2022-07-01 | 杭州国能汽轮工程有限公司 | Condenser |
| CN114688890B (en) * | 2022-05-31 | 2022-09-13 | 杭州国能汽轮工程有限公司 | Condenser |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105627787B (en) | 2017-11-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100498179C (en) | Antifreezing and fogging water-saving cooling tower | |
| CN102650503B (en) | Evaporative condensing and cooling device | |
| US7815173B2 (en) | Cooler | |
| CN105066734A (en) | Combined cooling tower | |
| CN201983650U (en) | Separated heat transfer spray closed cooling tower | |
| CN108709341A (en) | A kind of pre- cold mould spray evaporation type condenser | |
| CN103740567A (en) | High-temperature steam cooling system | |
| CN105157281A (en) | Tube-in-tube evaporative condenser with fins | |
| CN204359159U (en) | A kind of horizontal condensing heat exchanger | |
| CN203148265U (en) | Vaporizing type condensation and cooling device | |
| CN202274764U (en) | Vertical pervaporation air cooler | |
| CN205261805U (en) | Evaporation formula condensing equipment based on separated heat pipe precooling | |
| CN105627787A (en) | Full-evaporation air cooling condenser and using method thereof | |
| CN201917241U (en) | Evaporation air cooler of special-shaped section corrugated pipe | |
| CN104406422B (en) | Bushing type composite condensation cooling device | |
| CN204255132U (en) | Bushing type composite condensation cooling device | |
| CN110608492B (en) | Precooling evaporative condensing air conditioning system and control method thereof | |
| CN204255134U (en) | Pervaporation air cooling tubes condenser | |
| CN205174937U (en) | Sleeve pipe evaporative condenser with fin | |
| CN109453611B (en) | Condensate recycling system for high-temperature flue gas | |
| US4239511A (en) | Process and apparatus for cooling coke oven gas | |
| CN204535202U (en) | Economic benefits and social benefits are without dirty energy-saving evaporating type condensation device | |
| CN104132559B (en) | Phase transformation strengthening compound air cooling system | |
| CN206459524U (en) | Pre-cooling type surface evaporation air cooler | |
| CN209475918U (en) | The condensation water recovery and use system of high temperature cigarette vapour |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171124 Termination date: 20201027 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |