CN106595131A - Vertical direct contact condensation supercooled heat exchanger - Google Patents
Vertical direct contact condensation supercooled heat exchanger Download PDFInfo
- Publication number
- CN106595131A CN106595131A CN201611221876.4A CN201611221876A CN106595131A CN 106595131 A CN106595131 A CN 106595131A CN 201611221876 A CN201611221876 A CN 201611221876A CN 106595131 A CN106595131 A CN 106595131A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- perforated plate
- heat exchanger
- stop valve
- shrouding
- 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.)
- Pending
Links
Classifications
-
- 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
-
- 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0202—Header boxes having their inner space divided by partitions
- F28F9/0204—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
- F28F9/0214—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only longitudinal partitions
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a vertical direct contact condensation supercooled heat exchanger. The bottom of a partition baffle is provided with a rectangular through hole communicating with the inner spaces of the two sides of a cylinder. The four edges of the rectangular through hole separately make contact with and are in welded connection with an upper pipe plate, a lower pipe plate and the inner side walls of the two sides of the cylinder in the axial direction. A partition sealing plate is rectangular. A plurality of through holes are formed in the portion, located on one side of the partition sealing plate, of the upper pipe plate. One ends of heat exchange pipes are inserted into and are in welded connection with the through holes. A plurality of small holes are drilled in the portion, located on the other side of the partition sealing plate, of the upper pipe plate. The outer circle of the upper pipe plate is in welded connection with the inner wall of the cylinder. The lower pipe plate is circular. A plurality of through holes are formed in the portion, located on one side of the partition sealing baffle, of the lower pipe plate. The other ends of the heat exchange pipes are inserted into and are in welded connection with the through holes. The outer circle of the lower pipe plate is in welded connection with the inner wall of the cylinder. By adoption of the vertical direct contact condensation supercooled heat exchanger, the exhaust temperature of a refrigeration compressor can be effectively decreased, the pressure ratio is decreased, the performance of a refrigeration system is improved, and the vertical direct contact condensation supercooled heat exchanger is simple in structure and convenient to operate, protects the environment, and saves energy.
Description
Technical field
The present invention relates to a kind of refrigeration technology field, more particularly to a kind of vertical directly contact condensed cold heat exchanger.
Background technology
The high temperature and high pressure gas that refrigeration compressor is discharged in refrigeration system, take away heat cooling and condense by water cooling medium
Into the liquid of High Temperature High Pressure, cold-producing medium distributes heat to cooling water need to be through the heat convection of two side liquids and heat exchanger heat transfer wall
The heat conduction in face, the thermal resistance that the lubricating oil that particularly heat exchanger heat transfer wall itself and wall gather is formed with dirt causes to pass
Hot coefficient declines, and distributes the heat transfer temperature difference increase between the cold-producing medium and cooling medium needed for same heat, causes refrigerant compression
The pressure at expulsion of machine is raised, and pressure ratio increase, volumetric efficiency is reduced, and the wasted work of refrigeration compressor increases, the performance demands of refrigeration system
Number declines, if the cold-producing medium before reducing pressure by regulating flow is supercool, can increase the refrigerating capacity of vaporizer, corresponding raising refrigeration system
Performance, therefore, the supercool heat exchanger of directly contact coagulation band is developed, the delivery temperature of refrigeration compressor is reduced, pressure ratio is reduced,
Volumetric efficiency is improved, the wasted work of refrigeration compressor is reduced, increases refrigerating capacity, improve the performance of refrigeration system, realize energy-conserving and environment-protective.
But embodiment is there are no at present.
The content of the invention
The purpose of the present invention is the technological deficiency existed for existing refrigeration system, there is provided a kind of vertical directly contact condenses
Cold heat exchanger is crossed, to improve the runnability of refrigeration system.
To realize that the technical scheme that the purpose of the present invention is adopted is：
A kind of vertical directly contact condensed cold heat exchanger, including the first high-temperature gas stop valve, upper perforated plate, separation envelope
Plate, capping, feed pipe, the second high-temperature gas stop valve, solution feed pump, lower perforated plate, aperture, separation baffles, support, supercooled liquid cut-off
Valve, cylinder, heat exchanger tube, condensation water stop valve and cutoff.
The cylinder is cylindrical shape, and separation baffles are rectangle, and its bottom is provided with a connection both sides enclosure interior space
Rectangular through-hole, four edges are contacted and are welded to connect with the both sides axial side wall inwall of upper perforated plate, lower perforated plate, cylinder respectively；Point
It is rectangle every shrouding, upper perforated plate is circle, the one end contacted with separation shrouding is welded to connect, upper perforated plate is separating the one of shrouding
Side is provided with multiple through holes, inserts one end of heat exchanger tube and is welded to connect, and upper perforated plate is drilled with multiple little in the opposite side for separating shrouding
Hole, the inwall of the cylindrical and cylinder of upper perforated plate is welded to connect；Lower perforated plate is circle, is provided with multiple logical in the side of separation baffles
Hole, inserts one end of heat exchanger tube and is welded to connect, and the inwall of the cylindrical and cylinder of lower perforated plate is welded to connect.
The separation baffles side of the cylinder, offers and the first high-temperature gas stop valve, solidifying near one end of upper perforated plate
The aperture of the outlet connecting pipe in parallel welding of knot liquid stop valve, offers near one end of lower perforated plate and is connected with supercooled liquid stop valve
The aperture of sealing of tube, separation baffles other side is offered and the second high-temperature gas near one end of lower perforated plate, position higher position
The aperture of the connection sealing of tube of stop valve, position is relatively low, aperture with feed flow sealing of tube is offered closer at lower perforated plate, described
Capping is welded to connect respectively with the edge of separation shrouding, cylinder, and the cylinder separated between shrouding and capping is offered and feed pipe
The aperture of welding.
The vent connection of the first high-temperature gas stop valve, the entrance of the second high-temperature gas stop valve and refrigeration compressor
It is welded to connect, supercooled liquid stop valve is welded to connect with the inlet connection of reducing pressure by regulating flow element, entrance and the confession of condensation water stop valve
The discharge connection of liquid stop valve is welded to connect.
The import and export of the solution feed pump are welded to connect respectively with two sections of feed pipes.
The support has four, is distributed on the bottom of cylinder, and one end is welded to connect with the outer wall of cylinder, and the other end is fixed
In pond or water tank restocking.
The upper perforated plate on the cylinder top, the open spaces separated between shrouding place the exit end of cooling water pipe.
The separation baffles do not set with cylinder and be provided with the space of heat exchanger tube liquid-level floater valve, the cut-off of the first high-temperature gas
Valve, the second high-temperature gas stop valve, solution feed pump, supercooled liquid stop valve, condensation water stop valve and cutoff are by liquid-level floater
Valve control is opened and closed.
Compared with prior art, the invention has the beneficial effects as follows：
1st, vertical directly contact of the invention condensed cold heat exchanger, and directly contact condenses and supercool one, using high temperature
The refrigerant gas of high pressure are released heat and are condensed with liquid directly contact, can be effectively reduced the aerofluxuss temperature of refrigeration compressor
Degree, reduces pressure ratio, improves volumetric efficiency, reduces the wasted work of refrigeration compressor, improves the performance of refrigeration system.
2nd, vertical directly contact of the invention condensed cold heat exchanger, realize it is supercool before high temperature high pressure liquid reducing pressure by regulating flow,
So that the enthalpy into vaporizer is reduced, big refrigerant system capacity is put forward, further improve the performance of refrigeration system, structure letter
It is single, easy to operate, environmental protection, energy saving.
Description of the drawings
Fig. 1 show the schematic diagram that the vertical directly contact of the present invention condensed cold heat exchanger.
Specific embodiment
The present invention is described in further detail below in conjunction with the drawings and specific embodiments.
The vertical directly contact of the present invention condensed cold heat exchanger schematic diagram as shown in figure 1, cutting including the first high-temperature gas
Only valve 1, upper perforated plate 2, separate shrouding 3, capping 4, feed pipe 5, the second high-temperature gas stop valve 6, solution feed pump 7, lower perforated plate 8, hole
The cut-off of mouth 9, separation baffles 10, support 11, supercooled liquid stop valve 12, cylinder 13, heat exchanger tube 14, condensation water stop valve 15 and feed flow
Valve 16.
The cylinder 13 is cylindrical shape, and separation baffles 10 are rectangle, and upper perforated plate 2 is circle, and lower perforated plate 8 is circle, on
The circumferential periphery of tube sheet 2 and lower perforated plate 8 is fixed respectively with cylinder inboard wall, and separation baffles are put in cylinder along tubular axis, is separated
The upper surface and lower surface of baffle plate is fixed respectively with upper perforated plate and lower perforated plate, and separation baffles bottom is provided with UNICOM's both sides cylinder
The rectangular apertures 9 in portion space, separation baffles are contacted and are welded to connect with upper perforated plate, lower perforated plate and cylinder inboard wall respectively；Separate envelope
Plate 3 is rectangle, separates shrouding 3 and is fixed on upper perforated plate 2, separates shrouding 3 with separation baffles in same perpendicular, upper perforated plate
2 are provided with multiple through holes in the side for separating shrouding 3, insert one end of heat exchanger tube 14 and are welded to connect, and upper perforated plate 2 is separating shrouding
3 opposite side is drilled with multiple apertures；The other end of heat exchanger tube inserts respectively lower perforated plate and is welded to connect,
The cylinder 13 places the side outer wall of heat exchanger tube, and the one end near upper perforated plate 2 offers and the first high-temperature gas
Stop valve 1, the aperture of the outlet connecting pipe in parallel welding of condensation water stop valve 15, the one end near lower perforated plate 8 offers and mistake
Cold liquid stop valve 12 connects the aperture of sealing of tube, and the opposite side outer wall bottom of cylinder 13 offers and the second high-temperature gas stop valve 6
Connection sealing of tube aperture, with the second high-temperature gas stop valve 6 connection sealing of tube aperture below cylinder body outer wall open up
There is the aperture with the welding of feed pipe 5, the capping 4 is welded to connect respectively with the edge of separation shrouding 3, cylinder 13, separates shrouding 3
The aperture with the welding of feed pipe 5 is offered with the side wall of cylinder 13 between capping 4, feed pipe 5 arranges cutoff 16.
The first high-temperature gas stop valve 1, the entrance of the second high-temperature gas stop valve 6 and the aerofluxuss of refrigeration compressor connect
Sealing of tube connects, supercooled liquid stop valve 12 is welded to connect with the inlet connection of reducing pressure by regulating flow element, and condensation water stop valve 15 enters
Mouth is welded to connect with the discharge connection of cutoff 16.
The import and export of the solution feed pump 7 are welded to connect respectively with two sections of feed pipes 5.
The support 11 has four, is distributed on the bottom of cylinder 13, and one end is welded to connect with the outer wall of cylinder 13, another
End is fixed on pond or water tank restocking.
The upper perforated plate 2 on the top of the cylinder 13, the open spaces separated between shrouding 3 place the outlet one of cooling water pipe
End.
The separation baffles 10 do not set with cylinder 13 and be provided with the space of heat exchanger tube liquid-level floater valve, and the first high-temperature gas cuts
Only valve 1, the second high-temperature gas stop valve 6, solution feed pump 7, supercooled liquid stop valve 12, condensation water stop valve 15 and cutoff 16
Opened and closed by the control of liquid-level floater valve.
During assembling, the interior welds lower perforated plate 8 of cylinder 13, separation baffles 10 are welded respectively with cylinder 13, lower perforated plate 8, upper pipe
Plate 2 is welded respectively with separation baffles 10, cylinder 13 and separation shrouding 3, and in the heat exchange pore of upper perforated plate 2, lower perforated plate 8 heat exchanger tube is worn
14 and weld, will capping 4 respectively with separate shrouding 3, cylinder 13 edge be welded to connect, corresponding orifice position welding
Each adapter, welding support 11.
During refrigeration system startup optimization, refrigerant gas Jing oil eliminators of the High Temperature High Pressure that refrigeration compressor is discharged, the
One high-temperature gas stop valve 1 enters the space of cylinder 13, heat exchanger tube 14 and separation baffles 10, carries out with the cooling water in heat exchanger tube
Heat exchange, releases heat, and the high temperature high pressure liquid of condensation accumulates in lower space, and the aperture 9 of the bottom of Jing separation baffles 10 enters
The space of opposite side, when liquid level is to setting liquid level, the first high-temperature gas stop valve 1 is closed, the second high-temperature gas stop valve 6,
Solution feed pump 7, supercooled liquid stop valve 12, condensation water stop valve 15 and cutoff 16 are opened, liquid solution feed pump 7 promotion under,
Into capping 4, separate the space of shrouding 3, cylinder 13 and upper perforated plate 2, and the aperture sprinkling of Jing upper perforated plates 2 drip into upper perforated plate 2,
The space of cylinder 13 and separation baffles 10 and lower perforated plate 8, the refrigerant gas Jing oils of the High Temperature High Pressure that refrigeration compressor is discharged
The space of upper perforated plate 2, cylinder 13 and separation baffles 10 and lower perforated plate 8 is entered from device, the second high-temperature gas stop valve 6, with sprinkling
Liquid heat-exchange under drippage, releases heat and is condensed into liquid, and Jing cutoffs 16, condensation water stop valve 15 enter cylinder
13rd, the cooling water in the space of heat exchanger tube 14 and separation baffles 10, with heat exchanger tube carries out heat exchange, and releasing heat is supercool, supercool
The a part of bottom of Jing separation baffles 10 of liquid aperture 9 enter opposite side space, a part enter through cold liquid stop valve 12
Enter reducing pressure by regulating flow element, for the refrigerant liquid that vaporizer provides low-temp low-pressure, the cooling water of Jing cooling towers cooling is by cylinder
The upper perforated plate 2 on 13 tops, the open spaces separated between shrouding 3 are entered in heat exchanger tube, are flowed after absorption refrigeration agent liberated heat
In entering pond or the water tank of bottom.
The above is only the preferred embodiment of the present invention, it is noted that for the common skill of the art
For art personnel, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications
Also should be regarded as protection scope of the present invention.
Claims (3)
1. a kind of vertical directly contact condensed cold heat exchanger, including the first high-temperature gas stop valve, upper perforated plate, separate shrouding,
Capping, feed pipe, the second high-temperature gas stop valve, lower perforated plate, aperture, separation baffles, supercooled liquid stop valve, cylinder, heat exchanger tube,
Condensation water stop valve and cutoff；The cylinder is cylindrical shape, and separation baffles are rectangle, and upper perforated plate is circle, down tube
Plate is that the circumferential periphery of circle, upper perforated plate and lower perforated plate is fixed respectively with cylinder inboard wall, and separation baffles are put in cylinder along tubular axis
In vivo, the upper surface and lower surface of separation baffles is fixed respectively with upper perforated plate and lower perforated plate, and separation baffles bottom is provided with a UNICOM
The rectangular apertures in both sides inner barrel space, separation baffles are contacted and the company of welding respectively with upper perforated plate, lower perforated plate and cylinder inboard wall
Connect；Separation shrouding is rectangle, separates shrouding and is fixed on upper perforated plate, separates shrouding with separation baffles in same perpendicular,
Upper perforated plate is provided with multiple through holes in the side for separating shrouding, inserts one end of heat exchanger tube and is welded to connect, and upper perforated plate is separating envelope
The opposite side of plate is drilled with multiple apertures；The other end of heat exchanger tube inserts respectively lower perforated plate and is welded to connect,
The cylinder places the side outer wall of heat exchanger tube, and one end adjacent with upper perforated plate offers and the cut-off of the first high-temperature gas
Valve, the aperture of the outlet connecting pipe in parallel welding of condensation water stop valve, one end adjacent with lower perforated plate offers to be cut with supercooled liquid
Only valve connects the aperture of sealing of tube, and cylinder opposite side outer wall bottom offers the connection sealing of tube with the second high-temperature gas stop valve
Aperture, with the second high-temperature gas stop valve connection sealing of tube aperture below cylinder body outer wall offer and feed pipe outlet
The aperture of welding, the capping is welded to connect respectively with the edge of separation shrouding, cylinder, separates the cylinder between shrouding and capping
Side wall offers the aperture with the welding of feed flow tube inlet, and feed pipe arranges cutoff.
2. vertical directly contact according to claim 1 condensed cold heat exchanger, it is characterised in that the solution feed pump enters
Outlet is welded to connect respectively with feed pipe；Support has four, is distributed on the bottom of cylinder, and support one end is welded with the outer wall of cylinder
Connection, the support other end is fixed on pond or water tank restocking；Unlimited sky between upper perforated plate, the separation shrouding on the cylinder top
Between place cooling water pipe exit end.
3. vertical directly contact according to claim 1 condensed cold heat exchanger, it is characterised in that the separation baffles with
Cylinder does not set and be provided with the space of heat exchanger tube liquid-level floater valve, the first high-temperature gas stop valve, the second high-temperature gas stop valve, confession
Liquid pump, supercooled liquid stop valve, condensation water stop valve and cutoff are opened and closed by the control of liquid-level floater valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611221876.4A CN106595131A (en) | 2016-12-27 | 2016-12-27 | Vertical direct contact condensation supercooled heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611221876.4A CN106595131A (en) | 2016-12-27 | 2016-12-27 | Vertical direct contact condensation supercooled heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106595131A true CN106595131A (en) | 2017-04-26 |
Family
ID=58604172
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611221876.4A Pending CN106595131A (en) | 2016-12-27 | 2016-12-27 | Vertical direct contact condensation supercooled heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106595131A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108458604A (en) * | 2018-05-30 | 2018-08-28 | 天津商业大学 | Natural gas waste cold is subcooled and is in direct contact condensation heat transfer equipment |
| CN108645080A (en) * | 2018-05-30 | 2018-10-12 | 天津商业大学 | Spherical natural gas waste cold condensing heat exchanger |
| CN112393630A (en) * | 2019-09-19 | 2021-02-23 | 陶志东 | Counter-flow corrugated preheating plate exchanger for gas-gas heat exchange |
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| EP1031801A2 (en) * | 1999-02-26 | 2000-08-30 | Matsushita Electric Industrial Co., Ltd. | Heat exchanger |
| US6182455B1 (en) * | 1998-06-02 | 2001-02-06 | Sanyo Electronic Co., Ltd. | Apparatus for controlling cooling unit |
| CN2544233Y (en) * | 2002-04-17 | 2003-04-09 | 陈卫华 | High-efficient heat-exchange sleeve evaporation type condenser |
| WO2005005905A1 (en) * | 2003-07-09 | 2005-01-20 | Muller Industries Australia Pty Ltd | System and method of cooling |
| CN201389353Y (en) * | 2009-02-11 | 2010-01-27 | 赛鼎工程有限公司 | Gas stripping type falling film evaporator |
| CN202869091U (en) * | 2012-10-26 | 2013-04-10 | 北京汽车股份有限公司 | Air conditioner condenser structure |
| CN104390495A (en) * | 2014-12-03 | 2015-03-04 | 北京交通大学 | Undercooling type condensation heat exchanger and heat exchange method thereof |
| CN104781622A (en) * | 2012-09-03 | 2015-07-15 | 特灵国际有限公司 | Methods and systems to manage refrigerant in heat exchanger |
| CN204555443U (en) * | 2015-03-04 | 2015-08-12 | 浙江凯迪制冷设备有限公司 | A kind of vaporation-type spray condenser |
| CN206377895U (en) * | 2016-12-27 | 2017-08-04 | 天津商业大学 | Vertical direct contact condensed cold heat exchanger |
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Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US6182455B1 (en) * | 1998-06-02 | 2001-02-06 | Sanyo Electronic Co., Ltd. | Apparatus for controlling cooling unit |
| EP1031801A2 (en) * | 1999-02-26 | 2000-08-30 | Matsushita Electric Industrial Co., Ltd. | Heat exchanger |
| CN2544233Y (en) * | 2002-04-17 | 2003-04-09 | 陈卫华 | High-efficient heat-exchange sleeve evaporation type condenser |
| WO2005005905A1 (en) * | 2003-07-09 | 2005-01-20 | Muller Industries Australia Pty Ltd | System and method of cooling |
| CN201389353Y (en) * | 2009-02-11 | 2010-01-27 | 赛鼎工程有限公司 | Gas stripping type falling film evaporator |
| CN104781622A (en) * | 2012-09-03 | 2015-07-15 | 特灵国际有限公司 | Methods and systems to manage refrigerant in heat exchanger |
| CN202869091U (en) * | 2012-10-26 | 2013-04-10 | 北京汽车股份有限公司 | Air conditioner condenser structure |
| CN104390495A (en) * | 2014-12-03 | 2015-03-04 | 北京交通大学 | Undercooling type condensation heat exchanger and heat exchange method thereof |
| CN204555443U (en) * | 2015-03-04 | 2015-08-12 | 浙江凯迪制冷设备有限公司 | A kind of vaporation-type spray condenser |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108458604A (en) * | 2018-05-30 | 2018-08-28 | 天津商业大学 | Natural gas waste cold is subcooled and is in direct contact condensation heat transfer equipment |
| CN108645080A (en) * | 2018-05-30 | 2018-10-12 | 天津商业大学 | Spherical natural gas waste cold condensing heat exchanger |
| CN112393630A (en) * | 2019-09-19 | 2021-02-23 | 陶志东 | Counter-flow corrugated preheating plate exchanger for gas-gas heat exchange |
| CN112393629A (en) * | 2019-09-19 | 2021-02-23 | 陶志东 | Counter-flow corrugated preheating plate type heat exchanger for gas-gas heat exchange |
| CN112393630B (en) * | 2019-09-19 | 2022-07-22 | 苏州巴涛信息科技有限公司 | Counter-flow corrugated preheating plate exchanger for gas-gas heat exchange |
| CN112393629B (en) * | 2019-09-19 | 2022-09-16 | 苏州巴涛信息科技有限公司 | Counter-flow corrugated preheating plate type heat exchanger for gas-gas heat exchange |
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| PB01 | Publication | ||
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Application publication date: 20170426 |