WO2016119369A1 - Water chiller-heater unit with tube-and-plate type compound heat exchanging evaporative condenser - Google Patents

Water chiller-heater unit with tube-and-plate type compound heat exchanging evaporative condenser Download PDF

Info

Publication number
WO2016119369A1
WO2016119369A1 PCT/CN2015/081400 CN2015081400W WO2016119369A1 WO 2016119369 A1 WO2016119369 A1 WO 2016119369A1 CN 2015081400 W CN2015081400 W CN 2015081400W WO 2016119369 A1 WO2016119369 A1 WO 2016119369A1
Authority
WO
WIPO (PCT)
Prior art keywords
evaporative condenser
tube
heat exchange
compressor
plate
Prior art date
Application number
PCT/CN2015/081400
Other languages
French (fr)
Chinese (zh)
Inventor
李志明
谭栋
张勇
Original Assignee
广州市华德工业有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 广州市华德工业有限公司 filed Critical 广州市华德工业有限公司
Publication of WO2016119369A1 publication Critical patent/WO2016119369A1/en

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/14Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
    • F28F1/22Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally the means having portions engaging further tubular elements

Definitions

  • the invention relates to the field of heat exchange equipment, in particular to a cold and hot water unit with a plate type and a coil type composite type evaporative condenser.
  • the chiller and hot water unit on the market usually uses a curved coil to form a heat exchanger, and the outer surface of the heat exchanger is cooled by spray water, and the circulating spray water is used to evaporate and remove heat.
  • the outer surface of the heat exchanger tube of the coil heat exchanger is generally a smooth surface, and the heat exchange efficiency is low.
  • the surface area of the cooling water evaporating heat transfer is small, and the spacing of the coils needs to be increased to increase the heat exchange time between the cooling water and the air, resulting in a bulky volume of the entire heat exchanger.
  • a heat exchange tube for a coupling coupling coil evaporative condenser is disclosed, and a filler sheet is installed between the coils to guide the spray water to form a water film, and the solution is solved.
  • the problem of disorderly flying water of cooling water is attached to the coil tube by means of a buckle or the like, and the installation and disassembly are cumbersome; in such a mounting manner, the packing piece and the coil tube are not closely installed, which can meet the requirement of guiding the spray water to form a water film.
  • the need for direct heat exchange with the coil cannot be met, and the filler sheet is not a heat exchange material and cannot exchange heat with the coil. Therefore, although the invention patent improves the heat exchange efficiency to some extent, However, since the heat exchange efficiency is improved only by increasing the utilization rate of the cooling water, the heat exchange efficiency is not greatly improved.
  • the technical problem to be solved by the present invention is to increase the heat exchange efficiency to a greater extent by changing the heat exchange structure of the coil.
  • the technical solution adopted by the present invention is a cold water unit with a plate and tube composite heat exchange type evaporative condenser, including a compressor, an evaporative condenser, a throttling device and an evaporator;
  • the evaporative condenser comprises a fan, a water pump, a water distributor and a sump;
  • the evaporative condenser further comprises a plate-tube composite heat exchanger;
  • the plate-tube composite heat exchanger is passed by a plurality of plate-tube composite heat exchangers
  • the inlet tube and the outlet header are connected;
  • the plate tube composite heat exchange sheet comprises a heat transfer plate and a coil processed by the heat exchange tube;
  • the heat transfer plate is provided with a seating groove, and the groove is disposed
  • the shape matches the shape of the coil; the coil is placed in the seating groove, and the gap between the coil and the seating groove is filled with a thermally conductive adhesive layer.
  • the heat transfer plate can guide the spray cooling water from the upper heat exchange tube to the lower heat exchange tube to improve the utilization of the cooling water; and at the same time, the heat conductive adhesive layer fills the gap between the full coil and the heat transfer plate to make the disk
  • the tube is in full contact with the heat transfer plate, and the heat transfer plate becomes a rib of the coil, increasing the effective heat exchange area of the coil.
  • the thermally conductive adhesive layer is a metal filler.
  • a metal filler Such a structure can be realized by soaking liquid metal and then cooling, so that the heat conductive adhesive layer can be sufficiently filled into the gap, and the heat conductivity of the metal is good, thereby further improving the rib formation of the heat transfer sheet.
  • the gap between the coil and the seating groove is less than 10 mm. Such a knot The structure gap is small.
  • the liquid metal When the liquid metal is immersed, due to the viscosity of the liquid metal, the liquid metal will have a capillary action, and after penetrating into the inner surface of the heat transfer plate and the coil contact surface, a uniform layer can be formed in the contact surface.
  • the thin filler not only completely fuses the heat transfer plate and the coil into a whole body, but also has a thin filling layer to reduce the contact thermal resistance between the heat transfer plate and the coil.
  • the heat transfer sheet is also stamped with a plurality of limiting slots and/or positioning pads. Such a structure ensures that the gap between the coil and the heat transfer plate can be sufficiently small when the liquid metal is immersed.
  • the metal filler is one or more of zinc, tin, aluminum, and copper. These metals have low melting point and low price, and are used for liquid metal immersion, which is extremely cost-effective.
  • the thermally conductive adhesive layer is a thermally conductive adhesive. Direct use of thermal adhesives makes processing easier.
  • the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor Air port connection.
  • the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser
  • the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor a port connection
  • the chiller unit is provided with a first refrigerating valve, a second refrigerating valve, a first heat pump valve and a second heat pump valve;
  • the first refrigerating valve is disposed at an exhaust port of the compressor and evaporative condensation
  • the second refrigerating valve is disposed on the connecting pipe of the suction port of the compressor and the gas pipe of the evaporator, and the first heat pump valve is disposed at the exhaust port of the compressor and the gas of the evaporator
  • the second heat pump valve is set at the pressure
  • the suction port of the reducer is connected to the gas pipe of the evaporative conden
  • the exhaust port of the compressor is provided with a first reversing valve
  • the suction port of the compressor is provided with a second reversing valve
  • the two outlets of the first reversing valve are respectively connected with the gas of the evaporating condenser
  • the tube and the gas pipe of the evaporator are connected, and the two inlets of the second reversing valve are respectively connected with the gas pipe of the evaporative condenser and the gas pipe of the evaporator
  • the first and second reversing valves are two-position three-way Directional valve.
  • the hot and cold water unit is provided with a four-way reversing valve, and the four interfaces of the four-way reversing valve are respectively connected with a compressor exhaust port, a gas pipe of an evaporative condenser, a gas pipe of an evaporator, and a compressor.
  • the suction port is connected.
  • the hot and cold water unit with the plate tube composite heat exchange type evaporative condenser has the following beneficial effects:
  • the thermal conductive adhesive layer makes the heat transfer plate and the coil fully contact, so that the coil can generate a ribbing effect through the heat exchange plate and increase the effective heat exchange area;
  • the heat exchange plate can simultaneously drain the cooling water to form a continuous water flow surface, and increase the evaporation surface area of the cooling water;
  • FIG. 1 is a schematic view showing the principle of a refrigeration cycle mode of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser;
  • FIG. 2 is a schematic view showing the principle of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention
  • FIG. 3 is a schematic view showing the principle of a heat pump circulation mode of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention
  • FIG. 4 is a schematic view showing the principle of using a two-position three-way reversing valve for a group of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention
  • FIG. 5 is a schematic view showing the principle of using a four-way reversing valve for a group of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser;
  • Figure 6 is a schematic view showing the structure of an evaporative condenser of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention.
  • FIG. 7 is a schematic structural view of a plate-tube composite heat exchange sheet of a hot and cold water unit with a plate-tube composite heat exchange type evaporative condenser according to the present invention.
  • FIG. 8 is a schematic view showing the structure of a heat transfer plate of a plate-tube composite heat exchange sheet of a hot and cold water unit with a plate-tube composite heat exchange type evaporative condenser according to the present invention.
  • Figure 9 is a cross-sectional view taken along line A-A of Figure 7.
  • the hot and cold water unit includes a compressor 5 and an evaporation type. a condenser 4, an expansion device 6 and an evaporator 7; an exhaust port 51 of the compressor 5 is connected to a gas pipe 4a of the evaporative condenser 4, and a liquid pipe 4b of the evaporative condenser 4 is passed through a throttling device 6
  • the liquid pipe 7a of the evaporator 7 is connected, and the gas pipe 7b of the evaporator 7 is connected to the suction port 52 of the compressor 5.
  • the evaporative condenser 4 employs a plate-tube composite heat exchange sheet, which will not be described in detail herein.
  • the hot and cold water unit is provided with a first refrigeration valve 81, a second refrigeration valve 82, and a first a heat pump valve 83 and a second heat pump valve 84;
  • the first refrigerant valve 81 is disposed on a connecting line of the exhaust port 51 of the compressor 5 and the gas pipe 4a of the evaporative condenser 4
  • the second refrigerating valve 82 is disposed in the compression
  • the first heat pump valve 83 is disposed on the connection line between the exhaust port 51 of the compressor 5 and the gas pipe 7b of the evaporator 7,
  • the second heat pump valve 84 is disposed at the suction port of the compressor 5 52 is connected to the gas pipe 4a of the evaporative condenser 4. Therefore, the hot and cold water unit has a refrigeration cycle mode and a heat pump
  • the apparatus 6 forms a low temperature and low pressure liquid into the evaporative condenser 4, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser 4 and is sucked away by the compressor 1, completing the heat pump circulation mode.
  • FIG. 4 is a schematic view showing the principle of using a two-position three-way reversing valve for the cold and hot water unit of the present invention, which is different from the first embodiment in that the exhaust port 51 of the compressor 5 is provided with a first The two-position three-way reversing valve 85, the suction port 52 of the compressor is provided with a second two-position three-way reversing valve 86; the two outlets of the first two-position three-way reversing valve 85 are respectively connected with the evaporative condenser
  • the gas pipe 4a is connected to the gas pipe 7b of the evaporator, and the two inlets of the second two-position three-way switching valve 86 are connected to the gas pipe 4a of the evaporative condenser and the gas pipe 7b of the evaporator, respectively.
  • the evaporative condenser 4 plate tube composite heat exchange sheet.
  • Fig. 5 is a schematic view showing the principle of the four-way reversing valve of the cold and hot water unit of the present invention, which is different from the first embodiment in that the four ports of the four-way reversing valve 87 are respectively connected to the compressor.
  • the body tube 7b is connected to the suction port 52 of the compressor.
  • the evaporative condenser 4 employs a plate-tube composite heat exchange sheet.
  • the evaporative condenser 4 includes a fan 41, a water pump 42, a water distributor 43, a sump 44; and a plate-tube composite heat exchanger 45; the plate-tube composite heat exchanger 45 is located at the water distributor 43. Between the sump 44, the water distributor 43 and the sump 44 are connected by a water pump 42; the fan 41 is located at one end of the plate-tube composite heat exchanger 45.
  • the plate tube composite heat exchanger 45 is composed of a plurality of plate tube composite heat exchange sheets connected through an inlet header and an outlet header. As shown in FIG. 7 and FIG.
  • the plate tube composite heat exchange sheet includes a coil 1 processed by a heat exchange tube (the processing may be a bending of a long heat exchange tube into a coil tube, or may be The heat exchange tubes of the curved section are welded together with the heat exchange tubes of the straight section to form a coil), and the heat transfer sheet 2 is also included.
  • the coil 1 is formed by continuous S-shaped bending of the heat exchange tubes, wherein the straight sections of the heat exchange tubes are substantially parallel or non-parallel, and the coil 1 can also adopt other suitable for use in the evaporation condenser. shape.
  • the heat exchange tube of the coil 1 may be a copper tube, a stainless steel tube or a galvanized steel tube, etc., and the cross-sectional shape of the internal flow passage may be a circular shape, an elliptical shape, a spiral shape, a corrugated shape or an olive shape.
  • the inner and outer surfaces of the coil 1 can adopt a smooth surface, preferably an enhanced heat transfer surface provided with internal and external threads, and the outer surface of the coil 1 can also be provided with a hydrophilic or anti-corrosive coating.
  • the coil 1 is provided with an inlet and an outlet of a flow passage for connection with an inlet header and an outlet header.
  • the heat exchange tube is bent with a plurality of straight pipe sections; the straight pipe sections adjacent to the heat exchange pipe are parallel to each other, and the pipe spacing of the straight pipe sections adjacent to the heat exchange pipe is the same, or the pipe spacing is located
  • the lower layer that receives the spray cooling water first receives the lower layer of the spray cooling water gradually becomes smaller; or the length of the straight pipe section of the heat exchange tube The degree gradually increases from the upper layer which is first received by the cooling water spray to the lower layer which receives the spray cooling water.
  • the material of the heat transfer sheet 2 may be a carbon steel sheet, a stainless steel sheet, an aluminum sheet, a copper sheet or the like.
  • the plate-tube composite heat exchange fins are disposed longitudinally, that is, the cooling wind blown by the fan 41 flows along the longitudinal direction of the coil pipe 1.
  • the heat transfer plate 2 is provided with a receiving groove 21 .
  • the receiving groove 21 is realized by punching the heat transfer plate 2 , or may be produced.
  • the heat transfer sheet 2 is directly formed; the shape of the seating groove 21 matches the shape of the coil 1.
  • the coil 1 is placed in the seating groove 21, and a gap between the coil 1 and the seating groove 21 is filled with a thermally conductive adhesive layer 3.
  • the thermally conductive adhesive layer 3 is a metal filler zinc.
  • the specific method may be that the heat transfer sheet 2 and the coil 1 are immersed in the high temperature liquid zinc, so that the liquid zinc flows into the gap between the coil 1 and the seating groove 21, and the gap is filled, and the liquid metal is adhered.
  • the heat conductive adhesive layer 3 is filled between the coil 1 and the seating groove 21 to fix the both.
  • tin, aluminum, copper and other metals or combinations thereof can be used, all of which have the characteristics of low melting point and low price, and are cost-effective.
  • the gap between the coil 1 and the seating groove 21 is less than 10 mm.
  • the liquid metal may undergo capillary action, infiltration and transmission.
  • the thermally conductive adhesive layer 3 formed in the gap of the contact can be made uniform and thin, and the heat transfer sheet 2 and the coil 1 are completely fused together as a whole.
  • the thickness of the thermally conductive adhesive layer 3 is thin, the contact thermal resistance between the heat transfer sheet 2 and the coil 1 is effectively reduced. The smaller the gap between the coil 1 and the seating groove 21, the more obvious the capillary action of the liquid metal permeation is formed.
  • the thermal conductive adhesive layer 3 The more uniform the thermal conductive adhesive layer 3 will be, the greater the relative cost and the difficulty of processing; the gap width of 10 mm is the cost-optimal choice, and the gap width of 5 mm is the best cost-effective option, and the uniform effect is optimal within 3 mm. select.
  • the distance between the coil 1 and the heat transfer plate 2 can be sufficiently small, and a plurality of limit grooves and/or positioning pads can be punched out on the heat transfer plate 2 (Fig. Not shown), before the immersion, the coil 1 is pre-fixed by the limit slot mounting or the positioning of the solder joint. It is also possible to pre-fix the two by means of a clamp, but the operation is complicated.
  • the heat of the coil 1 is conducted to the heat transfer sheet 2 through the thermally conductive adhesive layer 3, and the heat transfer sheet 2 becomes the rib of the coil 1, which greatly increases the heat exchange area and directly enhances the heat exchange effect of the coil 1;
  • the hot plate 2 has the effect of guiding the cooling water, so that the cooling water forms a continuous water flow on the surface of the heat transfer plate 2, avoids the disordered flying water of the cooling water, and improves the utilization rate of the cooling water.
  • the heat transfer sheet 2 is integrated, the cooling water at the coupling with the coil 1 can be prevented from flowing alternately, and the water distribution rate can be ensured.
  • the thermal conductive adhesive layer 3 can be replaced by a thermal conductive adhesive; the thermal conductive adhesive is evenly applied to the mounting groove 21 of the heat transfer plate 2, and the coil 1 is directly placed into the mounting groove 21. It can be bonded (for some thermal adhesives that need to be combined, it is also necessary to apply a matching thermal adhesive on the coil 1), which is easy to install and simple in process.
  • the existing thermal conductive adhesives such as silicone thermal conductive adhesives, epoxy resin AB adhesives, and polyurethane thermal conductive adhesives, are not as strong as zinc, aluminum, etc., and are prone to unevenness during the laminating process, resulting in unevenness. When the coil 1 is adhered to the seating groove 21, an air layer insulation phenomenon may occur, which affects heat exchange efficiency.
  • openings, corrugations, bends, and water guides may be provided on the heat transfer plate 2. Structures such as dovetail grooves and ribs are used to increase the effect of water distribution, prevent flying water and enhance solidity. Further, a plurality of elongated holes, round holes or other shaped through holes (not shown) may be formed at the mounting groove 21, and when the coil 1 is placed in the seating groove 21, a part of the coil 1 may be exposed. Outside the tank 21, it can be directly in contact with the condensed water. This method can increase the direct contact area between the coil and the water. At the same time, the opening of the hole can disturb the heat transfer of the copper tube due to the uneven flow of water, but it is certain To a lesser extent, the ribbing of the heat transfer sheets is weakened.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

A water chiller-heater unit with a tube-and-plate type compound heat exchanging evaporative condenser comprises a compressor (5), an evaporative condenser (4), a throttling device (6), and an evaporator (7). The evaporative condenser (4) comprises a fan (41), a water pump (42), a water distributor (43), and a collecting basin (44). The evaporative condenser (4) further comprises a tube-and-plate type compound heat exchanger. The tube-and-plate type compound heat exchanger (45) is formed by connecting multiple tube-and-plate type compound heat exchange sheets between an inlet header and an outlet header. The tube-and-plate type compound heat exchange sheets comprise a heat transfer plate (2) and a coil pipe (1) formed by a shaped heat exchange pipe. The heat transfer plate (2) is provided with an accommodation groove (21). The shape of the accommodation groove (21) matches the shape of the coil pipe (1). The coil pipe (1) is placed in the accommodation groove (21). The gap between the coil pipe (1) and the accommodation groove (21) is filled with a thermally conductive bonding layer (3). The thermally conductive bonding layer (3) ensures full contact between the heat transfer plate (2) and the coil pipe (1), thereby enlarging the effective heat exchange area. The heat transfer plate (2) can also drain cooling water to form a continuous water flow surface, thereby increasing the evaporation surface area of the cooling water, improving heat exchange efficiency and also reducing condenser size.

Description

一种带板管复合换热型蒸发式冷凝器的冷热水机组Hot and cold water unit with plate tube composite heat exchange type evaporative condenser 技术领域Technical field
本发明涉及热交换设备领域,具体涉及一种带板片式、盘管式复合的换型蒸发式冷凝器的冷热水机组。The invention relates to the field of heat exchange equipment, in particular to a cold and hot water unit with a plate type and a coil type composite type evaporative condenser.
背景技术Background technique
现阶段市场上的冷热水机组,其蒸发式冷凝器通常采用弯曲盘管组成换热器,在换热器外表面用喷淋水进行冷却,并利用循环的喷淋水蒸发带走热量。然而,这种盘管式换热器换热管外表面一般为光滑表面,换热效率低。同时,冷却水蒸发换热表面积小,盘管的间距需拉大来增加冷却水与空气的换热时间,导致整个换热器体积庞大。另一方面,由于盘管的上下管之间无介质引导冷却水流动,当冷却水自上而下降落时,在垂直风向的牵引下,冷却水无序飘动易产生飞水,盘管上布水不均匀,易存干点,降低换热能力并存在结垢风险。At present, the chiller and hot water unit on the market usually uses a curved coil to form a heat exchanger, and the outer surface of the heat exchanger is cooled by spray water, and the circulating spray water is used to evaporate and remove heat. However, the outer surface of the heat exchanger tube of the coil heat exchanger is generally a smooth surface, and the heat exchange efficiency is low. At the same time, the surface area of the cooling water evaporating heat transfer is small, and the spacing of the coils needs to be increased to increase the heat exchange time between the cooling water and the air, resulting in a bulky volume of the entire heat exchanger. On the other hand, since there is no medium to guide the flow of cooling water between the upper and lower tubes of the coil, when the cooling water descends from above, under the traction of the vertical wind direction, the cooling water is disorderly fluttering and easy to generate flying water, and the coil is clothed. The water is uneven, easy to store dry spots, reduce heat exchange capacity and there is a risk of scaling.
申请人在先申请的公告号为CN202836298U的专利中,公开了一种填料耦合盘管蒸发式冷凝器用的换热管片,在盘管间加装填料片,引导喷淋水形成水膜,解决了冷却水无序飞水的问题。多片填料片通过卡扣等方式安装到盘管上,安装、拆卸较为繁琐;这样的安装方式,填料片与盘管之间会安装不紧密,可满足引导喷淋水形成水膜的需要,但不能满足与盘管直接换热的需要,而且填料片也不是换热材料,无法与盘管换热。因而虽然该发明专利在一定程度上提高了换热效率, 但由于仅仅是通过提高冷却水的利用率来提高换热效率,换热效率未能得到较大限度的提高。In the patent of the applicant's earlier application number CN202836298U, a heat exchange tube for a coupling coupling coil evaporative condenser is disclosed, and a filler sheet is installed between the coils to guide the spray water to form a water film, and the solution is solved. The problem of disorderly flying water of cooling water. The multi-piece packing piece is attached to the coil tube by means of a buckle or the like, and the installation and disassembly are cumbersome; in such a mounting manner, the packing piece and the coil tube are not closely installed, which can meet the requirement of guiding the spray water to form a water film. However, the need for direct heat exchange with the coil cannot be met, and the filler sheet is not a heat exchange material and cannot exchange heat with the coil. Therefore, although the invention patent improves the heat exchange efficiency to some extent, However, since the heat exchange efficiency is improved only by increasing the utilization rate of the cooling water, the heat exchange efficiency is not greatly improved.
发明内容Summary of the invention
针对上述现有技术不足,本发明要解决的技术问题是通过改变盘管的换热结构,更大限度地提高换热效率。In view of the above-mentioned deficiencies of the prior art, the technical problem to be solved by the present invention is to increase the heat exchange efficiency to a greater extent by changing the heat exchange structure of the coil.
为解决上述技术问题,本发明采用的技术方案为,一种带板管复合换热型蒸发式冷凝器的冷热水机组,包括压缩机、蒸发式冷凝器、节流装置和蒸发器;所述蒸发式冷凝器包括风机、水泵、布水器、集水池;所述蒸发式冷凝器还包括板管复合换热器;所述板管复合换热器由多个板管复合换热片通过进口集管和出口集管连接组成;所述板管复合换热片包括传热板片以及由换热管加工而成的盘管;所述传热板片设有安放槽,该安放槽的形状与盘管的形状匹配;盘管安放于安放槽内,盘管与安放槽之间的间隙填充有导热粘合层。传热板片能引导喷淋冷却水从上层换热管流向下层换热管,提高冷却水的利用率;同时由于导热粘合层填充满盘管与传热板片之间的间隙,使盘管与传热板片充分接触,传热板片从而成为盘管的肋片,增大盘管的有效换热面积。In order to solve the above technical problems, the technical solution adopted by the present invention is a cold water unit with a plate and tube composite heat exchange type evaporative condenser, including a compressor, an evaporative condenser, a throttling device and an evaporator; The evaporative condenser comprises a fan, a water pump, a water distributor and a sump; the evaporative condenser further comprises a plate-tube composite heat exchanger; the plate-tube composite heat exchanger is passed by a plurality of plate-tube composite heat exchangers The inlet tube and the outlet header are connected; the plate tube composite heat exchange sheet comprises a heat transfer plate and a coil processed by the heat exchange tube; the heat transfer plate is provided with a seating groove, and the groove is disposed The shape matches the shape of the coil; the coil is placed in the seating groove, and the gap between the coil and the seating groove is filled with a thermally conductive adhesive layer. The heat transfer plate can guide the spray cooling water from the upper heat exchange tube to the lower heat exchange tube to improve the utilization of the cooling water; and at the same time, the heat conductive adhesive layer fills the gap between the full coil and the heat transfer plate to make the disk The tube is in full contact with the heat transfer plate, and the heat transfer plate becomes a rib of the coil, increasing the effective heat exchange area of the coil.
作为优选,所述导热粘合层为金属填充物。这样的结构可采用浸泡液态金属再冷却的方式实现,使导热粘合层能充分地填充至间隙中,而且金属的导热性能好,进一步提高传热板片的肋化作用。Preferably, the thermally conductive adhesive layer is a metal filler. Such a structure can be realized by soaking liquid metal and then cooling, so that the heat conductive adhesive layer can be sufficiently filled into the gap, and the heat conductivity of the metal is good, thereby further improving the rib formation of the heat transfer sheet.
更优地,所述盘管与安放槽之间的间隙小于10毫米。这样的结 构间隙小,当进行液态金属浸泡时,由于液态金属的黏性,液体金属会发生毛细管作用,在渗透至传热板片与盘管接触面的内部后,能在接触面内形成一层均匀的薄填充物,不仅使传热板片与盘管完全融接为一个整体,而且填充层很薄从而减少了传热板片与盘管之间的接触热阻。More preferably, the gap between the coil and the seating groove is less than 10 mm. Such a knot The structure gap is small. When the liquid metal is immersed, due to the viscosity of the liquid metal, the liquid metal will have a capillary action, and after penetrating into the inner surface of the heat transfer plate and the coil contact surface, a uniform layer can be formed in the contact surface. The thin filler not only completely fuses the heat transfer plate and the coil into a whole body, but also has a thin filling layer to reduce the contact thermal resistance between the heat transfer plate and the coil.
更优地,所述传热板片还冲压有若干限位槽和/或定位焊点。这样的结构可以保证在浸泡液态金属时,盘管与传热板片之间的间隙能保证足够小。More preferably, the heat transfer sheet is also stamped with a plurality of limiting slots and/or positioning pads. Such a structure ensures that the gap between the coil and the heat transfer plate can be sufficiently small when the liquid metal is immersed.
作为优选,所述金属填充物为锌、锡、铝、铜中的一种或多种。这几种金属熔点低、价格便宜,用于液态金属浸泡,具有极高性价比。Preferably, the metal filler is one or more of zinc, tin, aluminum, and copper. These metals have low melting point and low price, and are used for liquid metal immersion, which is extremely cost-effective.
优选方式还可以为,所述导热粘合层为导热粘胶。直接使用导热粘胶使加工更简便。In a preferred embodiment, the thermally conductive adhesive layer is a thermally conductive adhesive. Direct use of thermal adhesives makes processing easier.
作为优选,所述压缩机的排气口与蒸发式冷凝器的气体管连接,蒸发式冷凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机的吸气口连接。Preferably, the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor Air port connection.
作为优选,所述压缩机的排气口与蒸发式冷凝器的气体管连接,蒸发式冷凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机的吸气口连接,所述冷热水机组设置有第一制冷阀、第二制冷阀、第一热泵阀和第二热泵阀;第一制冷阀设置在压缩机的排气口与蒸发式冷凝器的气体管的连接管路上,第二制冷阀设置在压缩机的吸气口与蒸发器的气体管的连接管路上,第一热泵阀设置在压缩机的排气口与蒸发器的气体管的连接管路上,第二热泵阀设置在压 缩机的吸气口与蒸发式冷凝器的气体管的连接管路上。Preferably, the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor a port connection, the chiller unit is provided with a first refrigerating valve, a second refrigerating valve, a first heat pump valve and a second heat pump valve; the first refrigerating valve is disposed at an exhaust port of the compressor and evaporative condensation On the connecting pipe of the gas pipe of the device, the second refrigerating valve is disposed on the connecting pipe of the suction port of the compressor and the gas pipe of the evaporator, and the first heat pump valve is disposed at the exhaust port of the compressor and the gas of the evaporator On the connecting pipe of the pipe, the second heat pump valve is set at the pressure The suction port of the reducer is connected to the gas pipe of the evaporative condenser.
作为优选,所述压缩机的排气口设有第一换向阀,压缩机的吸气口设有第二换向阀;第一换向阀的两个出口分别与蒸发式冷凝器的气体管和蒸发器的气体管连接,第二换向阀的两个进口分别与蒸发式冷凝器的气体管和蒸发器的气体管连接;所述第一、第二换向阀为二位三通换向阀。Preferably, the exhaust port of the compressor is provided with a first reversing valve, and the suction port of the compressor is provided with a second reversing valve; the two outlets of the first reversing valve are respectively connected with the gas of the evaporating condenser The tube and the gas pipe of the evaporator are connected, and the two inlets of the second reversing valve are respectively connected with the gas pipe of the evaporative condenser and the gas pipe of the evaporator; the first and second reversing valves are two-position three-way Directional valve.
作为优选,所述冷热水机组设置有四通换向阀,四通换向阀的四个接口分别与压缩机排气口、蒸发式冷凝器的气体管、蒸发器的气体管和压缩机的吸气口连接。Preferably, the hot and cold water unit is provided with a four-way reversing valve, and the four interfaces of the four-way reversing valve are respectively connected with a compressor exhaust port, a gas pipe of an evaporative condenser, a gas pipe of an evaporator, and a compressor. The suction port is connected.
本发明的一种带板管复合换热型蒸发式冷凝器的冷热水机组,与现有技术相比,具有如下有益效果:Compared with the prior art, the hot and cold water unit with the plate tube composite heat exchange type evaporative condenser has the following beneficial effects:
1)导热粘合层使传热板片与盘管充分接触,使得盘管能通过换热板片产生肋化效应,增大有效换热面积;1) The thermal conductive adhesive layer makes the heat transfer plate and the coil fully contact, so that the coil can generate a ribbing effect through the heat exchange plate and increase the effective heat exchange area;
2)换热板片同时能引流冷却水形成连续的水流面,增大冷却水蒸发表面积;2) The heat exchange plate can simultaneously drain the cooling water to form a continuous water flow surface, and increase the evaporation surface area of the cooling water;
3)增大有效换热面积和冷却水蒸发面积,既提高换热效率,同时又有利于减小冷凝器体积。3) Increasing the effective heat exchange area and the evaporation water evaporation area not only improves the heat exchange efficiency, but also helps to reduce the condenser volume.
上述说明仅是本发明技术方案的概述,为了能够更清楚了解本发明的技术手段,而可依照说明书的内容予以实施,并且为了让本发明的上述和其他目的、特征和优点能够更明显易懂,以下特举较佳实施例,并配合附图,详细说明如下。 The above description is only an overview of the technical solutions of the present invention, and the above-described and other objects, features and advantages of the present invention can be more clearly understood. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, preferred embodiments will be described in detail with reference to the accompanying drawings.
附图说明DRAWINGS
图1是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的制冷循环模式的原理示意图;1 is a schematic view showing the principle of a refrigeration cycle mode of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser;
图2是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的原理示意图;2 is a schematic view showing the principle of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention;
图3是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的热泵循环模式的原理示意图;3 is a schematic view showing the principle of a heat pump circulation mode of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention;
图4是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的组采用二位三通换向阀的原理示意图;4 is a schematic view showing the principle of using a two-position three-way reversing valve for a group of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention;
图5是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的组组采用四通换向阀的原理示意图;5 is a schematic view showing the principle of using a four-way reversing valve for a group of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser;
图6是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的蒸发式冷凝器的结构示意图。Figure 6 is a schematic view showing the structure of an evaporative condenser of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention.
图7是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的板管复合换热片的结构示意图。7 is a schematic structural view of a plate-tube composite heat exchange sheet of a hot and cold water unit with a plate-tube composite heat exchange type evaporative condenser according to the present invention.
图8是本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的板管复合换热片的传热板片结构示意图。8 is a schematic view showing the structure of a heat transfer plate of a plate-tube composite heat exchange sheet of a hot and cold water unit with a plate-tube composite heat exchange type evaporative condenser according to the present invention.
图9是图7沿A-A线的剖面图。Figure 9 is a cross-sectional view taken along line A-A of Figure 7.
具体实施方式detailed description
为更进一步阐述本发明为达成预定发明目的所采取的技术手段及功效,以下结合附图及较佳实施例,对依据本发明的具体实施方式、 结构、特征及其功效,详细说明如下:To further illustrate the technical means and efficacy of the present invention in order to achieve the intended purpose of the invention, the following detailed description of the embodiments The structure, characteristics and efficacy are described in detail as follows:
实施例1Example 1
图1示出了本发明一种带板管复合换热型蒸发式冷凝器的冷热水机组的制冷循环模式的原理示意图,由图1可见,本冷热水机组包括压缩机5、蒸发式冷凝器4、节流装置6和蒸发器7;所述压缩机5的排气口51与蒸发式冷凝器4的气体管4a连接,蒸发式冷凝器4的液体管4b通过节流装置6与蒸发器7的液体管7a连接,蒸发器7的气体管7b与压缩机5的吸气口52连接。该蒸发式冷凝器4采用了板管复合换热片,在此先不做详细描述。1 is a schematic view showing the principle of a refrigeration cycle mode of a hot and cold water unit with a plate and tube composite heat exchange type evaporative condenser according to the present invention. As can be seen from FIG. 1, the hot and cold water unit includes a compressor 5 and an evaporation type. a condenser 4, an expansion device 6 and an evaporator 7; an exhaust port 51 of the compressor 5 is connected to a gas pipe 4a of the evaporative condenser 4, and a liquid pipe 4b of the evaporative condenser 4 is passed through a throttling device 6 The liquid pipe 7a of the evaporator 7 is connected, and the gas pipe 7b of the evaporator 7 is connected to the suction port 52 of the compressor 5. The evaporative condenser 4 employs a plate-tube composite heat exchange sheet, which will not be described in detail herein.
工作原理:制冷剂经压缩机5压缩后成高温高压状态的气体时由制冷系统管道进入蒸发式冷凝器4,经过蒸发式冷凝器4后,高温高压状态的气体被冷却成低温高压液体,并经节流装置6形成低温低压液体进入蒸发器7中与冷冻水进行热交换,制取冷水,然后在蒸发器7中制冷剂液体蒸发汽化并被压缩机5吸走,完成制冷循环模式;Working principle: when the refrigerant is compressed by the compressor 5 into a high temperature and high pressure state, the refrigerant enters the evaporative condenser 4 through the pipeline of the refrigeration system. After passing through the evaporative condenser 4, the gas in the high temperature and high pressure state is cooled into a low temperature and high pressure liquid, and The low-temperature low-pressure liquid is formed in the evaporator 7 through the throttling device 6 to exchange heat with the chilled water to prepare cold water, and then the refrigerant liquid is evaporated and vaporized in the evaporator 7 and sucked away by the compressor 5 to complete the refrigeration cycle mode;
实施例2Example 2
图2示出了本发明冷热水机组的原理示意图,与实施例1相比较,其不同之处在于,所述冷热水机组设置有第一制冷阀81、第二制冷阀82、第一热泵阀83和第二热泵阀84;第一制冷阀81设置在压缩机5的排气口51与蒸发式冷凝器4的气体管4a的连接管路上,第二制冷阀82设置在压缩机5的吸气口52与蒸发器7的气体管7b的连接管路上,第一热泵阀83设置在压缩机5的排气口51与蒸发器7的气体管7b的连接管路上,第二热泵阀84设置在压缩机5的吸气口 52与蒸发式冷凝器4的气体管4a的连接管路上。所以冷热水机组具有制冷循环模式和热泵循环模式。同样,该蒸发式冷凝器2采用了板管复合换热片。2 is a schematic view showing the principle of the cold and hot water unit of the present invention, which is different from the first embodiment in that the hot and cold water unit is provided with a first refrigeration valve 81, a second refrigeration valve 82, and a first a heat pump valve 83 and a second heat pump valve 84; the first refrigerant valve 81 is disposed on a connecting line of the exhaust port 51 of the compressor 5 and the gas pipe 4a of the evaporative condenser 4, and the second refrigerating valve 82 is disposed in the compression On the connection line between the intake port 52 of the machine 5 and the gas pipe 7b of the evaporator 7, the first heat pump valve 83 is disposed on the connection line between the exhaust port 51 of the compressor 5 and the gas pipe 7b of the evaporator 7, The second heat pump valve 84 is disposed at the suction port of the compressor 5 52 is connected to the gas pipe 4a of the evaporative condenser 4. Therefore, the hot and cold water unit has a refrigeration cycle mode and a heat pump cycle mode. Also, the evaporative condenser 2 employs a plate-tube composite heat exchange sheet.
工作原理:当热泵循环模式时,如图3所示,此时打开第一热泵阀83和第二热泵阀84,关闭第一制冷阀81和第二制冷阀82,制冷剂经压缩机5压缩后成高温高压状态的气体时由制冷系统管道进入蒸发器7,与低温热水进行热交换,制取高温热水,然后高温高压状态的气体被冷却成低温高压液体,并经节流装置6形成低温低压液体进入蒸发式冷凝器4,然后在蒸发式冷凝器4中制冷剂液体蒸发汽化并被压缩机1吸走,完成热泵循环模式。Working principle: When the heat pump is in the circulation mode, as shown in FIG. 3, the first heat pump valve 83 and the second heat pump valve 84 are opened at this time, and the first refrigeration valve 81 and the second refrigeration valve 82 are closed, and the refrigerant passes through the compressor. 5 After the gas is compressed into a high temperature and high pressure state, the refrigerant enters the evaporator 7 through the pipeline of the refrigeration system, exchanges heat with the low temperature hot water, and obtains high temperature hot water, and then the gas in the high temperature and high pressure state is cooled into a low temperature and high pressure liquid, and is throttled. The apparatus 6 forms a low temperature and low pressure liquid into the evaporative condenser 4, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser 4 and is sucked away by the compressor 1, completing the heat pump circulation mode.
实施例3Example 3
图4示出了本发明冷热水机组采用二位三通换向阀的原理示意图,与实施例1相比较,其不同之处在于,所述压缩机5的排气口51设有第一二位三通换向阀85,压缩机的吸气口52设有第二二位三通换向阀86;第一二位三通换向阀85的两个出口分别与蒸发式冷凝器的气体管4a和蒸发器的气体管7b连接,第二二位三通换向阀86的两个进口分别与蒸发式冷凝器的气体管4a和蒸发器的气体管7b连接。同样,该蒸发式冷凝器4板管复合换热片。4 is a schematic view showing the principle of using a two-position three-way reversing valve for the cold and hot water unit of the present invention, which is different from the first embodiment in that the exhaust port 51 of the compressor 5 is provided with a first The two-position three-way reversing valve 85, the suction port 52 of the compressor is provided with a second two-position three-way reversing valve 86; the two outlets of the first two-position three-way reversing valve 85 are respectively connected with the evaporative condenser The gas pipe 4a is connected to the gas pipe 7b of the evaporator, and the two inlets of the second two-position three-way switching valve 86 are connected to the gas pipe 4a of the evaporative condenser and the gas pipe 7b of the evaporator, respectively. Similarly, the evaporative condenser 4 plate tube composite heat exchange sheet.
实施例4Example 4
图5示出了本发明冷热水机组采用四通换向阀的原理示意图,与实施例1相比较,其不同之处在于,所述四通换向阀87的四个接口分别与压缩机的排气口51、蒸发式冷凝器的气体管4a、蒸发器的气 体管7b和压缩机的吸气口52连接。同样,该蒸发式冷凝器4采用了板管复合换热片。Fig. 5 is a schematic view showing the principle of the four-way reversing valve of the cold and hot water unit of the present invention, which is different from the first embodiment in that the four ports of the four-way reversing valve 87 are respectively connected to the compressor. Exhaust port 51, gas tube 4a of the evaporative condenser, gas of the evaporator The body tube 7b is connected to the suction port 52 of the compressor. Also, the evaporative condenser 4 employs a plate-tube composite heat exchange sheet.
对于上述实施例中所使用的蒸发式冷凝器4,下面进行详细说明。The evaporative condenser 4 used in the above embodiment will be described in detail below.
如图6所示,蒸发式冷凝器4,包括风机41、水泵42、布水器43、集水池44;还包括板管复合换热器45;板管复合换热器45位于布水器43与集水池44之间,布水器43与集水池44由水泵42连通;风机41位于板管复合换热器45的一端。所述板管复合换热器45由多个板管复合换热片通过进口集管和出口集管连接组成。如图7和图8所示,所述板管复合换热片,包括由换热管加工而成的盘管1(所述加工可以为对长换热管弯曲成盘管,也可以是把弯段的换热管与直段的换热管焊接在一起成为盘管),还包括传热板片2。本实施例中盘管1由换热管连续S形弯曲而成,其中换热管的直线段大致基本平行,也可以不平行,该盘管1也可以采用其他适用于蒸发冷凝器内的其它形状。盘管1的换热管可以采用铜管、不锈钢管或镀锌钢管等,其内部流道的截面形状可为圆形、椭圆形、螺旋形、波纹形或橄榄形等形状。作为本领域人员可以理解的是,盘管1内外表面可以采用光滑表面,优选采用设有内、外螺纹的强化传热表面,同时所述盘管1外表面也可设有亲水或防腐涂层。该盘管1设有流道的入口及出口,用于与进口集管、出口集管连接。本实施例中,所述换热管弯曲有多个直管段;相邻所述换热管的直管段相互平行,相邻所述换热管的直管段的管间距相同,或者管间距从位于先接受喷淋冷却水的上层至后接受喷淋冷却水的下层逐渐变小;也可以是所述换热管的直管段的长 度从位于先接受冷却水喷淋的上层至后接受喷淋冷却水的下层逐渐增加。传热板片2的材质可为碳钢板、不锈钢板、铝片、铜片等。所述板管复合换热片纵向设置,即所述风机41吹的冷却风沿所述盘管1的大致长度方向流动。As shown in FIG. 6, the evaporative condenser 4 includes a fan 41, a water pump 42, a water distributor 43, a sump 44; and a plate-tube composite heat exchanger 45; the plate-tube composite heat exchanger 45 is located at the water distributor 43. Between the sump 44, the water distributor 43 and the sump 44 are connected by a water pump 42; the fan 41 is located at one end of the plate-tube composite heat exchanger 45. The plate tube composite heat exchanger 45 is composed of a plurality of plate tube composite heat exchange sheets connected through an inlet header and an outlet header. As shown in FIG. 7 and FIG. 8 , the plate tube composite heat exchange sheet includes a coil 1 processed by a heat exchange tube (the processing may be a bending of a long heat exchange tube into a coil tube, or may be The heat exchange tubes of the curved section are welded together with the heat exchange tubes of the straight section to form a coil), and the heat transfer sheet 2 is also included. In this embodiment, the coil 1 is formed by continuous S-shaped bending of the heat exchange tubes, wherein the straight sections of the heat exchange tubes are substantially parallel or non-parallel, and the coil 1 can also adopt other suitable for use in the evaporation condenser. shape. The heat exchange tube of the coil 1 may be a copper tube, a stainless steel tube or a galvanized steel tube, etc., and the cross-sectional shape of the internal flow passage may be a circular shape, an elliptical shape, a spiral shape, a corrugated shape or an olive shape. As can be understood by those skilled in the art, the inner and outer surfaces of the coil 1 can adopt a smooth surface, preferably an enhanced heat transfer surface provided with internal and external threads, and the outer surface of the coil 1 can also be provided with a hydrophilic or anti-corrosive coating. Floor. The coil 1 is provided with an inlet and an outlet of a flow passage for connection with an inlet header and an outlet header. In this embodiment, the heat exchange tube is bent with a plurality of straight pipe sections; the straight pipe sections adjacent to the heat exchange pipe are parallel to each other, and the pipe spacing of the straight pipe sections adjacent to the heat exchange pipe is the same, or the pipe spacing is located The lower layer that receives the spray cooling water first receives the lower layer of the spray cooling water gradually becomes smaller; or the length of the straight pipe section of the heat exchange tube The degree gradually increases from the upper layer which is first received by the cooling water spray to the lower layer which receives the spray cooling water. The material of the heat transfer sheet 2 may be a carbon steel sheet, a stainless steel sheet, an aluminum sheet, a copper sheet or the like. The plate-tube composite heat exchange fins are disposed longitudinally, that is, the cooling wind blown by the fan 41 flows along the longitudinal direction of the coil pipe 1.
如图8和图9所示,所述传热板片2的设有安放槽21,本实施例中,该安放槽21通过对传热板片2进行冲压的方式实现,也可以是在生产传热板片2是直接成型;该安放槽21的形状与盘管1的形状匹配。盘管1安放于安放槽21内,盘管1与安放槽21之间的间隙填充有导热粘合层3。本实施例中,所述导热粘合层3为金属填充物锌。具体的做法可以为,将传热板片2、盘管1在高温的液态锌内浸泡,使液态的锌流进盘管1与安放槽21的间隙中,将间隙填满,液态金属的黏性使两者粘紧,液态金属冷却凝固为固态时,成为导热粘合层3,填充于盘管1与安放槽21之间,将两者固定。除了锌外,还可以选用锡、铝、铜等金属或其金属组合,它们都具有熔点低、价格便宜的特点,性价比高。As shown in FIG. 8 and FIG. 9 , the heat transfer plate 2 is provided with a receiving groove 21 . In the embodiment, the receiving groove 21 is realized by punching the heat transfer plate 2 , or may be produced. The heat transfer sheet 2 is directly formed; the shape of the seating groove 21 matches the shape of the coil 1. The coil 1 is placed in the seating groove 21, and a gap between the coil 1 and the seating groove 21 is filled with a thermally conductive adhesive layer 3. In this embodiment, the thermally conductive adhesive layer 3 is a metal filler zinc. The specific method may be that the heat transfer sheet 2 and the coil 1 are immersed in the high temperature liquid zinc, so that the liquid zinc flows into the gap between the coil 1 and the seating groove 21, and the gap is filled, and the liquid metal is adhered. When the liquid metal is cooled and solidified into a solid state, the heat conductive adhesive layer 3 is filled between the coil 1 and the seating groove 21 to fix the both. In addition to zinc, tin, aluminum, copper and other metals or combinations thereof can be used, all of which have the characteristics of low melting point and low price, and are cost-effective.
进一步地,本实施例中,所述盘管1与安放槽21之间的间隙小于10毫米,当进行液态金属浸泡时,由于液态金属的黏性,液体金属会发生毛细管作用,在渗透至传热板片2与盘管1的接触面内部后,能使在接触的间隙内形成的导热粘合层3均匀且厚度薄,不仅使传热板片2与盘管1完全融接为一个整体,而且由于导热粘合层3的厚度薄,有效减少了传热板片2与盘管1之间的接触热阻。盘管1与安放槽21之间的间隙越小,液态金属渗透的毛细管作用越明显,形成的 导热粘合层3会越均匀,相对地成本和加工难度却越大;10毫米的间隙宽度为成本最优选择,而5毫米的间隙宽度为最优性价比选择,3毫米以内为均匀效果最优选择。更进一步地,为保证浸泡高温液态金属时,盘管1与传热板片2之间的间距能足够小,可以在传热板片2冲压出若干限位槽和/或定位焊点(图未示出),在浸泡之前,通过限位槽限位安装或定位焊点部分焊接,先对盘管1实现预固定。也可以采用夹具的方式使两者先预固定,但操作较复杂。Further, in this embodiment, the gap between the coil 1 and the seating groove 21 is less than 10 mm. When the liquid metal is immersed, due to the viscosity of the liquid metal, the liquid metal may undergo capillary action, infiltration and transmission. After the hot plate 2 and the inside of the contact surface of the coil 1, the thermally conductive adhesive layer 3 formed in the gap of the contact can be made uniform and thin, and the heat transfer sheet 2 and the coil 1 are completely fused together as a whole. Moreover, since the thickness of the thermally conductive adhesive layer 3 is thin, the contact thermal resistance between the heat transfer sheet 2 and the coil 1 is effectively reduced. The smaller the gap between the coil 1 and the seating groove 21, the more obvious the capillary action of the liquid metal permeation is formed. The more uniform the thermal conductive adhesive layer 3 will be, the greater the relative cost and the difficulty of processing; the gap width of 10 mm is the cost-optimal choice, and the gap width of 5 mm is the best cost-effective option, and the uniform effect is optimal within 3 mm. select. Furthermore, in order to ensure that the high temperature liquid metal is immersed, the distance between the coil 1 and the heat transfer plate 2 can be sufficiently small, and a plurality of limit grooves and/or positioning pads can be punched out on the heat transfer plate 2 (Fig. Not shown), before the immersion, the coil 1 is pre-fixed by the limit slot mounting or the positioning of the solder joint. It is also possible to pre-fix the two by means of a clamp, but the operation is complicated.
盘管1的热量通过导热粘合层3传导至传热板片2,传热板片2成为盘管1的肋片,大大增加换热面积,直接强化盘管1的换热效果;同时传热板片2又具有引导冷却水的效果,使冷却水在传热板片2的表面形成连续水流,避免冷却水无序飞水,提高冷却水利用率。此外,由于传热板片2为一个整体,能避免与盘管1耦合处的冷却水交错流动,保证布水率。The heat of the coil 1 is conducted to the heat transfer sheet 2 through the thermally conductive adhesive layer 3, and the heat transfer sheet 2 becomes the rib of the coil 1, which greatly increases the heat exchange area and directly enhances the heat exchange effect of the coil 1; The hot plate 2 has the effect of guiding the cooling water, so that the cooling water forms a continuous water flow on the surface of the heat transfer plate 2, avoids the disordered flying water of the cooling water, and improves the utilization rate of the cooling water. In addition, since the heat transfer sheet 2 is integrated, the cooling water at the coupling with the coil 1 can be prevented from flowing alternately, and the water distribution rate can be ensured.
另一方面,所述导热粘合层3可以采用导热粘胶代替;只需把导热粘胶均匀涂抹在传热板片2的安放槽21处,再直接把盘管1安放进安放槽21内即可粘合(对于部分需要组合使用的导热粘胶,则还需在盘管1上涂抹配合的导热粘胶),安装简便、工艺简单。但现有的导热粘胶,例如有机硅导热胶、环氧树脂AB胶、聚氨酯导热胶等,其导热能力都不如锌、铝等金属强,而且在布胶过程中容易出现不均匀现象,导致盘管1粘合到安放槽21内时可能会出现空气层隔热现象,影响换热效率。On the other hand, the thermal conductive adhesive layer 3 can be replaced by a thermal conductive adhesive; the thermal conductive adhesive is evenly applied to the mounting groove 21 of the heat transfer plate 2, and the coil 1 is directly placed into the mounting groove 21. It can be bonded (for some thermal adhesives that need to be combined, it is also necessary to apply a matching thermal adhesive on the coil 1), which is easy to install and simple in process. However, the existing thermal conductive adhesives, such as silicone thermal conductive adhesives, epoxy resin AB adhesives, and polyurethane thermal conductive adhesives, are not as strong as zinc, aluminum, etc., and are prone to unevenness during the laminating process, resulting in unevenness. When the coil 1 is adhered to the seating groove 21, an air layer insulation phenomenon may occur, which affects heat exchange efficiency.
此外,还可以在传热板片2上设置开孔、波纹、折弯、导水槽、 燕尾槽、加强筋等结构,以实现增加布水效果、防止飞水以及增强坚固性等效果。更进一步地,可在安放槽21处开设若干长条形孔、圆孔或其他形状的通孔(图未示出),当盘管1安置于安放槽21内的时候,可以有一部分露出于安放槽21外,可直接与冷凝水接触,此种做法可以增大盘管与水的直接接触面积,同时开孔处由于不平整对水流动有扰动的作用可强化铜管换热,但在一定程度上弱化了传热板片的肋化作用。In addition, openings, corrugations, bends, and water guides may be provided on the heat transfer plate 2. Structures such as dovetail grooves and ribs are used to increase the effect of water distribution, prevent flying water and enhance solidity. Further, a plurality of elongated holes, round holes or other shaped through holes (not shown) may be formed at the mounting groove 21, and when the coil 1 is placed in the seating groove 21, a part of the coil 1 may be exposed. Outside the tank 21, it can be directly in contact with the condensed water. This method can increase the direct contact area between the coil and the water. At the same time, the opening of the hole can disturb the heat transfer of the copper tube due to the uneven flow of water, but it is certain To a lesser extent, the ribbing of the heat transfer sheets is weakened.
上述实施方式仅为本发明的优选实施方式,不能以此来限定本发明保护的范围,本领域的技术人员在本发明的基础上所做的任何非实质性的变化及替换均属于本发明所要求保护的范围。 The above embodiments are merely preferred embodiments of the present invention, and the scope of the present invention is not limited thereto, and any insubstantial changes and substitutions made by those skilled in the art based on the present invention belong to the present invention. The scope of the claim.

Claims (10)

  1. 一种带板管复合换热型蒸发式冷凝器的冷热水机组,包括压缩机、蒸发式冷凝器、节流装置和蒸发器;所述蒸发式冷凝器包括风机、水泵、布水器、集水池;其特征在于:所述蒸发式冷凝器还包括板管复合换热器;所述板管复合换热器由多个板管复合换热片通过进口集管和出口集管连接组成;所述板管复合换热片包括传热板片以及由换热管加工而成的盘管;所述传热板片设有安放槽,该安放槽的形状与盘管的形状匹配;盘管安放于安放槽内,盘管与安放槽之间的间隙填充有导热粘合层。A hot and cold water unit with a tube-tube composite heat exchange type evaporative condenser, comprising a compressor, an evaporative condenser, a throttling device and an evaporator; the evaporative condenser comprises a fan, a water pump, a water distributor, a collecting pool; characterized in that: the evaporative condenser further comprises a plate-tube composite heat exchanger; the plate-tube composite heat exchanger is composed of a plurality of plate-tube composite heat-exchange sheets connected through an inlet header and an outlet header; The plate tube composite heat exchange sheet comprises a heat transfer plate and a coil processed by the heat exchange tube; the heat transfer plate is provided with a seating groove, and the shape of the receiving groove matches the shape of the coil; the coil Placed in the mounting groove, the gap between the coil and the mounting groove is filled with a thermally conductive adhesive layer.
  2. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述导热粘合层为金属填充物。The hot and cold water unit with a tube-tube composite heat exchange type evaporative condenser according to claim 1, wherein the heat conductive adhesive layer is a metal filler.
  3. 根据权利要求2所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述盘管与安放槽之间的间隙小于10毫米。The hot and cold water unit with a plate tube composite heat exchange type evaporative condenser according to claim 2, wherein a gap between the coil and the seating groove is less than 10 mm.
  4. 根据权利要求3所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述传热板片还冲压有若干限位槽和/或定位焊点。The hot and cold water unit with a plate tube composite heat exchange type evaporative condenser according to claim 3, wherein the heat transfer plate is further stamped with a plurality of limiting grooves and/or positioning pads.
  5. 根据权利要求2所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述金属填充物为锌、锡、铝、铜中的一种或多种。The hot and cold water unit with a tube-tube composite heat exchange type evaporative condenser according to claim 2, wherein the metal filler is one or more of zinc, tin, aluminum and copper.
  6. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述导热粘合层为导热粘胶。The hot and cold water unit with a plate tube composite heat exchange type evaporative condenser according to claim 1, wherein the heat conductive adhesive layer is a heat conductive adhesive.
  7. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述压缩机的排气口与蒸发式冷凝器的气体 管连接,蒸发式冷凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机的吸气口连接。The hot and cold water unit with a plate tube composite heat exchange type evaporative condenser according to claim 1, wherein: the exhaust port of the compressor and the gas of the evaporative condenser The tube is connected, and the liquid tube of the evaporative condenser is connected to the liquid tube of the evaporator through a throttling device, and the gas tube of the evaporator is connected to the suction port of the compressor.
  8. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述压缩机的排气口与蒸发式冷凝器的气体管连接,蒸发式冷凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机的吸气口连接,所述冷热水机组设置有第一制冷阀、第二制冷阀、第一热泵阀和第二热泵阀;第一制冷阀设置在压缩机的排气口与蒸发式冷凝器的气体管的连接管路上,第二制冷阀设置在压缩机的吸气口与蒸发器的气体管的连接管路上,第一热泵阀设置在压缩机的排气口与蒸发器的气体管的连接管路上,第二热泵阀设置在压缩机的吸气口与蒸发式冷凝器的气体管的连接管路上。The hot and cold water unit with a plate tube composite heat exchange type evaporative condenser according to claim 1, wherein the exhaust port of the compressor is connected to a gas pipe of the evaporative condenser, and the evaporative condenser The liquid pipe is connected to the liquid pipe of the evaporator through a throttling device, and the gas pipe of the evaporator is connected to the suction port of the compressor, and the hot and cold water unit is provided with a first refrigeration valve, a second refrigeration valve, and a first heat. a pump valve and a second heat pump valve; the first refrigerating valve is disposed on a connecting line of the exhaust port of the compressor and the gas pipe of the evaporating condenser, and the second refrigerating valve is disposed at the suction port of the compressor and the evaporator On the connecting pipe of the gas pipe, the first heat pump valve is disposed on the connecting pipe of the exhaust port of the compressor and the gas pipe of the evaporator, and the second heat pump valve is disposed at the suction port of the compressor and the evaporative condenser On the connecting line of the gas pipe.
  9. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述压缩机的排气口设有第一换向阀,压缩机的吸气口设有第二换向阀;第一换向阀的两个出口分别与蒸发式冷凝器的气体管和蒸发器的气体管连接,第二换向阀的两个进口分别与蒸发式冷凝器的气体管和蒸发器的气体管连接;所述第一、第二换向阀为二位三通换向阀。The hot and cold water unit with a plate-tube composite heat exchange type evaporative condenser according to claim 1, wherein the exhaust port of the compressor is provided with a first reversing valve, and an intake port of the compressor. a second reversing valve is provided; the two outlets of the first reversing valve are respectively connected with the gas pipe of the evaporative condenser and the gas pipe of the evaporator, and the two inlets of the second reversing valve are respectively connected with the evaporative condenser The gas pipe is connected to the gas pipe of the evaporator; the first and second reversing valves are two-position three-way reversing valves.
  10. 根据权利要求1所述的带板管复合换热型蒸发式冷凝器的冷热水机组,其特征在于:所述冷热水机组设置有四通换向阀,四通换向阀的四个接口分别与压缩机排气口、蒸发式冷凝器的气体管、蒸发器的气体管和压缩机的吸气口连接。 The hot and cold water unit with a tube-tube composite heat exchange type evaporative condenser according to claim 1, wherein the hot and cold water unit is provided with a four-way reversing valve and four four-way reversing valves. The interface is respectively connected to a compressor discharge port, a gas pipe of the evaporative condenser, a gas pipe of the evaporator, and an intake port of the compressor.
PCT/CN2015/081400 2015-01-28 2015-06-12 Water chiller-heater unit with tube-and-plate type compound heat exchanging evaporative condenser WO2016119369A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510045115.7 2015-01-28
CN201510045115.7A CN105987534A (en) 2015-01-28 2015-01-28 Cold-and-hot water unit with plate-pipe composite heat-exchange evaporative condenser

Publications (1)

Publication Number Publication Date
WO2016119369A1 true WO2016119369A1 (en) 2016-08-04

Family

ID=56542282

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2015/081400 WO2016119369A1 (en) 2015-01-28 2015-06-12 Water chiller-heater unit with tube-and-plate type compound heat exchanging evaporative condenser

Country Status (2)

Country Link
CN (1) CN105987534A (en)
WO (1) WO2016119369A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108826735A (en) * 2018-08-01 2018-11-16 安徽欧瑞达电器科技有限公司 A kind of routine swimming pool Hot water units

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114739208B (en) * 2022-04-11 2022-12-16 江苏德翔化工机械有限公司 Combined type heat exchanger

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08270131A (en) * 1995-04-03 1996-10-15 Matsushita Electric Works Ltd Structure of heating floor
CN1520509A (en) * 2001-05-01 2004-08-11 ����������÷��-�������� Plate-tube type heat exchanger
CN202056027U (en) * 2011-04-27 2011-11-30 林勇 Liquid impact prevention device for air-cooled heat pump air-conditioning compressor
CN102628626A (en) * 2012-04-26 2012-08-08 广州市华德工业有限公司 Air conditioning dehumidification evaporative type condensation three-work-condition cold and hot water unit
CN202562130U (en) * 2012-04-26 2012-11-28 广州市华德工业有限公司 Air conditioner dehumidification evaporative condensation three-working-condition cold-and-hot water unit
CN204612230U (en) * 2015-01-28 2015-09-02 广州市华德工业有限公司 A kind of water chiller-heater unit of band plate pipe composite heat-exchange type evaporative condenser

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2238410Y (en) * 1995-10-31 1996-10-23 深圳市和利达换热系统工程公司 Three-dimensional internal ribbed elliptic fin heat exchanging pipe
JP2001033120A (en) * 1999-07-19 2001-02-09 Fujitsu General Ltd Multi-room type air conditioner
EP1333952A4 (en) * 2000-09-25 2007-10-31 Showa Denko Kk Method for manufacturing heat exchanger
JP2002361405A (en) * 2000-09-25 2002-12-18 Showa Denko Kk Method for manufacturing heat exchanger
CN201724491U (en) * 2010-06-30 2011-01-26 元纬科技股份有限公司 Ice making tray
CN102135248A (en) * 2011-01-23 2011-07-27 符建 Liquid metal heat dissipation-based high-power LED (Light Emitting Diode) light source with threaded connection structure
CN202032795U (en) * 2011-04-08 2011-11-09 海尔集团公司 Plate and tube condenser for refrigerator and refrigerator
JP2013132675A (en) * 2011-12-27 2013-07-08 Daikin Industries Ltd Method for manufacturing heat exchanger
CN103574965B (en) * 2012-07-20 2016-12-21 广州市华德工业有限公司 A kind of handpiece Water Chilling Units of band filler coupling coil pipe evaporative condenser
CN202770066U (en) * 2012-09-17 2013-03-06 江苏亚光金属制品有限公司 High-efficiency refrigerator evaporator

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08270131A (en) * 1995-04-03 1996-10-15 Matsushita Electric Works Ltd Structure of heating floor
CN1520509A (en) * 2001-05-01 2004-08-11 ����������÷��-�������� Plate-tube type heat exchanger
CN202056027U (en) * 2011-04-27 2011-11-30 林勇 Liquid impact prevention device for air-cooled heat pump air-conditioning compressor
CN102628626A (en) * 2012-04-26 2012-08-08 广州市华德工业有限公司 Air conditioning dehumidification evaporative type condensation three-work-condition cold and hot water unit
CN202562130U (en) * 2012-04-26 2012-11-28 广州市华德工业有限公司 Air conditioner dehumidification evaporative condensation three-working-condition cold-and-hot water unit
CN204612230U (en) * 2015-01-28 2015-09-02 广州市华德工业有限公司 A kind of water chiller-heater unit of band plate pipe composite heat-exchange type evaporative condenser

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108826735A (en) * 2018-08-01 2018-11-16 安徽欧瑞达电器科技有限公司 A kind of routine swimming pool Hot water units
CN108826735B (en) * 2018-08-01 2023-06-30 安徽欧瑞达电器科技有限公司 Conventional swimming pool hot water unit

Also Published As

Publication number Publication date
CN105987534A (en) 2016-10-05

Similar Documents

Publication Publication Date Title
WO2016119365A1 (en) Compound heat exchange evaporative condenser of board pipe
CN103958995B (en) Heat and mass exchanger for liquid desiccant air regulator
CN109154460B (en) Laminated header, heat exchanger, and air conditioner
CN103930747B (en) Plate fin and tube type heat exchanger and there is the refrigerated air-conditioning system of this plate fin and tube type heat exchanger
WO2014012287A1 (en) Air conditioning unit with filler coupling coil pipe evaporative type condenser
WO2014012286A1 (en) Cold water machine group of filler coupling coil pipe evaporative type condenser
CN107003085A (en) Cascade type collector, heat exchanger and air-conditioning device
EP3875878B1 (en) Heat exchanger and refrigeration cycle device
CN106796091A (en) Heat exchanger and conditioner
CN108027223A (en) Cascade type collector, heat exchanger and conditioner
CN105157281A (en) Tube-in-tube evaporative condenser with fins
WO2016119364A1 (en) Tube-and-plate type compound heat exchange sheet and manufacturing method therefor
WO2014012284A1 (en) Filler coupling coil pipe evaporative type condenser
WO2016119369A1 (en) Water chiller-heater unit with tube-and-plate type compound heat exchanging evaporative condenser
WO2016119367A1 (en) Air conditioning unit having tubesheet combined heat-exchanging evaporative condenser
US20230341161A1 (en) A refrigeration system and a method for controlling such a refrigeration system
CN204612230U (en) A kind of water chiller-heater unit of band plate pipe composite heat-exchange type evaporative condenser
CN204612221U (en) A kind of air-conditioner set of band plate pipe composite heat-exchange type evaporative condenser
JP3658677B2 (en) Plate heat exchanger and refrigeration system
CN105823353A (en) High-efficiency condenser
US20230030270A1 (en) A refrigeration system and method
WO2016119366A1 (en) Closed cooling tower having tubesheet combined heat exchange piece
JP2013204913A (en) Heat exchanger
CN209181321U (en) Plate pipe composite heat-exchange type vaporation-type water cooler
CN110748983A (en) Condensation heat exchanger and outdoor unit with same

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15879575

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 15879575

Country of ref document: EP

Kind code of ref document: A1