CN201021877Y - Condensation heat exchanger of heat pump type water heating equipment - Google Patents
Condensation heat exchanger of heat pump type water heating equipment Download PDFInfo
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- CN201021877Y CN201021877Y CNU2007200481948U CN200720048194U CN201021877Y CN 201021877 Y CN201021877 Y CN 201021877Y CN U2007200481948 U CNU2007200481948 U CN U2007200481948U CN 200720048194 U CN200720048194 U CN 200720048194U CN 201021877 Y CN201021877 Y CN 201021877Y
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- refrigerant
- hot water
- heat pump
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 95
- 238000010438 heat treatment Methods 0.000 title abstract description 6
- 230000005494 condensation Effects 0.000 title abstract description 5
- 238000009833 condensation Methods 0.000 title abstract description 5
- 239000003507 refrigerant Substances 0.000 claims abstract description 45
- 238000009826 distribution Methods 0.000 claims abstract description 14
- 238000005452 bending Methods 0.000 claims abstract description 11
- 230000000694 effects Effects 0.000 description 11
- 238000004321 preservation Methods 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种换热器,特别涉及一种热泵式热水设备的冷凝换热器,主要用于目前市场上的热泵式热水设备,使此类设备获得更高的出水温度和能效比。The utility model relates to a heat exchanger, in particular to a condensing heat exchanger for heat pump hot water equipment, which is mainly used for heat pump hot water equipment on the market, so that such equipment can obtain higher outlet water temperature and energy efficiency. Compare.
背景技术 Background technique
在目前使用的各种热水生产设备中,热泵式热水设备以其运行成本低廉、节能、环保、安全等优点,在市场上获得了高速的发展。但是目前市场上的热泵式热水设备,大多采用循环加热方式生产热水,也就是把保温水箱里的水,泵入热泵式热水机组,吸收机组内制冷剂冷凝排放的热量获得升温后,再流回保温水箱,如此不断循环,来提高保温水箱内热水的温度。当保温水箱内的水温升高到50℃时,热泵机组的出水温度在55℃以上,此时制冷剂的冷凝温度超过53℃,已经达到了普通制冷压缩机的工作极限,所以目前市场上的普通热泵式热水设备,实际上很难获得高于50℃的热水。再加上机组进出水温差小,换热效果不良,降低了机组的制热效率,不仅增加能耗,还使制冷压缩机处于高温状态运行,极易损害压缩机。这些缺点大大限制了热泵式热水设备的使用效果。Among the various hot water production equipment currently in use, heat pump hot water equipment has achieved rapid development in the market due to its advantages of low operating cost, energy saving, environmental protection, and safety. However, most of the heat pump water heaters currently on the market use the circulation heating method to produce hot water, that is, the water in the heat preservation water tank is pumped into the heat pump water heater unit, and after absorbing the heat discharged by the condensation of the refrigerant in the unit, the heat is raised. Then flow back to the heat preservation water tank, so that the circulation continues to increase the temperature of the hot water in the heat preservation water tank. When the water temperature in the heat preservation water tank rises to 50°C, the outlet water temperature of the heat pump unit is above 55°C. At this time, the condensation temperature of the refrigerant exceeds 53°C, which has reached the working limit of ordinary refrigeration compressors. It is actually difficult to obtain hot water higher than 50°C for ordinary heat pump hot water equipment. In addition, the temperature difference between the inlet and outlet water of the unit is small, and the heat exchange effect is poor, which reduces the heating efficiency of the unit, not only increases energy consumption, but also makes the refrigeration compressor run at a high temperature, which is very easy to damage the compressor. These shortcomings greatly limit the use effect of heat pump water heating equipment.
实用新型内容Utility model content
本实用新型的目的在于,克服上述现有技术的不足,提供一种使热泵热水机组可以获得更高的出水温度,可改善热泵热水设备中制冷压缩机的运行工况,高效节能,用于热泵式热水设备的换热器。The purpose of this utility model is to overcome the shortcomings of the above-mentioned prior art, and provide a heat pump water heater unit that can obtain a higher outlet water temperature, which can improve the operating conditions of the refrigeration compressor in the heat pump water heater equipment, with high efficiency and energy saving. Heat exchanger for heat pump hot water equipment.
为达上述目的,本实用新型所采用技术方案为,一种热泵式热水设备冷凝换热器,包括壳体和盘管,壳体上设有冷水入口和热水出口,所述壳体被分层板隔成弯曲的水流通道,在该水流通道内水流方向与盘管内制冷剂的流向整体上相反。In order to achieve the above purpose, the technical solution adopted by the utility model is, a heat pump type hot water equipment condensing heat exchanger, including a shell and a coil, the shell is provided with a cold water inlet and a hot water outlet, and the shell is covered by The layered plates are separated into curved water flow channels, and the direction of water flow in the water flow channels is generally opposite to that of the refrigerant in the coil.
本实用新型由于舍弃了循环水式热交换方式,而采用延长热量交换流程的方式对水进行一次性加热,且通过控制使水流方向与制冷剂的流向整体上相反,从而实现了使水温可以升高到与高温制冷剂比较接近的温度,并且使制冷剂的降温效果比较明显以改善制冷压缩机工作条件。Since the utility model abandons the circulating water heat exchange mode, the water is heated once by prolonging the heat exchange process, and the direction of the water flow is opposite to that of the refrigerant as a whole by controlling, so that the water temperature can be raised. The temperature is as high as that of the high-temperature refrigerant, and the cooling effect of the refrigerant is more obvious to improve the working conditions of the refrigeration compressor.
上述的热泵式热水设备冷凝换热器,所述的盘管有多根,它们等距平行排列,且其两端与两根压力分配管相通,制冷剂入口和制冷剂出口设在两根内径远大于盘管内径的压力分配管上。均匀设置多根盘管,可使换热更均匀;压力分配管可使各盘管入口和出口压力接近,以确保每根盘管获得均匀的流量。In the heat pump type hot water equipment condensing heat exchanger described above, there are multiple coils, which are equidistantly arranged in parallel, and their two ends communicate with two pressure distribution pipes, and the refrigerant inlet and refrigerant outlet are located in two On pressure distribution pipes with an inner diameter much larger than the inner diameter of the coil. Evenly setting multiple coils can make the heat exchange more uniform; the pressure distribution pipe can make the inlet and outlet pressures of each coil close to ensure that each coil can obtain a uniform flow.
上述的热泵式热水设备冷凝换热器,所述制冷剂入口和制冷剂出口设在两压力分配管中部。这样可以更好地保证每根盘管获得均匀的流量。In the above-mentioned condensing heat exchanger of heat pump hot water equipment, the refrigerant inlet and refrigerant outlet are arranged in the middle of the two pressure distribution pipes. This better guarantees an even flow to each coil.
上述的热泵式热水设备冷凝换热器,所述的冷水入口设在壳体下部,热水出口设在壳体上部,而制冷剂入口设在壳体上部,制冷剂出口设在壳体下部。这样在保证换热效果的情况下,可进一步使水流更平稳。In the above-mentioned condensing heat exchanger for heat pump hot water equipment, the cold water inlet is arranged at the lower part of the casing, the hot water outlet is arranged at the upper part of the casing, the refrigerant inlet is arranged at the upper part of the casing, and the refrigerant outlet is arranged at the lower part of the casing . In this way, under the condition of ensuring the heat exchange effect, the water flow can be further made more stable.
上述的热泵式热水设备冷凝换热器,所述盘管呈多弯形状,且直段部分相互等距平行,壳体内可以每三层弯曲设置一层分层板。在换热效果满足的情况下,可减少分层板的使用。In the above-mentioned condensing heat exchanger for heat pump hot water equipment, the coil is in a multi-bend shape, and the straight sections are equidistant and parallel to each other, and a layer of layered plates can be arranged every three layers of bending in the shell. When the heat exchange effect is satisfied, the use of layered plates can be reduced.
上述的热泵式热水设备冷凝换热器,所述盘管呈多弯形状,且直段部分相互等距平行,壳体内也可以每二层弯曲设置一层分层板。相比每三层弯曲设置一层分层板换热效果更好。In the above-mentioned condensing heat exchanger for heat pump hot water equipment, the coil is in a multi-bend shape, and the straight sections are equidistant and parallel to each other, and a layer of layered plates can also be arranged every two layers of bending in the shell. Compared with setting one layer of layered plates every three layers of bending, the heat exchange effect is better.
上述的热泵式热水设备冷凝换热器,所述盘管呈多弯形状,且直段部分相互等距平行,壳体内还可以每一层弯曲设置一层分层板。这样换热效果会最好。In the above-mentioned condensing heat exchanger for heat pump hot water equipment, the coil is in the shape of multiple bends, and the straight sections are equidistant and parallel to each other, and a layer of layered plates can be arranged in each layer of bending in the shell. This way the heat exchange effect will be the best.
附图说明 Description of drawings
以下结合附图对本实用新型做进一步具体说明。Below in conjunction with accompanying drawing, the utility model is described in further detail.
本说明书所附图1为本实用新型一种实施例的立体剖视示意图;Accompanying drawing 1 of this specification is a three-dimensional cross-sectional schematic view of an embodiment of the utility model;
图2、图3和图4分别为图1所示实施例在正视、侧视和俯视三个方向的剖视图。Fig. 2, Fig. 3 and Fig. 4 are cross-sectional views of the embodiment shown in Fig. 1 in three directions of front view, side view and plan view respectively.
图中,1是壳体,2是盘管,3是制冷剂入口,4是制冷剂出口,5是冷水入口,6是热水出口,7是压力分配管,8是分层板。In the figure, 1 is the housing, 2 is the coil, 3 is the refrigerant inlet, 4 is the refrigerant outlet, 5 is the cold water inlet, 6 is the hot water outlet, 7 is the pressure distribution pipe, and 8 is the layered plate.
具体实施方式 Detailed ways
在附图1、2、3和4所示实施例中,本实用新型热泵式热水设备冷凝换热器由壳体1、盘管2、制冷剂入口3、制冷剂出口4、冷水入口5、热水出口6、压力分配管7和分层板8构成。制冷剂入口3与热泵热水机组内制冷剂循环回路中的压缩机的制冷剂流出口相联,制冷剂出口4与上述制冷剂循环回路中的干燥过滤器相联,冷水入口5与冷水供水管相联,热水出口6与用水或储水设施相联。盘管2有多根,它们等距并行,可以获得更均匀的换热效果。各盘管直管段布置在同一平面上互相平行,每根盘管的两端分别与两个压力分配管7内腔相联。压力分配管7的内径远比盘管2内径大,以使各盘管2的入口和出口压力相近,以确保每根盘管2获得均匀的流量。在盘管的每层直段之间装有一层分层板8(也可根据设计的换热效果需要每两层或每三层设置一层分层板),分层板8与盘管2的直管段平行,并与各盘管直管段焊接在一起,以增加实际的换热面积,其与盘管直段平行的边与壳体1紧密连接,另两边中一边与壳体紧密连接,另一边只连到盘管的弯管处,留出通道让水从此流过。相邻两块分层板留出的通道口相对,从而形成弯曲的水道,以使水在进入壳体后,能够沿着盘管逐级向上流动,大大改善换热效果。In the embodiment shown in accompanying
在本实用新型中,压缩机排出高温高压的气态制冷剂从制冷剂入口3进入压力分配管7,然后均匀地流入各盘管2,被加热的水从盘管2外流过,吸收制冷剂排出的热量。制冷剂排热后在盘管的某一区间完成冷凝变相为液态,并继续被水冷却降温,然后从制冷剂出口4流出并进入机组制冷剂循环回路中的干燥过滤器。In the utility model, the high-temperature and high-pressure gaseous refrigerant discharged from the compressor enters the pressure distribution pipe 7 from the
冷水从冷水入口5进入,由于受壳体1和分层板8的限制,会沿着盘管2外壁流动,并与制冷剂流动方向整体相反(是指总流向而不是每一段的流向),吸收制冷剂排热后水温逐渐提高,最后高温热水从出口6流出,送入用水或储水设备以供用户使用。本实用新型产品不仅可以提供高温水,也可以通过控制进水的速度来提供低温水。由于水的换热温差大,换热器出水温度高,换热效果好,制冷剂冷凝成为液体后又继续被冷水降温,更有利于制冷剂循环回路中后段的蒸发吸热需要,所以大大提高了机组的制热效率,并改善了压缩机的运行工况。由于水温是逐渐提高的,所以制冷剂在盘管内的冷凝温度比热水出水温度低得多,产出的热水温度也比普通热泵热水机组高得多。从而使热泵热水机组实现了高水温、高效率的目的。The cold water enters from the
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Cited By (1)
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CN110608622A (en) * | 2019-05-20 | 2019-12-24 | 无锡蓝海工程设计有限公司 | Tower type tube bundle heat exchanger |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN110608622A (en) * | 2019-05-20 | 2019-12-24 | 无锡蓝海工程设计有限公司 | Tower type tube bundle heat exchanger |
CN110608622B (en) * | 2019-05-20 | 2020-12-18 | 无锡蓝海工程设计有限公司 | Tower type tube bundle heat exchanger |
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Granted publication date: 20080213 Termination date: 20100202 |