WO2011044757A1 - Method, apparatus and multi-functional system for supplying hot water and warm air simultaneously - Google Patents

Method, apparatus and multi-functional system for supplying hot water and warm air simultaneously Download PDF

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Publication number
WO2011044757A1
WO2011044757A1 PCT/CN2010/001616 CN2010001616W WO2011044757A1 WO 2011044757 A1 WO2011044757 A1 WO 2011044757A1 CN 2010001616 W CN2010001616 W CN 2010001616W WO 2011044757 A1 WO2011044757 A1 WO 2011044757A1
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WO
WIPO (PCT)
Prior art keywords
refrigerant
high temperature
refrigerant gas
gas
temperature refrigerant
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PCT/CN2010/001616
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French (fr)
Chinese (zh)
Inventor
梁显庭
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全联有限公司
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Publication of WO2011044757A1 publication Critical patent/WO2011044757A1/en

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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
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H6/00Combined water and air heaters
    • 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
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/021Indoor unit or outdoor unit with auxiliary heat exchanger not forming part of the indoor or outdoor unit
    • F25B2313/0214Indoor unit or outdoor unit with auxiliary heat exchanger not forming part of the indoor or outdoor unit the auxiliary heat exchanger being used parallel to the indoor unit during heating operation
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers

Definitions

  • the present invention generally relates to a method and apparatus for simultaneously providing hot water and warm air, and a multifunctional system thereof, and more particularly, to a A method and apparatus for providing hot water and warm air and a multi-functional system thereof are realized by utilizing a change in state of the refrigerant.
  • BACKGROUND OF THE INVENTION Currently, water heaters sold on the market are generally electric water heaters, gas water heaters and solar water heaters. Electric water heaters consume large amounts of electricity, are expensive to use, and require a certain amount of preheating time. Solar water heaters cannot be used around the clock, making them inconvenient to use. Gas water heaters are prone to accidents and endanger people's lives.
  • An object of the present invention is to provide a method for simultaneously providing hot water and warm air, comprising: compressing a refrigerant into an initial high-temperature refrigerant gas of not lower than 75 ° C using a compressor; and outputting the compressor
  • the initial high-temperature refrigerant gas is branched into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas through a flow dividing device;
  • the first high-temperature refrigerant gas is input into the multi-channel microtube heat exchanger to exchange heat with the tap water to convert the tap water a hot water of 45 ° C to 60 ° C, converting the first high temperature refrigerant gas into a first refrigerant liquid, and inputting the second high temperature refrigerant gas into the indoor fan to exchange heat with indoor air to provide warm Winding, and converting the second high temperature refrigerant gas into a second refrigerant liquid; and circulating the first refrigerant liquid and the second refrigerant liquid
  • the "compressing the refrigerant to an initial temperature of not lower than 75 ° C using a compressor includes compressing the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C. wherein the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger is performed with tap water.
  • the step of converting the tap water into hot water of 45 ° C to 60 ° C and converting the first high temperature refrigerant gas into the first refrigerant liquid " may include converting the first high temperature refrigerant gas to 30 a first refrigerant liquid of from ° C to 40 ° C.
  • said "the first high-temperature refrigerant gas is supplied to the multi-channel microtube heat exchanger for heat exchange with tap water to convert the tap water to 45t to 60°
  • the step of converting the hot water of C to the first high-temperature refrigerant gas to the first refrigerant liquid may include converting the tap water into hot water of about 55 ° C, and converting the first high-temperature refrigerant gas into a first refrigerant liquid of about 35 ° C.
  • the "the second high-temperature refrigerant gas is supplied to the indoor fan for heat exchange with the indoor air to provide warm air, and the second high-temperature refrigerant gas is converted into The second refrigerant liquid "steps can be And comprising: converting the second high-temperature refrigerant gas into a second refrigerant liquid having a temperature of 20° C. to 40° C., wherein “the second high-temperature refrigerant gas is input into the indoor fan and exchanges heat with the indoor air to The step of providing warm air and converting the second high temperature refrigerant gas to the second refrigerant liquid may include converting the second high temperature refrigerant gas to a second refrigerant liquid having a temperature of about 25 ° C.
  • the flow rate of the first high temperature refrigerant gas is higher than the flow rate of the second high temperature refrigerant gas, wherein a ratio of a flow rate of the first high temperature refrigerant gas to a flow rate of the second high temperature refrigerant gas may be greater than 2.
  • Another object of the present invention is to provide an apparatus for simultaneously providing hot water and warm air, comprising: a compressor that compresses a refrigerant into a high-temperature refrigerant gas of not lower than 75 ° C; a flow dividing device The splitting device divides the initial high-temperature refrigerant gas output by the compressor into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas; a multi-channel microtube heat exchanger, the multi-channel micro The tube heat exchanger exchanges heat between the first high-temperature refrigerant gas and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and converts the first high-temperature refrigerant gas into the first refrigerant a liquid fan, the indoor fan heat exchanges the second high temperature refrigerant gas with the indoor air to provide warm air, and converts the second high temperature refrigerant gas into a second refrigerant liquid; and an air-cooled evaporator, the first a
  • the multi-channel microtube heat exchanger can convert the first high-temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C. Wherein the multi-channel microtube heat exchanger converts the tap water into hot water of about 55 ° C and will The first high temperature refrigerant gas is converted to a first refrigerant liquid of about 35 °C.
  • the indoor fan can convert the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of 20 ° C to 40. Wherein, the indoor fan can convert the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of about 25 °C.
  • a liquid storage device is further connected between the refrigerant outlet end of the multi-channel microtube heat exchanger and the refrigerant outlet end of the indoor fan and the refrigerant inlet end of the air-cooled evaporator, the liquid storage device a first refrigerant inlet end and a second refrigerant inlet end are respectively connected to a refrigerant outlet end of the multi-channel microtube heat exchanger and a refrigerant outlet end of the indoor fan, and a refrigerant outlet end of the liquid storage device is The inlet end of the refrigerant of the air-cooled evaporator is connected.
  • a gas-liquid separator is connected in series between the refrigerant outlet end of the air-cooled evaporator and the refrigerant inlet end of the compressor.
  • the flow dividing device further comprises a refrigerant pressure releasing end, and an instantaneous pressure balancer is further connected between the refrigerant outlet end of the air-cooling evaporator and the refrigerant pressure releasing end of the flow dividing device.
  • the flow rate of the first high temperature refrigerant gas may be higher than the flow rate of the second high temperature refrigerant gas.
  • the ratio of the flow rate of the first high-temperature refrigerant gas to the flow rate of the second high-temperature refrigerant gas may be greater than 2.
  • the multi-channel microtube heat exchanger comprises at least three refrigerant lines in parallel. It is still another object of the present invention to provide a multi-functional system comprising: a compressor including a refrigerant inlet end and a refrigerant outlet end, the compressor compressing refrigerant from a refrigerant inlet end of the compressor to the compressor The outlet end of the refrigerant outputs an initial high-temperature refrigerant gas of not less than 75t; the first flow dividing device, the first end of the first flow dividing device is connected to the refrigerant outlet end of the compressor, the first flow dividing device Distributing the initial high temperature refrigerant gas output by the compressor into a first high temperature refrigerant gas and a second high temperature refrigerant gas respectively outputted from the second end and the third end of the first flow dividing device; a heat exchanger, wherein a refrigerant inlet end of the multi-channel microtube heat exchanger is connected to a second end of the first
  • the compressor compresses the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C.
  • a liquid storage device is further connected between the refrigerant outlet end of the multi-channel microtube heat exchanger and the second end of the indoor fan and the first end of the air-cooled evaporator, the liquid storage device The first end and the second end are respectively connected to the refrigerant outlet end of the multi-channel microtube heat exchanger and the second end of the indoor fan, and the third end of the liquid storage device and the air-cooled evaporator The first end is connected.
  • a gas-liquid separator is further connected in series between the second end of the air-cooled evaporator and the refrigerant inlet end of the compressor, wherein the second end of the air-cooled evaporator passes the second shunt
  • a fourth end and a second end of the apparatus are connected to an inlet end of the gas-liquid separator, and an outlet end of the gas-liquid separator is connected to an inlet end of the compressor.
  • the first flow dividing device further comprises a fourth end for the pressure relief of the refrigerant, and an instantaneous pressure balance is further bridged between the inlet end of the gas-liquid separator and the fourth end of the first flow dividing device Device.
  • FIG. 1 is a schematic structural diagram of an apparatus 100 for providing both hot and warm air in accordance with the present invention.
  • FIG. 2 is a block diagram of a method 200 of providing both hot and warm air in accordance with the present invention.
  • Figure 3 is a schematic view showing the structure of a multi-channel microtube heat exchanger 1 1 according to the present invention.
  • Fig. 4 is a partial enlarged view of a portion A in Fig. 3.
  • Figure 5 is a cross-sectional view of the refrigerant line 21 in the multi-channel microtube heat exchanger 11 in accordance with the present invention.
  • Figure 6 is a block diagram showing the structure of a multi-function device 1000 in accordance with the present invention.
  • FIG 7 is a schematic illustration of one embodiment of a liquid storage device 114 of a multi-function device 1000 in accordance with the present invention.
  • DETAILED DESCRIPTION OF THE INVENTION In the following description, numerous specific details are set forth However, it will be apparent to those skilled in the art that the present invention may be practiced without these specific details. Moreover, well-known structures and devices are shown in block diagram form. In this regard, the particular exemplary embodiments shown are not intended to limit the invention, but are merely illustrative. Therefore, the scope of the invention is not to be limited Referring to Figure 1, there is shown a block diagram of a device 100 for providing both hot and warm air in accordance with the present invention.
  • the apparatus 100 includes a compressor 10, a flow dividing device 9, a multi-channel microtube heat exchanger 11, an indoor fan 12, an air-cooled evaporator 13, a reservoir 14, a gas-liquid separator 15, and an instantaneous pressure balancer 16.
  • the refrigerant outlet end 10a of the compressor 10 is connected to the refrigerant inlet end 9a of the flow dividing device 9.
  • the first refrigerant outlet end 9b of the flow dividing device 9 is connected to the refrigerant inlet end 11a of the multi-channel microtube heat exchanger 11.
  • the second refrigerant outlet end 9c of the flow dividing device 9 is connected to the refrigerant inlet end 12a of the indoor fan 12.
  • the refrigerant outlet end l ib of the multi-channel microtube heat exchanger 11 is connected to the first refrigerant inlet end 14a of the accumulator 14.
  • the refrigerant outlet end 12b of the indoor fan 12 is connected to the second refrigerant inlet end 14b of the accumulator 14.
  • the refrigerant outlet end 14c of the accumulator 14 is connected to the refrigerant inlet end 13a of the air-cooled evaporator 13.
  • the refrigerant outlet end 13b of the air-cooled evaporator 13 is connected to the refrigerant inlet end 15a of the gas-liquid separator 15.
  • the refrigerant outlet end 15b of the gas-liquid separator 15 is connected to the inlet end 10b of the compressor 10.
  • an instantaneous pressure balancer 16 is further bridged between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device.
  • 11c is the water inlet of tap water (such as municipal tap water or other similar domestic water)
  • l id is the outlet of heated tap water.
  • the refrigerant is compressed by the compressor 10 into an initial high-temperature refrigerant gas (at 10a) of not lower than 75 ° C; and the initial high-temperature refrigerant gas output from the compressor 10 is passed through the flow dividing device 9 Dividing into a first high-temperature refrigerant gas (%) and a second high-temperature refrigerant gas (at 9c); and introducing the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger 11 to exchange heat with tap water to make the tap water Converting to hot water (l id) of 45 ° C to 60 ° C, converting the first high temperature refrigerant gas into a first refrigerant liquid (at ib), and inputting the second high temperature refrigerant gas into the chamber
  • the fan 12 exchanges heat with indoor air to provide warm air, and converts the second high temperature refrigerant gas into a second refrigerant liquid (at 12b); and passes the first refriger
  • the step of "compressing the refrigerant into an initial high-temperature refrigerant gas of not lower than 75 ° C using a compressor” includes compressing the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C ( 10a).
  • the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger and the tap water is performed, so that the tap water is converted into hot water (l id) of 45 ° C to 60 ° C
  • the step of converting the first high-temperature refrigerant gas into the first refrigerant liquid may include converting the first high-temperature refrigerant gas into a first refrigerant liquid (at a position of 1 ib) of 30 ° C to 40 ° C.
  • the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger and the tap water is performed to convert the tap water into hot water of 45 ° C to 60 ° C
  • the The step of converting a high temperature refrigerant gas into the first refrigerant liquid may include converting the tap water to hot water (at 1 id) of about 55 ° C, and converting the first high temperature refrigerant gas to about 35 ° C
  • the "the second high-temperature refrigerant gas is input into the indoor fan 12 to exchange heat with the indoor air to provide warm air, and the second high-temperature refrigerant gas is converted into the second refrigerant liquid (at 12b)"
  • the step may include converting the second high temperature refrigerant gas to a second refrigerant liquid (at 12b) at a temperature of from 20 °C to 40 °C.
  • the step of "inputting the second high-temperature refrigerant gas into the indoor fan 12 to exchange heat with the indoor air to provide warm air and converting the second high-temperature refrigerant gas into the second refrigerant liquid” may include:
  • the second high temperature refrigerant gas is converted to a second refrigerant liquid (at 12b) at a temperature of about 25 °C.
  • the flow rate of the first high temperature refrigerant gas is higher than the flow rate of the second high temperature refrigerant gas.
  • the ratio of the flow rate of the first high-temperature refrigerant gas to the flow rate of the second high-temperature refrigerant gas may be greater than 2.
  • the examples of the flow rate of the first high-temperature refrigerant gas and the flow rate of the second high-temperature refrigerant gas are merely used to illustrate the present invention, and the present invention is not limited thereto.
  • the flow rate of the first high temperature refrigerant gas may also be smaller than the flow rate of the second high temperature refrigerant gas, the flow rate of the first high temperature refrigerant gas and the second high temperature refrigerant gas
  • the flow ratio can also be greater than a value of 3, 4 or greater.
  • the structure and parameters employed in the above embodiments not only provide simultaneous hot water and warm air, but also increase the flexibility and convenience of adjustment control and operation.
  • a temperature regulating device or pre-cooling may be additionally provided between the second refrigerant outlet end 9c and the refrigerant inlet end 12a of the indoor fan 12.
  • Device (not shown). If it is used for general indoor heating, in addition to adjusting the flow distribution, the high temperature gas of the second refrigerant outlet end 9c may be additionally pre-cooled to a medium temperature refrigerant liquid of not less than about 35 ° C and then indoor air. Exchange to get the warm air in the most comfortable section of centuries.
  • the above structures and parameters were determined by the inventors of the present invention through a large number of unconventional experiments and studies.
  • Figure 2 is a block diagram of a method 200 for providing both hot and warm air in accordance with the present invention. The method includes the following steps:
  • Step 201 compressing the refrigerant into an initial high-temperature refrigerant gas of not less than 75t by using a compressor;
  • Step 202 The initial high-temperature refrigerant gas output by the compressor is branched into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas through a flow dividing device;
  • Step 203 Perform heat exchange between the first high-temperature refrigerant gas and the multi-channel micro-tube heat exchanger and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and make the first high temperature Converting the refrigerant gas into a first refrigerant liquid, and introducing the second high-temperature refrigerant gas into the indoor fan to exchange heat with the indoor air to provide warm air and converting the second high-temperature refrigerant gas into the second refrigerant liquid;
  • Step 204 Circulate the first refrigerant liquid and the second refrigerant liquid to the compressor after passing through an air-cooled evaporator and a gas-liquid separator.
  • the step 201 may include compressing the refrigerant to a high temperature refrigerant gas of 80 ° C to 90 ° C.
  • the step 203 may include converting the first high temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C. Therein, it may include converting the tap water into hot water of about 55 ° C and converting the first high temperature refrigerant gas into a first refrigerant liquid of about 35 ° C.
  • the step 203 may further include converting the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of 20 ° C to 40 ° C. Wherein, the second high temperature refrigerant gas may be converted into a second refrigerant liquid having a temperature of about 25 °C. See Figures 3 to 5.
  • 3 is a schematic structural view of a multi-channel microtube heat exchanger 11 according to the present invention.
  • Fig. 4 is a partial enlarged view of a portion A in Fig. 3.
  • Figure 5 is a cross-sectional view of the refrigerant line 21 in the multi-channel microtube heat exchanger 11 in accordance with the present invention.
  • the multi-channel microtube heat exchanger 11 includes a plurality of refrigerant tubes 21 which are in the shape of a coil and which are provided with a water pipe 22 for heat exchange therewith.
  • the water pipe 22 is provided with a heating passage formed by the water inlet 11c and the water outlet l id, so that the water in the water pipe 22 passes through the multi-channel micro-tube heat exchanger 11 to exchange heat to hot water, and flows out from the water outlet l id for supply. use.
  • a thermostat 17 is installed on the water outlet l id to control the outlet water temperature within a prescribed range.
  • a sleeve 23 for preventing refrigerant from leaking into the water is provided between the refrigerant pipe 21 and the water pipe 22, and a refrigerant leakage alarm device 7 is provided at the end of the casing 23.
  • the refrigerant line 21 leaks, the refrigerant enters the sleeve 23 and is alarmed by the refrigerant leakage alarm device 7 at the end of the sleeve 23 to ensure that the water is free from contamination and safer to use.
  • the refrigerant inlet 8 is provided at the refrigerant inlet end 11a of the multi-channel microtube heat exchanger 11 to make the refrigerant entering the plurality of refrigerant lines 21 more uniform and to increase the pressure.
  • the power is turned on frequently, and the standby time after the shutdown is shortened, at the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device 9.
  • An instantaneous pressure balancer 16 is also connected across.
  • the flow dividing device 9 can be realized by an electromagnetic four-way valve, but the invention is not limited thereto. Those skilled in the art will appreciate that other shunting devices, proportional valves, etc. that meet the functional requirements of the present invention can be used.
  • the first high temperature gas from the first refrigerant outlet end 9b of the flow dividing device 9 enters the multi-channel microtube heat exchanger 11, more
  • the outside of the refrigerant line 21 in the passage microtube heat exchanger 11 is covered with a water pipe 22 for heat exchange therewith.
  • the high-temperature refrigerant in the refrigerant pipe 21 transfers heat to the water to be used as hot water.
  • the indoor fan 12 supplies the second high-temperature refrigerant gas from the second refrigerant outlet end 9c of the flow dividing device 9 to heat exchange with the indoor air to provide heating.
  • the refrigerant liquid subjected to heat exchange by the multi-channel microtube heat exchanger 11 and the indoor fan 12 is sent to the air-cooled evaporator 13.
  • the refrigerant gas evaporates to become a gas, and is sucked by the compressor 10, and is compressed to become a high-temperature high-pressure refrigerant gas. In this way, by continuously circulating, hot water and heating can be continuously supplied for use at the same time.
  • a balance line 18 is disposed between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device. When the compressor 10 is de-energized, an instantaneous pressure balancer is provided on the balance line 18.
  • the present invention is exemplified by bridging the instantaneous pressure balancer 16 between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device 9, but it should be understood by those skilled in the art.
  • Other connection means are also possible, for example, bridging the instantaneous pressure balancer 16 between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant outlet end 10a of the compressor 10.
  • the present invention is provided with a supercharging device 8, and as shown in Figs. 3 and 4, the refrigerant entering the refrigerant line 21 is made more uniform, and a plurality of refrigerant lines 21 are installed in the water pipe 22.
  • the surfaces of the refrigerant pipe 21 and the water pipe 22 are made uneven, whereby the water in the refrigerant pipe 21 and the water pipe 22 can be turbulent during use, so that heat can be quickly transferred, and excellent heat transfer efficiency can be achieved.
  • a thermostat 17 is disposed on the water outlet l id of the water pipe 22, and the water temperature is monitored by the temperature sensor and the flow rate of the refrigerant in the refrigerant pipe 21 is controlled by the control circuit to achieve the purpose of controlling the water temperature.
  • the multi-channel microtube heat exchanger 11 is provided with a leak-proof casing 23 which prevents refrigerant and oil from entering the water when the refrigerant pipe 21 leaks during operation to ensure the safety of the user.
  • the refrigerant leakage alarm device 7 is a sleeve that is outside the end of the refrigerant line 21 to isolate the water tube 22 from the refrigerant line 21.
  • the refrigerant pipe leaks the refrigerant and the refrigerating oil enter the casing 23.
  • the pressure sensing system can cause the system to alarm to ensure safe use.
  • the multi-channel microtube heat exchanger comprises at least three refrigerant lines 21 in parallel.
  • three parallel refrigerant lines 21 are taken as an example in FIG. 4, those skilled in the art can understand that the present invention is not limited thereto, and four, five, six or more parallel or serial/parallel refrigerant tubes are not limited thereto.
  • Road 21 is possible.
  • the cross section of the plurality of refrigerant lines 21 is not limited to a circular shape, and different diameters and/or cross sections may be employed as long as the heat exchange parameter requirements of the present invention are satisfied.
  • the indoor fan 12 of the present invention may be an indoor fan of a general air conditioner, or a fan specially designed to exchange heat with indoor air, and the invention is not limited thereto.
  • the air-cooled evaporator 13 of the present invention may be a corresponding device of a conventional air conditioner (such as a radiator of an outdoor unit of a split air conditioner), or a specially designed air-cooled evaporator, and the invention is not limited thereto.
  • Figure 6 is a multi-functional, combined system according to the present invention, which not only achieves "hot water + warm air” And the function of "cooling + hot water”, it is also convenient to realize a single "hot water", “cooling” or “warm air” and other functions.
  • the multi-function, modular system 1000 will now be described with reference to FIG.
  • a multi-functional system 1000 comprising: a compressor 110, the compressor including a refrigerant inlet end 110b and a refrigerant outlet end 110a, the compressor 110 compressing a refrigerant from a refrigerant inlet end 110b of the compressor into a refrigerant An initial high temperature refrigerant gas of not less than 75 ° C outputted from the refrigerant outlet end 110a of the compressor 110; a first flow dividing device 109, a first end 109a of the first flow dividing device and the refrigerant of the compressor 110 The outlet end 110a is connected, and the first flow dividing device 109 branches the initial high-temperature refrigerant gas output by the compressor 110 into a first output from the second end 109b and the third end 109c of the first flow dividing device, respectively.
  • a multi-channel microtube heat exchanger 111 the refrigerant inlet end 111a of the multi-channel microtube heat exchanger 111 is connected to the second end 109b of the first flow dividing device 109,
  • the multi-channel microtube heat exchanger 111 exchanges heat between the first high-temperature refrigerant gas and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and the first high-temperature refrigerant gas Converted from the above a first refrigerant liquid outputted from the refrigerant outlet end 111b of the passage microtube heat exchanger 111; a second flow dividing device 119, a first end 119a of the second flow dividing device 119 and a third end 109c of the first flow dividing device 109 Connected to the indoor fan 112, the first end 112a of the indoor fan 112 is connected to the third end 119c of the second diverting
  • the indoor fan 112 exchanges heat between the second high temperature refrigerant gas and the indoor air to provide warm air, and convert the second high temperature refrigerant gas into a slave a second refrigerant liquid outputted from the first end 112a of the indoor fan 112, the first refrigerant liquid and the second refrigerant liquid passing through the air-cooled evaporator 113 and passing through the second end of the second shunt device 119 119b and fourth end 119d are circulated to the refrigerant inlet end HObc of the compressor 110, wherein when the first end 119a and the fourth end 119d of the second diverting device 119 are in communication and the first from the first When the second high temperature refrigerant gas of
  • the two end 11% and third end 119c are circulated to the refrigerant inlet end 110b of the compressor 110.
  • the compressor compresses the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C.
  • a liquid storage may be connected between the refrigerant outlet end 11b of the multi-channel microtube heat exchanger 11 1 and the second end 112b of the indoor fan 112 and the first end 113a of the air-cooled evaporator 113.
  • the first end 114a and the second end 114b of the liquid storage device 114 are respectively connected to the refrigerant outlet end 1 1 lb of the multi-channel microtube heat exchanger 111 and the second end 112b of the indoor fan 1 12 Connected, the third end 14c of the liquid storage device 14 is connected to the first end 113a of the air-cooled evaporator 113.
  • a gas-liquid separator 115 may be connected in series between the second end 113b of the air-cooled evaporator 1 13 and the refrigerant inlet end 110b of the compressor 110, wherein the second end of the air-cooled evaporator 1 13 113b is connected to the inlet end 115a of the gas-liquid separator 115 through the fourth end 119d and the second end 119b of the second flow dividing device 1 19, the outlet end 1 15b of the gas-liquid separator 115 is The inlet ends 1 10b of the compressor 110 are connected.
  • the first flow dividing device 109 further includes a fourth end 109d for refrigerant pressure relief, and is also bridged between the inlet end 115a of the gas-liquid separator 115 and the fourth end 109d of the first flow dividing device 109.
  • FIG. 7 is a schematic illustration of one embodiment of the above described liquid storage device 114. Among them, including the liquid storage tank 1 140, the filter
  • a single "hot water” (the refrigerant is all output from 109b) can be realized, and a single “refrigerating wind (the refrigerant is all output from 109c via 119d)” or a single “Warm air (all refrigerants are output from 109c via 119c)" without changing the basic structure of the system. Therefore, it should be understood by those skilled in the art that any of the first high temperature refrigerant gas and the second high temperature refrigerant gas which are branched as mentioned in the technical solution of the present invention may be zero.
  • first and second flow dividing devices 109, 19 of the present invention can be implemented by an electromagnetic four-way valve, but the invention is not limited thereto.
  • shunting devices, proportional valves, etc. that meet the functional requirements of the present invention can be used.
  • the other components are similar to those described above with respect to FIGS. 1 to 5 and will not be described again.
  • the embodiment of the present invention achieves both hot water and warm air and various other functions in a relatively simple structure, parameters, and a manner that can be easily controlled and adjusted, thereby achieving safety, energy saving, and environmental protection. It is also very convenient to achieve this function on existing air conditioning and refrigeration systems with a small amount of work. Maximize application space. While the invention has been described with respect to the embodiments, the modifications The appended claims are to be construed as covering all such modifications and modifications

Abstract

A method, apparatus and multi-functional system for supplying hot water and warm air simultaneously are provided. Specifically, a method for supplying hot water and warm air simultaneously includes: refrigerant is compressed to initial high temperature refrigerant gas no less than 75℃ by a compressor (10, 110); the initial high temperature refrigerant gas is divided into first high temperature refrigerant gas and second high temperature refrigerant gas by a flow distribution device (9, 109); the first high temperature refrigerant gas is sent to a multi-channel micro-tube heat exchanger (11, 111) and exchanges heat with tap water to turn the tap water into hot water with a temperature of 45~60℃, and the first high temperature refrigerant gas is transformed into first refrigerant liquid, while the second high temperature refrigerant gas is sent to an indoor fan (12,112) and exchanges heat with room air to supply warm air, and the second high temperature refrigerant gas is transformed into second refrigerant liquid; and the first and second refrigerant liquid is circulated to the compressor (10, 110) after having passed an air-cooled evaporator (13, 113) and a gas-liquid separator (15, 115).

Description

说明书 一种同时提供热水和暖风的方法和装置及其多功能系统 技术领域 本发明总地涉及同时提供热水和暖风的方法和装置及其多功能系统, 并且更具体地, 涉及一种利用冷媒的物态变化来同时实现提供热水和暖风的方法和装置及其多功能系统。 背景技术 目前, 市场上销售的热水器一般是电热水器、 燃气热水器和太阳能热水器。 电热水器 耗电量大、 使用成本高, 而且需要一定的预加热时间。 太阳能热水器无法全天候使用, 带 来使用不便。 燃气热水器容易发生事故, 危害人的生命安全。 近年来, 出现了利用冷媒的物态变化来加热水的热水机, 甚至出现了在制冷时可以同 时提供热水的即热式冷媒热水机。这些设备的出现,在一定程度上提高了能源的利用效率。 然而, 利用冷媒的物态变化来同时实现提供热水和暖风的方法及其装置一直没有能够实 现。 另外, 目前的冷媒热水机在能源的利用效率方面仍有提高的潜力可以挖掘。 本发明的申请人己经另案提出了一种基本上呈串联布置的能同时实现提供热水和暖 风的方法及其装置, 获得了很好的节能效果。 但是, 在使用灵活性和操作上还有进一步改 进的空间。 因此, 存在对安全、 环保、 节能和易于操控的、 能同时实现提供热水和暖风的方法及 其装置的需求。 另外, 也存在对多功能组合式热水、 暖风、 冷风 (制冷) 系统的需求。 发明内容 本发明的一个目的是提供一种同时提供热水和暖风的方法, 包括: 采用压缩机将冷媒 压缩为不低于 75°C的初始高温冷媒气体;将所述压缩机输出的所述初始高温冷媒气体通过 分流装置分流为第一高温冷媒气体和第二高温冷媒气体;将所述第一高温冷媒气体输入多 通道微管换热器与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使 所述第一高温冷媒气体转换为第一冷媒液体, 以及将所述第二高温冷媒气体输入室内风机 与室内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转化为第二冷媒液体; 以及将所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器和气液分离器后循环至所 述压缩机。 根据本发明的一个实施方案,所述"采用压缩机将冷媒压缩为不低于 75°C的初始高温 冷媒气体" 的步骤包括将冷媒压縮为 80°C至 90°C的初始高温冷媒气体。 其中, 所述 "将所述第一高温冷媒气体输入多通道微管换热器与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为第一冷媒 液体" 的步骤可以包括使所述第一高温冷媒气体转换为 30°C至 40°C的第一冷媒液体。 其 中, 所述"将所述第一高温冷媒气体输入多通道微管换热器与自来水进行热交换, 以使所 述自来水转换为 45t至 60°C的热水, 并使所述第一高温冷媒气体转换为第一冷媒液体" 的步骤可以包括使所述自来水转换为约 55°C的热水,并使所述第一高温冷媒气体转换为约 35°C的第一冷媒液体。 ' 其中, 所述"将所述第二高温冷媒气体输入室内风机与室内空气进行热交换, 以提供 暖风, 并使所述第二高温冷媒气体转化为第二冷媒液体"的步骤可以包括使所述第二高温 冷媒气体转化为温度 20°C至 40°C的第二冷媒液体。 其中, 所述 "将所述第二高温冷媒气 体输入室内风机与室内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转化为 第二冷媒液体"的步骤可以包括使所述第二高温冷媒气体转化为温度约 25°C的第二冷媒液 体。 根据本发明的另一个实施方案,所述第一高温冷媒气体的流量高于所述第二高温冷媒 气体的流量。其中, 所述第一高温冷媒气体的流量与所述第二高温冷媒气体的流量之比可 以大于 2。 本发明的另一个目的是提供一种同时提供热水和暖风的装置, 包括: 压缩机, 所述压 缩机将冷媒压缩为不低于 75°C的高温冷媒气体;分流装置,所述分流装置将所述压缩机输 出的所述初始高温冷媒气体分流为第一高温冷媒气体和第二高温冷媒气体;多通道微管换 热器, 所述多通道微管换热器将所述第一高温冷媒气体与自来水进行热交换, 以使所述自 来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为第一冷媒液体; 室内 风机, 所述室内风机将第二高温冷媒气体与室内空气进行热交换, 以提供暖风, 并使第二 高温冷媒气体转化为第二冷媒液体; 以及风冷蒸发器, 所述第一冷媒液体和所述第二冷媒 液体通过风冷蒸发器后循环至所述压缩机; 其中, 所述压缩机的出口端与所述分流装置的 冷媒入口端相连,所述分流装置的第一冷媒出口端与所述多通道微管换热器的冷媒入口端 相连, 所述分流装置的第二冷媒出口端与所述室内风机的冷媒入口端相连, 所述多通道微 管换热器的冷媒出口端和所述室内风机的冷媒出口端与所述风冷蒸发器的冷媒入口端相 连, 所述风冷蒸发器的冷媒出口端被连接到所述压缩机的入口端。 根据本发明的一个实施方案, 所述压缩机将冷媒压缩为 80°C至 90°C的初始高温冷媒 气体。 其中, 所述多通道微管换热器可以将所述第一高温冷媒气体转换为 30°C至 40°C的第 一冷媒液体。其中所述多通道微管换热器可以将所述自来水转换为约 55°C的热水,并且将 所述第一高温冷媒气体转换为约 35°C的第一冷媒液体。 其中, 所述室内风机可以将所述第二高温冷媒气体转化为温度 20°C至 40 的第二冷 媒液体。其中,所述室内风机可以将所述第二高温冷媒气体转化为温度约 25°C的第二冷媒 液体。 其中,在所述多通道微管换热器的冷媒出口端和所述室内风机的冷媒出口端与所述风 冷蒸发器的冷媒入口端之间还连接有储液装置,所述储液装置的第一冷媒入口端和第二冷 媒入口端分别与所述多通道微管换热器的冷媒出口端和所述室内风机的冷媒出口端相连, 所述储液装置的冷媒出口端与所述风冷蒸发器的冷媒入口端相连。 其中,在所述风冷蒸发器的冷媒出口端与所述压缩机的冷媒入口端之间还串接有气液 分离器。 其中, 所述分流装置还包括冷媒泄压端, 在所述风冷蒸发器的冷媒出口端与所述分流 装置的所述冷媒泄压端之间还跨接有瞬间压力平衡器。 根据本发明的另一个实施方案,所述第一高温冷媒气体的流量可以高于所述第二高温 冷媒气体的流量。其中, 所述第一高温冷媒气体的流量与所述第二高温冷媒气体的流量之 比可以大于 2。 根据本发明的另一个实施方案, 所述多通道微管换热器包括至少并行的三条冷媒管 路。 本发明的再一个目的在于提供一种多功能系统, 包括: 压缩机, 包括冷媒入口端和冷 媒出口端,所述压缩机将来自所述压缩机的冷媒入口端的冷媒压缩为从所述压缩机的冷媒 出口端输出的不低于 75t的初始高温冷媒气体;第一分流装置,所述第一分流装置的第一 端与所述压缩机的所述冷媒出口端相连,所述第一分流装置将所述压缩机输出的所述初始 高温冷媒气体分流为分别从所述第一分流装置的第二端和第三端输出的第一高温冷媒气 体和第二高温冷媒气体; 多通道微管换热器, 所述多通道微管换热器的冷媒入口端与所述 第一分流装置的第二端相连,所述多通道微管换热器将所述第一高温冷媒气体与自来水进 行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换 为从所述多通道微管换热器的冷媒出口端输出的第一冷媒液体; 第二分流装置, 所述第二 分流装置的第一端与所述第一分流装置的第三端相连; 室内风机, 所述室内风机的第一端 与所述第二分流装置的第三端相连; 以及风冷蒸发器, 所述多通道微管换热器的冷媒出口 端和所述室内风机的第二端与所述风冷蒸发器的第一端相连,所述风冷蒸发器的第二端通 过所述第二分流装置的第四端和第二端被连接到所述压缩机的入口端,所述风冷蒸发器的 第一端与所述第二分流装置的第四端相连; 其中, 当所述第二分流装置的第一端和第三端 联通并将所述来自所述第一分流装置的第三端的所述第二高温冷媒气体传递到所述第二 分流装置的第三端时, 所述室内风机将所述第二高温冷媒气体与室内空气进行热交换, 以 提供暖风,并使所述第二高温冷媒气体转化为从所述室内风机的第一端输出的第二冷媒液 体,所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器后通过所述第二分流装置的联 通的第二端和第四端循环至所述压缩机的所述冷媒入口端; 其中, 当所述第二分流装置的 第一端和第四端联通并将所述来自所述第一分流装置的第三端的所述第二高温冷媒气体 传递到所述第二分流装置的第四端时,所述风冷蒸发器将所述第二高温冷媒气体转化为从 风冷蒸发器的第一端输出的第二冷媒液体,所述第一冷媒液体和所述第二冷媒液体通过室 内风机蒸发吸热以通过和室内空气交换后提供冷气,然后通过所述第二分流装置的联通的 第二端和第三端循环至所述压缩机的所述冷媒入口端。 根据本发明的一个实施方案, 所述压缩机将冷媒压缩为 80°C至 90°C的初始高温冷媒 气体。 其中,在所述多通道微管换热器的冷媒出口端和所述室内风机的第二端与所述风冷蒸 发器的第一端之间还连接有储液装置,所述储液装置的第一端和第二端分别与所述多通道 微管换热器的冷媒出口端和所述室内风机的第二端相连,所述储液装置的第三端与所述风 冷蒸发器的第一端相连。 其中,在所述风冷蒸发器的第二端与所述压缩机的冷媒入口端之间还串接有气液分离 器,其中所述风冷蒸发器的第二端通过所述第二分流装置的第四端和第二端被连接到所述 气液分离器的入口端, 所述气液分离器的出口端与所述压缩机的入口端相连。 其中, 所述第一分流装置还包括用于冷媒泄压的第四端, 在所述气液分离器的入口端 与所述第一分流装置的第四端之间还跨接有瞬间压力平衡器。 本领域技术人员可以理解, 该多功能系统不但可以实现 "热水 +暖风" 的功能和 "制 冷 +热水" 的功能, 而且通过调节所述第一和第二分流装置的工作方式, 还可以实现 "热 水" 、 "制冷"和 "暖风"等各种功能, 而不需改变系统基本结构。 本发明的实施方案以简单、 易于操控和调节的方式实现了同时提供热水和暖风, 不但 达到了安全、节能和环保的目的, 而且非常便于以较小的工作量在现有的空调和制冷系统 上实现。 附图说明 通过参照对本发明的实施方案的图示说明可以更好地理解本发明, 在附图中- 图 1为根据本发明的同时提供热水和暖风的装置 100的结构示意图。 BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention generally relates to a method and apparatus for simultaneously providing hot water and warm air, and a multifunctional system thereof, and more particularly, to a A method and apparatus for providing hot water and warm air and a multi-functional system thereof are realized by utilizing a change in state of the refrigerant. BACKGROUND OF THE INVENTION Currently, water heaters sold on the market are generally electric water heaters, gas water heaters and solar water heaters. Electric water heaters consume large amounts of electricity, are expensive to use, and require a certain amount of preheating time. Solar water heaters cannot be used around the clock, making them inconvenient to use. Gas water heaters are prone to accidents and endanger people's lives. In recent years, there has been a hot water machine that uses a change in state of the refrigerant to heat the water, and even a hot-type refrigerant water heater that can simultaneously supply hot water during cooling has appeared. The emergence of these devices has improved the efficiency of energy use to a certain extent. However, the method and apparatus for simultaneously providing hot water and warm air using the change of the state of the refrigerant have not been realized. In addition, the current refrigerant hot water machine has the potential to improve in terms of energy utilization efficiency. The applicant of the present invention has separately proposed a method and a device for simultaneously providing hot water and warm air which are arranged substantially in series, and a good energy saving effect is obtained. However, there is room for further improvement in terms of flexibility and operation. Therefore, there is a need for a method and apparatus for providing hot water and warm air that is safe, environmentally friendly, energy-saving, and easy to handle. In addition, there is a need for a multifunctional combined hot water, warm air, and cold air (refrigeration) system. SUMMARY OF THE INVENTION An object of the present invention is to provide a method for simultaneously providing hot water and warm air, comprising: compressing a refrigerant into an initial high-temperature refrigerant gas of not lower than 75 ° C using a compressor; and outputting the compressor The initial high-temperature refrigerant gas is branched into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas through a flow dividing device; the first high-temperature refrigerant gas is input into the multi-channel microtube heat exchanger to exchange heat with the tap water to convert the tap water a hot water of 45 ° C to 60 ° C, converting the first high temperature refrigerant gas into a first refrigerant liquid, and inputting the second high temperature refrigerant gas into the indoor fan to exchange heat with indoor air to provide warm Winding, and converting the second high temperature refrigerant gas into a second refrigerant liquid; and circulating the first refrigerant liquid and the second refrigerant liquid to the compressor after passing through an air-cooled evaporator and a gas-liquid separator. According to an embodiment of the present invention, the "compressing the refrigerant to an initial temperature of not lower than 75 ° C using a compressor The step of "refrigerating gas" includes compressing the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C. wherein the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger is performed with tap water. The step of converting the tap water into hot water of 45 ° C to 60 ° C and converting the first high temperature refrigerant gas into the first refrigerant liquid " may include converting the first high temperature refrigerant gas to 30 a first refrigerant liquid of from ° C to 40 ° C. wherein: said "the first high-temperature refrigerant gas is supplied to the multi-channel microtube heat exchanger for heat exchange with tap water to convert the tap water to 45t to 60° The step of converting the hot water of C to the first high-temperature refrigerant gas to the first refrigerant liquid may include converting the tap water into hot water of about 55 ° C, and converting the first high-temperature refrigerant gas into a first refrigerant liquid of about 35 ° C. ' wherein, the "the second high-temperature refrigerant gas is supplied to the indoor fan for heat exchange with the indoor air to provide warm air, and the second high-temperature refrigerant gas is converted into The second refrigerant liquid "steps can be And comprising: converting the second high-temperature refrigerant gas into a second refrigerant liquid having a temperature of 20° C. to 40° C., wherein “the second high-temperature refrigerant gas is input into the indoor fan and exchanges heat with the indoor air to The step of providing warm air and converting the second high temperature refrigerant gas to the second refrigerant liquid may include converting the second high temperature refrigerant gas to a second refrigerant liquid having a temperature of about 25 ° C. According to the present invention In one embodiment, the flow rate of the first high temperature refrigerant gas is higher than the flow rate of the second high temperature refrigerant gas, wherein a ratio of a flow rate of the first high temperature refrigerant gas to a flow rate of the second high temperature refrigerant gas may be greater than 2. Another object of the present invention is to provide an apparatus for simultaneously providing hot water and warm air, comprising: a compressor that compresses a refrigerant into a high-temperature refrigerant gas of not lower than 75 ° C; a flow dividing device The splitting device divides the initial high-temperature refrigerant gas output by the compressor into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas; a multi-channel microtube heat exchanger, the multi-channel micro The tube heat exchanger exchanges heat between the first high-temperature refrigerant gas and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and converts the first high-temperature refrigerant gas into the first refrigerant a liquid fan, the indoor fan heat exchanges the second high temperature refrigerant gas with the indoor air to provide warm air, and converts the second high temperature refrigerant gas into a second refrigerant liquid; and an air-cooled evaporator, the first a refrigerant liquid and the second refrigerant liquid are circulated to the compressor after passing through an air-cooled evaporator; wherein an outlet end of the compressor is connected to a refrigerant inlet end of the flow dividing device, and the first of the flow dividing devices a refrigerant outlet end is connected to the refrigerant inlet end of the multi-channel microtube heat exchanger, and a second refrigerant outlet end of the flow dividing device is connected to a refrigerant inlet end of the indoor fan, the multi-channel microtube heat exchanger a refrigerant outlet end and a refrigerant outlet end of the indoor fan are connected to a refrigerant inlet end of the air-cooled evaporator, and a refrigerant outlet end of the air-cooled evaporator is connected to an inlet end of the compressor According to an embodiment of the present invention, the compressor compresses the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C. Wherein, the multi-channel microtube heat exchanger can convert the first high-temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C. Wherein the multi-channel microtube heat exchanger converts the tap water into hot water of about 55 ° C and will The first high temperature refrigerant gas is converted to a first refrigerant liquid of about 35 °C. Wherein, the indoor fan can convert the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of 20 ° C to 40. Wherein, the indoor fan can convert the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of about 25 °C. Wherein a liquid storage device is further connected between the refrigerant outlet end of the multi-channel microtube heat exchanger and the refrigerant outlet end of the indoor fan and the refrigerant inlet end of the air-cooled evaporator, the liquid storage device a first refrigerant inlet end and a second refrigerant inlet end are respectively connected to a refrigerant outlet end of the multi-channel microtube heat exchanger and a refrigerant outlet end of the indoor fan, and a refrigerant outlet end of the liquid storage device is The inlet end of the refrigerant of the air-cooled evaporator is connected. Wherein, a gas-liquid separator is connected in series between the refrigerant outlet end of the air-cooled evaporator and the refrigerant inlet end of the compressor. Wherein, the flow dividing device further comprises a refrigerant pressure releasing end, and an instantaneous pressure balancer is further connected between the refrigerant outlet end of the air-cooling evaporator and the refrigerant pressure releasing end of the flow dividing device. According to another embodiment of the present invention, the flow rate of the first high temperature refrigerant gas may be higher than the flow rate of the second high temperature refrigerant gas. The ratio of the flow rate of the first high-temperature refrigerant gas to the flow rate of the second high-temperature refrigerant gas may be greater than 2. According to another embodiment of the invention, the multi-channel microtube heat exchanger comprises at least three refrigerant lines in parallel. It is still another object of the present invention to provide a multi-functional system comprising: a compressor including a refrigerant inlet end and a refrigerant outlet end, the compressor compressing refrigerant from a refrigerant inlet end of the compressor to the compressor The outlet end of the refrigerant outputs an initial high-temperature refrigerant gas of not less than 75t; the first flow dividing device, the first end of the first flow dividing device is connected to the refrigerant outlet end of the compressor, the first flow dividing device Distributing the initial high temperature refrigerant gas output by the compressor into a first high temperature refrigerant gas and a second high temperature refrigerant gas respectively outputted from the second end and the third end of the first flow dividing device; a heat exchanger, wherein a refrigerant inlet end of the multi-channel microtube heat exchanger is connected to a second end of the first flow dividing device, and the multi-channel microtube heat exchanger heats the first high-temperature refrigerant gas and tap water Exchanging to convert the tap water into hot water of 45 ° C to 60 ° C, and converting the first high temperature refrigerant gas into a first cold output from a refrigerant outlet end of the multi-channel microtube heat exchanger a second flow dividing device, the first end of the second flow dividing device is connected to the third end of the first flow dividing device; the indoor fan, the first end of the indoor fan and the second end of the second shunt device a three-terminal connection; and an air-cooled evaporator, the refrigerant outlet end of the multi-channel micro-tube heat exchanger and the second end of the indoor fan are connected to the first end of the air-cooled evaporator, the air-cooled evaporation The second end of the device is connected to the inlet end of the compressor through the fourth end and the second end of the second flow dividing device, the first end of the air-cooled evaporator and the second end of the second flow dividing device Connected to the four ends; wherein, when the first end and the third end of the second flow dividing device are connected, the second high temperature refrigerant gas from the third end of the first flow dividing device is transferred to the second When the third end of the flow dividing device, the indoor fan exchanges heat between the second high temperature refrigerant gas and the indoor air to provide warm air, and convert the second high temperature refrigerant gas into the first fan a second refrigerant liquid outputted at one end, the first refrigerant liquid and the second refrigerant liquid are circulated to the compression through the second end and the fourth end of the communication of the second flow dividing device after passing through the air-cooled evaporator The refrigerant inlet end of the machine; wherein, when the first end and the fourth end of the second flow dividing device are connected, the second high temperature refrigerant gas from the third end of the first flow dividing device is transferred to The fourth end of the second flow dividing device, the air-cooled evaporator converts the second high-temperature refrigerant gas into a second refrigerant liquid output from a first end of the air-cooled evaporator, the first refrigerant liquid And the second refrigerant liquid is evaporated and absorbed by the indoor fan to provide cold air after being exchanged with the indoor air, and then circulated to the compressor by the second end and the third end of the communication of the second flow dividing device Refrigerant Mouth end. According to an embodiment of the present invention, the compressor compresses the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C. Wherein a liquid storage device is further connected between the refrigerant outlet end of the multi-channel microtube heat exchanger and the second end of the indoor fan and the first end of the air-cooled evaporator, the liquid storage device The first end and the second end are respectively connected to the refrigerant outlet end of the multi-channel microtube heat exchanger and the second end of the indoor fan, and the third end of the liquid storage device and the air-cooled evaporator The first end is connected. Wherein a gas-liquid separator is further connected in series between the second end of the air-cooled evaporator and the refrigerant inlet end of the compressor, wherein the second end of the air-cooled evaporator passes the second shunt A fourth end and a second end of the apparatus are connected to an inlet end of the gas-liquid separator, and an outlet end of the gas-liquid separator is connected to an inlet end of the compressor. Wherein, the first flow dividing device further comprises a fourth end for the pressure relief of the refrigerant, and an instantaneous pressure balance is further bridged between the inlet end of the gas-liquid separator and the fourth end of the first flow dividing device Device. Those skilled in the art can understand that the multifunctional system can not only realize the function of "hot water + warm air" but also the function of "cooling + hot water", and by adjusting the working modes of the first and second flow dividing devices, Various functions such as "hot water", "cooling" and "warm air" can be realized without changing the basic structure of the system. The embodiment of the present invention achieves both hot water and warm air in a simple, easy to handle and adjust manner, which not only achieves safety, energy saving and environmental protection purposes, but also facilitates the operation of existing air conditioners with a small workload. Implemented on a refrigeration system. BRIEF DESCRIPTION OF THE DRAWINGS The invention can be better understood by reference to the description of embodiments of the invention, in which: FIG. 1 is a schematic structural diagram of an apparatus 100 for providing both hot and warm air in accordance with the present invention.
图 2为根据本发明的同时提供热水和暖风的方法 200的框图。  2 is a block diagram of a method 200 of providing both hot and warm air in accordance with the present invention.
图 3为根据本发明的多通道微管换热器 1 1的结构示意图。 图 4为图 3中的 A部分的局部放大图。 Figure 3 is a schematic view showing the structure of a multi-channel microtube heat exchanger 1 1 according to the present invention. Fig. 4 is a partial enlarged view of a portion A in Fig. 3.
图 5为根据本发明的多通道微管换热器 11中的冷媒管路 21的剖面图。  Figure 5 is a cross-sectional view of the refrigerant line 21 in the multi-channel microtube heat exchanger 11 in accordance with the present invention.
图 6为根据本发明的多功能装置 1000的结构示意图。  Figure 6 is a block diagram showing the structure of a multi-function device 1000 in accordance with the present invention.
图 7为根据本发明的多功能装置 1000的储液装置 114的一个实施方案的示意图。 具体实施方式 在以下描述中, 出于解释的目的, 阐述了大量具体的细节, 以提供对本发明的完整理 解。 然而, 本领域的技术人员将清楚, 没有这些具体的细节也可以实现本发明。 此外, 公 知的结构和设备是以框图的形式示出的。在这方面, 所示出的特定示例性实施方案不是用 来限制本发明, 而仅仅是用来图示说明它。 因此, 本发明的范围不是由所提供的具体实施 例来确定, 而仅仅是由所附权利要求书的表述来限定。 参见图 1, 图 1为根据本发明的同时提供热水和暖风的装置 100的结构示意图。 所述 装置 100包括压缩机 10, 分流装置 9, 多通道微管换热器 11, 室内风机 12, 风冷蒸发器 13, 储液器 14, 气液分离器 15以及瞬间压力平衡器 16。 其中, 所述压缩机 10的冷媒出口端 10a与所述分流装置 9的冷媒入口端 9a相连。 所 述分流装置 9的第一冷媒出口端 9b与所述多通道微管换热器 11的冷媒入口端 11a相连。 所述分流装置 9的第二冷媒出口端 9c与所述室内风机 12的冷媒入口端 12a相连。所述多 通道微管换热器 11的冷媒出口端 l ib与所述储液器 14的第一冷媒入口端 14a相连。所述 室内风机 12的冷媒出口端 12b与所述储液器 14的第二冷媒入口端 14b相连。所述储液器 14的冷媒出口端 14c与风冷蒸发器 13的冷媒入口端 13a相连。所述风冷蒸发器 13的冷媒 出口端 13b与所述气液分离器 15的冷媒入口端 15a相连。所述气液分离器 15的冷媒出口 端 15b被连接到所述压缩机 10的入口端 10b。 其中, 在所述风冷蒸发器 13的冷媒出口端 13b与所述分流装置的冷媒泄压端 9d之间还跨接有瞬间压力平衡器 16。 11c为自来水(例 如市政自来水或其他类似生活用水) 的入水口, l id为加热后的自来水的出水口。 根据本发明的一个实施方案, 采用压缩机 10将冷媒压缩为不低于 75°C的初始高温冷 媒气体(10a处); 将所述压缩机 10输出的所述初始高温冷媒气体通过分流装置 9分流为 第一高温冷媒气体 (%处) 和第二高温冷媒气体 (9c处) ; 将所述第一高温冷媒气体输 入多通道微管换热器 11与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水 ( l id处) , 并使所述第一高温冷媒气体转换为第一冷媒液体 (l ib处) , 以及将所述第 二高温冷媒气体输入室内风机 12与室内空气进行热交换, 以提供暖风, 并使所述第二高 温冷媒气体转化为第二冷媒液体 (12b处) ; 以及将所述第一冷媒液体和所述第二冷媒液 体通过风冷蒸发器 13和气液分离器 15后循环至所述压缩机 10。 根据本发明的一个实施方案,所述"采用压缩机将冷媒压缩为不低于 75°C的初始高温 冷媒气体" 的步骤包括将冷媒压缩为 80°C至 90°C的初始高温冷媒气体 (10a处) 。 其中, 所述 "将所述第一高温冷媒气体输入多通道微管换热器与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水(l id处), 并使所述第一高温冷媒气体转换为 第一冷媒液体" 的步骤可以包括使所述第一高温冷媒气体转换为 30°C至 40°C的第一冷媒 液体 (l ib处) 。 其中, 所述 "将所述第一高温冷媒气体输入多通道微管换热器与自来水 进行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转 换为第一冷媒液体"的步骤可以包括使所述自来水转换为约 55°C的热水(l id处) , 并使 所述第一高温冷媒气体转换为约 35°C的第一冷媒液体 (l ib处) 。 其中, 所述 "将所述第二高温冷媒气体输入室内风机 12与室内空气进行热交换, 以 提供暖风, 并使所述第二高温冷媒气体转化为第二冷媒液体 (12b处) "的步骤可以包括 使所述第二高温冷媒气体转化为温度 20°C至 40°C的第二冷媒液体(12b处)。 其中, 所述 "将所述第二高温冷媒气体输入室内风机 12与室内空气进行热交换, 以提供暖风, 并使 所述第二高温冷媒气体转化为第二冷媒液体"的步骤可以包括使所述第二高温冷媒气体转 化为温度约 25°C的第二冷媒液体 (12b处) 。 根据本发明的另一个实施方案,所述第一高温冷媒气体的流量高于所述第二高温冷媒 气体的流量。其中, 所述第一高温冷媒气体的流量与所述第二高温冷媒气体的流量之比可 以大于 2。 本领域技术人员应当可以理解, 这里所列举的所述第一高温冷媒气体的流量与 所述第二高温冷媒气体的流量分配的例子只是用来说明本发明,本发明不以此为限。例如, 根据不同的应用场合的要求,所述第一高温冷媒气体的流量也可以小于所述第二高温冷媒 气体的流量,所述第一高温冷媒气体的流量与所述第二高温冷媒气体的流量之比也可以大 于 3、 4或更大的数值。 上述实施方案中采用的结构和参数不但实现了同时提供热水和暖风,而且增加了调整 控制和操作的灵活性和便捷性。 为了根据不同的应用场合获得不同温度的暖风, '除了调节流量以外, 也可以附加地在 第二冷媒出口端 9c与所述室内风机 12的冷媒入口端 12a之间设置温度调节装置或预冷却 装置(未示出) 。 如果是用于一般的室内采暖, 除了调节流量分配以外, 也可以附加地将 所述第二冷媒出口端 9c的高温气体先预冷为不低于约 35°C的中温冷媒液体再与室内空气 进行交换, 以获得处于人类最舒适区段的暖风。 上述结构和参数是本发明的发明人经过大量非常规的实验和研究确定的。 然而, 本领 域技术人员可以理解,上述参数在此用来举例说明本发明的技术方案,本发明不以此为限。 参见图 2, 图 2为根据本发明的同时提供热水和暖风的方法 200的框图。 所述方法包 括以下步骤: Figure 7 is a schematic illustration of one embodiment of a liquid storage device 114 of a multi-function device 1000 in accordance with the present invention. DETAILED DESCRIPTION OF THE INVENTION In the following description, numerous specific details are set forth However, it will be apparent to those skilled in the art that the present invention may be practiced without these specific details. Moreover, well-known structures and devices are shown in block diagram form. In this regard, the particular exemplary embodiments shown are not intended to limit the invention, but are merely illustrative. Therefore, the scope of the invention is not to be limited Referring to Figure 1, there is shown a block diagram of a device 100 for providing both hot and warm air in accordance with the present invention. The apparatus 100 includes a compressor 10, a flow dividing device 9, a multi-channel microtube heat exchanger 11, an indoor fan 12, an air-cooled evaporator 13, a reservoir 14, a gas-liquid separator 15, and an instantaneous pressure balancer 16. The refrigerant outlet end 10a of the compressor 10 is connected to the refrigerant inlet end 9a of the flow dividing device 9. The first refrigerant outlet end 9b of the flow dividing device 9 is connected to the refrigerant inlet end 11a of the multi-channel microtube heat exchanger 11. The second refrigerant outlet end 9c of the flow dividing device 9 is connected to the refrigerant inlet end 12a of the indoor fan 12. The refrigerant outlet end l ib of the multi-channel microtube heat exchanger 11 is connected to the first refrigerant inlet end 14a of the accumulator 14. The refrigerant outlet end 12b of the indoor fan 12 is connected to the second refrigerant inlet end 14b of the accumulator 14. The refrigerant outlet end 14c of the accumulator 14 is connected to the refrigerant inlet end 13a of the air-cooled evaporator 13. The refrigerant outlet end 13b of the air-cooled evaporator 13 is connected to the refrigerant inlet end 15a of the gas-liquid separator 15. The refrigerant outlet end 15b of the gas-liquid separator 15 is connected to the inlet end 10b of the compressor 10. Therein, an instantaneous pressure balancer 16 is further bridged between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device. 11c is the water inlet of tap water (such as municipal tap water or other similar domestic water), l id is the outlet of heated tap water. According to an embodiment of the present invention, the refrigerant is compressed by the compressor 10 into an initial high-temperature refrigerant gas (at 10a) of not lower than 75 ° C; and the initial high-temperature refrigerant gas output from the compressor 10 is passed through the flow dividing device 9 Dividing into a first high-temperature refrigerant gas (%) and a second high-temperature refrigerant gas (at 9c); and introducing the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger 11 to exchange heat with tap water to make the tap water Converting to hot water (l id) of 45 ° C to 60 ° C, converting the first high temperature refrigerant gas into a first refrigerant liquid (at ib), and inputting the second high temperature refrigerant gas into the chamber The fan 12 exchanges heat with indoor air to provide warm air, and converts the second high temperature refrigerant gas into a second refrigerant liquid (at 12b); and passes the first refrigerant liquid and the second refrigerant liquid The air-cooled evaporator 13 and the gas-liquid separator 15 are then circulated to the compressor 10. According to an embodiment of the present invention, the step of "compressing the refrigerant into an initial high-temperature refrigerant gas of not lower than 75 ° C using a compressor" includes compressing the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C ( 10a). Wherein: the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger and the tap water is performed, so that the tap water is converted into hot water (l id) of 45 ° C to 60 ° C, The step of converting the first high-temperature refrigerant gas into the first refrigerant liquid may include converting the first high-temperature refrigerant gas into a first refrigerant liquid (at a position of 1 ib) of 30 ° C to 40 ° C. Wherein: the heat exchange of the first high-temperature refrigerant gas into the multi-channel microtube heat exchanger and the tap water is performed to convert the tap water into hot water of 45 ° C to 60 ° C, and the The step of converting a high temperature refrigerant gas into the first refrigerant liquid may include converting the tap water to hot water (at 1 id) of about 55 ° C, and converting the first high temperature refrigerant gas to about 35 ° C The first refrigerant liquid (at ib). Wherein, the "the second high-temperature refrigerant gas is input into the indoor fan 12 to exchange heat with the indoor air to provide warm air, and the second high-temperature refrigerant gas is converted into the second refrigerant liquid (at 12b)" The step may include converting the second high temperature refrigerant gas to a second refrigerant liquid (at 12b) at a temperature of from 20 °C to 40 °C. The step of "inputting the second high-temperature refrigerant gas into the indoor fan 12 to exchange heat with the indoor air to provide warm air and converting the second high-temperature refrigerant gas into the second refrigerant liquid" may include: The second high temperature refrigerant gas is converted to a second refrigerant liquid (at 12b) at a temperature of about 25 °C. According to another embodiment of the present invention, the flow rate of the first high temperature refrigerant gas is higher than the flow rate of the second high temperature refrigerant gas. The ratio of the flow rate of the first high-temperature refrigerant gas to the flow rate of the second high-temperature refrigerant gas may be greater than 2. It should be understood by those skilled in the art that the examples of the flow rate of the first high-temperature refrigerant gas and the flow rate of the second high-temperature refrigerant gas are merely used to illustrate the present invention, and the present invention is not limited thereto. For example, according to requirements of different applications, the flow rate of the first high temperature refrigerant gas may also be smaller than the flow rate of the second high temperature refrigerant gas, the flow rate of the first high temperature refrigerant gas and the second high temperature refrigerant gas The flow ratio can also be greater than a value of 3, 4 or greater. The structure and parameters employed in the above embodiments not only provide simultaneous hot water and warm air, but also increase the flexibility and convenience of adjustment control and operation. In order to obtain warm air of different temperatures according to different applications, in addition to adjusting the flow rate, a temperature regulating device or pre-cooling may be additionally provided between the second refrigerant outlet end 9c and the refrigerant inlet end 12a of the indoor fan 12. Device (not shown). If it is used for general indoor heating, in addition to adjusting the flow distribution, the high temperature gas of the second refrigerant outlet end 9c may be additionally pre-cooled to a medium temperature refrigerant liquid of not less than about 35 ° C and then indoor air. Exchange to get the warm air in the most comfortable section of mankind. The above structures and parameters were determined by the inventors of the present invention through a large number of unconventional experiments and studies. However, those skilled in the art can understand that the above parameters are used herein to illustrate the technical solutions of the present invention, and the present invention is not limited thereto. Referring to Figure 2, Figure 2 is a block diagram of a method 200 for providing both hot and warm air in accordance with the present invention. The method includes the following steps:
步骤 201: 采用压缩机将冷媒压缩为不低于 75t的初始高温冷媒气体; 步骤 202: 将所述压缩机输出的所述初始高温冷媒气体通过分流装置分流为第一高温 冷媒气体和第二高温冷媒气体; Step 201: compressing the refrigerant into an initial high-temperature refrigerant gas of not less than 75t by using a compressor; Step 202: The initial high-temperature refrigerant gas output by the compressor is branched into a first high-temperature refrigerant gas and a second high-temperature refrigerant gas through a flow dividing device;
步骤 203 : 将所述第一高温冷媒气体输入多通道微管换热器与自来水进行热交换, 以 使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为第一冷媒液 体, 以及将所述第二高温冷媒气体输入室内风机与室内空气进行热交换, 以提供暖风, 并 使所述第二高温冷媒气体转化为第二冷媒液体; 以及  Step 203: Perform heat exchange between the first high-temperature refrigerant gas and the multi-channel micro-tube heat exchanger and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and make the first high temperature Converting the refrigerant gas into a first refrigerant liquid, and introducing the second high-temperature refrigerant gas into the indoor fan to exchange heat with the indoor air to provide warm air and converting the second high-temperature refrigerant gas into the second refrigerant liquid;
步骤 204: 将所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器和气液分离器后 循环至所述压缩机。 根据本发明的一个^施方案, 所述步骤 201可以包括将冷媒压缩为 80°C至 90°C的高 温冷媒气体。 所述步骤 203可以包括所述第一高温冷媒气体转换为 30°C至 40°C的第一冷 媒液体。其中, 可以包括使所述自来水转换为约 55°C的热水, 并使所述第一高温冷媒气体 转换为约 35°C的第一冷媒液体。所述步骤 203还可以包括使所述第二高温冷媒气体转化为 温度 20°C至 40°C的第二冷媒液体。 其中, 可以包括使所述第二高温冷媒气体转化为温度 约 25°C的第二冷媒液体。 参见图 3至图 5。其中, 图 3为根据本发明的多通道微管换热器 11的结构示意图。 图 4为图 3中的 A部分的局部放大图。 图 5为根据本发明的多通道微管换热器 11中的冷媒 管路 21的剖面图。 多通道微管换热器 11包括有多条冷媒管路 21,该冷媒管路 21为盘管形状,而且在其 上套有与之进行热交换的水管 22。 该水管 22设有进水口 11c和出水口 l id形成的加热通 道, 使水管 22内的水经过多通道微管换热器 11时进行热交换变为热水, 从出水口 l id流 出以供使用。 在出水口 l id 上装有恒温装置 17, 以控制出水水温在规定的范围内。 本发明在冷媒管路 21与水管 22之间设有防止冷媒泄漏到水内的套管 23, 在套管 23 的端部设有冷媒泄漏报警装置 7。 当冷媒管路 21发生泄漏时, 冷媒进入套管 23, 并通过 套管 23端部的冷媒泄漏报警装置 7报警, 以确保用水无污染, 使用更安全。 在多通道微 管换热器 11的冷媒入口端 11a装有增压装置 8,使进入多个冷媒管路 21的冷媒更加均匀, 并增加了压力。 在本发明中, 为了能让压缩机 10迅速开机, 频繁开机, 缩短停机后的待机时间, 在 所述风冷蒸发器 13的冷媒出口端 13b与所述分流装置 9的冷媒泄压端 9d之间还跨接有瞬 间压力平衡器 16。 分流装置 9可以用电磁四通阀来实现, 但是本发明不以此为限。本领域技术人员应该 可以理解, 其他满足本发明功能要求的分流装置和比例阀等均可以使用。 来自分流装置 9的第一冷媒出口端 9b的第一高温气体进入多通道微管换热器 11, 多 通道微管换热器 11中冷媒管路 21的外侧包覆有与之进行热交换的水管 22。 当水管 22有 水流动时, 冷媒管路 21内高温的冷媒就将热传给水, 制成热水后供使用。 室内风机 12将 来自分流装置 9的第二冷媒出口端 9c的第二高温冷媒气体供与室内空气进行热交换, 以 提供暖气。经过多通道微管换热器 11和室内风机 12进行热交换后的冷媒液体被送到风冷 蒸发器 13中。 风冷蒸发器 13中冷媒气体蒸发而成为气体, 再被压缩机 10吸入, 经压缩 后成为高温高压的冷媒气体输出。 这样, 通过不断循环, 可以连续地同时提供热水和暖气 以供使用。在所述风冷蒸发器 13的冷媒出口端 13b与所述分流装置的冷媒泄压端 9d之间 装有平衡管路 18, 当压缩机 10断电后, 平衡管路 18上瞬间压力平衡器 16 (比如通断装 置)打开, 使系统瞬间得到压力平衡, 以便停机后可立即开动, 频繁起动, 待机时间可缩 短到 1.5秒, 这样就跟液化石油热水器一样, 可以即开即热。 本发明是以在所述风冷蒸发 器 13的冷媒出口端 13b与所述分流装置 9的冷媒泄压端 9d之间跨接瞬间压力平衡器 16 为例子, 但是, 本领域技术人员应当可以理解, 其他连接方式也是可能的, 例如在所述风 冷蒸发器 13的冷媒出口端 13b与所述压缩机 10的冷媒出口端 10a之间跨接瞬间压力平衡 器 16。 本发明设有增压装置 8, 如图 3、 图 4所示, 使进入冷媒管路 21的冷媒更加均匀, 并 且在水管 22内装有多根冷媒管路 21。 冷媒管路 21和水管 22的表面被制成凹凸不平, 由 此在使用时可使冷媒管路 21与水管 22内水成紊流状态, 从而可以迅速传热, 达到极佳的 传热效率。 而且, 在水管 22的出水口 l id上还设置有恒温装置 17, 通过温度传感器监测 水温并通过控制电路控制冷媒管路 21内的冷媒流量, 以达到控制水温的目的。 在多通道微管换热器 11上装有防止泄漏的套管 23,当冷媒管路 21在运行中发生泄漏 时, 可以防止冷媒和油进入水中, 以保证使用者的安全。所述冷媒泄漏报警装置 7如图 3、 图 4所示, 为一套在冷媒管路 21端部外侧的套管, 使水管 22与冷媒管路 21隔离。 当冷 媒管发生泄漏时, 冷媒和冷冻油进入套管 23。 当冷媒聚集较多, 例如压力超过 O.OlMPa 时, 通过压力传感系统, 可以引起系统报警, 以确保使用安全。 根据本发明的另一个实施方案,其中所述多通道微管换热器包括至少并行的三条冷媒 管路 21。 尽管图 4中以并行的三条冷媒管路 21为例子, 但是本领域技术人员可以理解, 本发明不以此为限, 四条、 五条、 六条或更多条平行的或串 /并结合的冷媒管路 21均是可 能的。 另外, 所述多条冷媒管路 21的截面也不限于圆形, 也可以采用不同的直径和 /或截 面, 只要满足本发明的热交换参数要求。 本发明的室内风机 12可以采用一般空调的室内风机, 也可以采用专门设计的适合与 室内空气进行热交换的风机, 本发明不以此为限。 本发明的风冷蒸发器 13可以为一般现 有空调的相应设备(比如分体空调的室外机的散热器) , 也可以采用专门设计的风冷蒸发 器, 本发明不以此为限。 图 6为根据本发明的一个多功能、 组合式系统, 该系统不但可以实现 "热水 +暖风" 和 "制冷 +热水" 的功能, 还可以方便地实现单一的 "热水" 、 "制冷"或 "暖风"等各 种功能。 下面参照图 6, 来说明该多功能、 组合式系统 1000。 一种多功能系统 1000, 包括: 压 缩机 110, 所述压缩机包括冷媒入口端 110b和冷媒出口端 110a, 所述压缩机 110将来自 所述压缩机的冷媒入口端 110b的冷媒压缩为从所述压缩机 110的冷媒出口端 110a输出的 不低于 75°C的初始高温冷媒气体; 第一分流装置 109, 所述第一分流装置的第一端 109a 与所述压缩机 110的所述冷媒出口端 110a相连,所述第一分流装置 109将所述压缩机 110 输出的所述初始高温冷媒气体分流为分别从所述第一分流装置的第二端 109b 和第三端 109c输出的第一高温冷媒气体和第二高温冷媒气体; 多通道微管换热器 111, 所述多通道 微管换热器 111的冷媒入口端 111a与所述第一分流装置 109的第二端 109b相连,所述多 通道微管换热器 111将所述第一高温冷媒气体与自来水进行热交换, 以使所述自来水转换 为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为从所述多通道微管换热器 111 的冷媒出口端 111b输出的第一冷媒液体;第二分流装置 119,所述第二分流装置 119的第 —端 119a与所述第一分流装置 109的第三端 109c相连;室内风机 112,所述室内风机 112 的第一端 112a与所述第二分流装置 119的第三端 119c相连; 以及风冷蒸发器 113, 所述 多通道微管换热器 111的冷媒出口端 111b和所述室内风机 112的第二端 112b与所述风冷 蒸发器 113的第一端 113a相连(如下所述, 多通道微管换热器 111的冷媒出口端 111b和 所述室内风机 112的第二端 112b与所述风冷蒸发器 113的第一端 113a之间可以通过储液 装置 114进行连接) , 所述风冷蒸发器 113的第二端 113b通过所述第二分流装置 119的 第四端 119d和第二端 119b被连接到所述压缩机 110的入口端 110b (如下所述,风冷蒸发 器 113的第二端 113b通过所述第二分流装置 119的第四端 119d和第二端 119b可以经过 串接气液分离器 115被连接到所述压缩机 110的入口端 110b),所述风冷蒸发器 113的第' 二端 113b与所述第二分流装置 119的第四端 119d相连。 其中, 当所述第二分流装置 119的第一端 119a和第三端 119c联通并将所述来自所述 第一分流装置 109的第三端 109c的所述第二高温冷媒气体传递到所述第二分流装置 119 的第三端 119c时, 所述室内风机 112将所述第二高温冷媒气体与室内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转化为从所述室内风机 112的第一端 112a输出 的第二冷媒液体,所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器 113后通过所述 第二分流装置 119的联通的第二端 119b和第四端 119d循环至所述压缩机 110的所述冷媒 入口端 HObc 其中, 当所述第二分流装置 119的第一端 119a和第四端 119d联通并将所述来自所述 第一分流装置 109的第三端 109c的所述第二高温冷媒气体传递到所述第二分流装置 119 的第四端 119d时,所述风冷蒸发器 113将所述第二高温冷媒气体转化为从风冷蒸发器 113 的第一端 113a输出的第二冷媒液体, 所述第一冷媒液体和所述第二冷媒液体通过室内风 机 112蒸发吸热以通过和室内空气交换后提供冷气,然后通过所述第二分流装置 119的联 通的第二端 11%和第三端 119c循环至所述压缩机 110的所述冷媒入口端 110b。 根据本发明的一个实施方案, 所述压缩机将冷媒压缩为 80°C至 90°C的初始高温冷媒 气体。 在所述多通道微管换热器 11 1的冷媒出口端 1 11b和所述室内风机 112的第二端 112b 与所述风冷蒸发器 113的第一端 113a之间还可以连接有储液装置 114,所述储液装置 114 的第一端 114a和第二端 114b分别与所述多通道微管换热器 111的冷媒出口端 1 1 lb和所 述室内风机 1 12的第二端 112b相连, 所述储液装置 1 14的第三端 1 14c与所述风冷蒸发器 113的第一端 113a相连。 所述风冷蒸发器 1 13的第二端 113b与所述压缩机 110的冷媒入口端 110b之间还可以 串接有气液分离器 115, 其中所述风冷蒸发器 1 13的第二端 113b通过所述第二分流装置 1 19的第四端 119d和第二端 119b被连接到所述气液分离器 115的入口端 115a,所述气液 分离器 115的出口端 1 15b与所述压缩机 110的入口端 1 10b相连。 所述第一分流装置 109还包括用于冷媒泄压的第四端 109d, 在所述气液分离器 115 的入口端 115a与所述第一分流装置 109的第四端 109d之间还跨接有瞬间压力平衡器 116 的平衡管路 1 18。 图 7为上述储液装置 114的一个实施方案的示意图。其中, 包括储液罐 1 140, 过滤器Step 204: Circulate the first refrigerant liquid and the second refrigerant liquid to the compressor after passing through an air-cooled evaporator and a gas-liquid separator. According to one embodiment of the present invention, the step 201 may include compressing the refrigerant to a high temperature refrigerant gas of 80 ° C to 90 ° C. The step 203 may include converting the first high temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C. Therein, it may include converting the tap water into hot water of about 55 ° C and converting the first high temperature refrigerant gas into a first refrigerant liquid of about 35 ° C. The step 203 may further include converting the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of 20 ° C to 40 ° C. Wherein, the second high temperature refrigerant gas may be converted into a second refrigerant liquid having a temperature of about 25 °C. See Figures 3 to 5. 3 is a schematic structural view of a multi-channel microtube heat exchanger 11 according to the present invention. Fig. 4 is a partial enlarged view of a portion A in Fig. 3. Figure 5 is a cross-sectional view of the refrigerant line 21 in the multi-channel microtube heat exchanger 11 in accordance with the present invention. The multi-channel microtube heat exchanger 11 includes a plurality of refrigerant tubes 21 which are in the shape of a coil and which are provided with a water pipe 22 for heat exchange therewith. The water pipe 22 is provided with a heating passage formed by the water inlet 11c and the water outlet l id, so that the water in the water pipe 22 passes through the multi-channel micro-tube heat exchanger 11 to exchange heat to hot water, and flows out from the water outlet l id for supply. use. A thermostat 17 is installed on the water outlet l id to control the outlet water temperature within a prescribed range. In the present invention, a sleeve 23 for preventing refrigerant from leaking into the water is provided between the refrigerant pipe 21 and the water pipe 22, and a refrigerant leakage alarm device 7 is provided at the end of the casing 23. When the refrigerant line 21 leaks, the refrigerant enters the sleeve 23 and is alarmed by the refrigerant leakage alarm device 7 at the end of the sleeve 23 to ensure that the water is free from contamination and safer to use. The refrigerant inlet 8 is provided at the refrigerant inlet end 11a of the multi-channel microtube heat exchanger 11 to make the refrigerant entering the plurality of refrigerant lines 21 more uniform and to increase the pressure. In the present invention, in order to enable the compressor 10 to be quickly turned on, the power is turned on frequently, and the standby time after the shutdown is shortened, at the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device 9. An instantaneous pressure balancer 16 is also connected across. The flow dividing device 9 can be realized by an electromagnetic four-way valve, but the invention is not limited thereto. Those skilled in the art will appreciate that other shunting devices, proportional valves, etc. that meet the functional requirements of the present invention can be used. The first high temperature gas from the first refrigerant outlet end 9b of the flow dividing device 9 enters the multi-channel microtube heat exchanger 11, more The outside of the refrigerant line 21 in the passage microtube heat exchanger 11 is covered with a water pipe 22 for heat exchange therewith. When the water pipe 22 has water flowing, the high-temperature refrigerant in the refrigerant pipe 21 transfers heat to the water to be used as hot water. The indoor fan 12 supplies the second high-temperature refrigerant gas from the second refrigerant outlet end 9c of the flow dividing device 9 to heat exchange with the indoor air to provide heating. The refrigerant liquid subjected to heat exchange by the multi-channel microtube heat exchanger 11 and the indoor fan 12 is sent to the air-cooled evaporator 13. In the air-cooled evaporator 13, the refrigerant gas evaporates to become a gas, and is sucked by the compressor 10, and is compressed to become a high-temperature high-pressure refrigerant gas. In this way, by continuously circulating, hot water and heating can be continuously supplied for use at the same time. A balance line 18 is disposed between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device. When the compressor 10 is de-energized, an instantaneous pressure balancer is provided on the balance line 18. 16 (such as the on/off device) is turned on, so that the system can be pressure balanced instantaneously, so that it can be started immediately after the shutdown, and the standby time can be shortened to 1.5 seconds, which is the same as the liquefied petroleum water heater. The present invention is exemplified by bridging the instantaneous pressure balancer 16 between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant discharge end 9d of the flow dividing device 9, but it should be understood by those skilled in the art. Other connection means are also possible, for example, bridging the instantaneous pressure balancer 16 between the refrigerant outlet end 13b of the air-cooled evaporator 13 and the refrigerant outlet end 10a of the compressor 10. The present invention is provided with a supercharging device 8, and as shown in Figs. 3 and 4, the refrigerant entering the refrigerant line 21 is made more uniform, and a plurality of refrigerant lines 21 are installed in the water pipe 22. The surfaces of the refrigerant pipe 21 and the water pipe 22 are made uneven, whereby the water in the refrigerant pipe 21 and the water pipe 22 can be turbulent during use, so that heat can be quickly transferred, and excellent heat transfer efficiency can be achieved. Further, a thermostat 17 is disposed on the water outlet l id of the water pipe 22, and the water temperature is monitored by the temperature sensor and the flow rate of the refrigerant in the refrigerant pipe 21 is controlled by the control circuit to achieve the purpose of controlling the water temperature. The multi-channel microtube heat exchanger 11 is provided with a leak-proof casing 23 which prevents refrigerant and oil from entering the water when the refrigerant pipe 21 leaks during operation to ensure the safety of the user. As shown in Figs. 3 and 4, the refrigerant leakage alarm device 7 is a sleeve that is outside the end of the refrigerant line 21 to isolate the water tube 22 from the refrigerant line 21. When the refrigerant pipe leaks, the refrigerant and the refrigerating oil enter the casing 23. When the refrigerant accumulates more, for example, when the pressure exceeds O.OlMPa, the pressure sensing system can cause the system to alarm to ensure safe use. According to another embodiment of the invention, wherein the multi-channel microtube heat exchanger comprises at least three refrigerant lines 21 in parallel. Although three parallel refrigerant lines 21 are taken as an example in FIG. 4, those skilled in the art can understand that the present invention is not limited thereto, and four, five, six or more parallel or serial/parallel refrigerant tubes are not limited thereto. Road 21 is possible. Further, the cross section of the plurality of refrigerant lines 21 is not limited to a circular shape, and different diameters and/or cross sections may be employed as long as the heat exchange parameter requirements of the present invention are satisfied. The indoor fan 12 of the present invention may be an indoor fan of a general air conditioner, or a fan specially designed to exchange heat with indoor air, and the invention is not limited thereto. The air-cooled evaporator 13 of the present invention may be a corresponding device of a conventional air conditioner (such as a radiator of an outdoor unit of a split air conditioner), or a specially designed air-cooled evaporator, and the invention is not limited thereto. Figure 6 is a multi-functional, combined system according to the present invention, which not only achieves "hot water + warm air" And the function of "cooling + hot water", it is also convenient to realize a single "hot water", "cooling" or "warm air" and other functions. The multi-function, modular system 1000 will now be described with reference to FIG. A multi-functional system 1000, comprising: a compressor 110, the compressor including a refrigerant inlet end 110b and a refrigerant outlet end 110a, the compressor 110 compressing a refrigerant from a refrigerant inlet end 110b of the compressor into a refrigerant An initial high temperature refrigerant gas of not less than 75 ° C outputted from the refrigerant outlet end 110a of the compressor 110; a first flow dividing device 109, a first end 109a of the first flow dividing device and the refrigerant of the compressor 110 The outlet end 110a is connected, and the first flow dividing device 109 branches the initial high-temperature refrigerant gas output by the compressor 110 into a first output from the second end 109b and the third end 109c of the first flow dividing device, respectively. a high-temperature refrigerant gas and a second high-temperature refrigerant gas; a multi-channel microtube heat exchanger 111, the refrigerant inlet end 111a of the multi-channel microtube heat exchanger 111 is connected to the second end 109b of the first flow dividing device 109, The multi-channel microtube heat exchanger 111 exchanges heat between the first high-temperature refrigerant gas and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and the first high-temperature refrigerant gas Converted from the above a first refrigerant liquid outputted from the refrigerant outlet end 111b of the passage microtube heat exchanger 111; a second flow dividing device 119, a first end 119a of the second flow dividing device 119 and a third end 109c of the first flow dividing device 109 Connected to the indoor fan 112, the first end 112a of the indoor fan 112 is connected to the third end 119c of the second diverting device 119; and the air-cooled evaporator 113, the refrigerant of the multi-channel micro-tube heat exchanger 111 The outlet end 111b and the second end 112b of the indoor fan 112 are connected to the first end 113a of the air-cooled evaporator 113 (as described below, the refrigerant outlet end 111b of the multi-channel microtube heat exchanger 111 and the chamber The second end 112b of the fan 112 and the first end 113a of the air-cooled evaporator 113 may be connected by a liquid storage device 114, and the second end 113b of the air-cooled evaporator 113 passes the second shunt The fourth end 119d and the second end 119b of the device 119 are connected to the inlet end 110b of the compressor 110 (as described below, the second end 113b of the air-cooled evaporator 113 passes the fourth of the second diverting device 119 The end 119d and the second end 119b may be connected via the tandem gas-liquid separator 115 The inlet end 110 of the compressor 110b), the second air-cooled evaporator '113 second end 113b connected to the fourth terminal of the second shunt device 119 119d. Wherein the first end 119a and the third end 119c of the second flow dividing device 119 are in communication and the second high temperature refrigerant gas from the third end 109c of the first flow dividing device 109 is transferred to the When the third end 119c of the second flow dividing device 119, the indoor fan 112 exchanges heat between the second high temperature refrigerant gas and the indoor air to provide warm air, and convert the second high temperature refrigerant gas into a slave a second refrigerant liquid outputted from the first end 112a of the indoor fan 112, the first refrigerant liquid and the second refrigerant liquid passing through the air-cooled evaporator 113 and passing through the second end of the second shunt device 119 119b and fourth end 119d are circulated to the refrigerant inlet end HObc of the compressor 110, wherein when the first end 119a and the fourth end 119d of the second diverting device 119 are in communication and the first from the first When the second high temperature refrigerant gas of the third end 109c of the flow dividing device 109 is transferred to the fourth end 119d of the second flow dividing device 119, the air-cooled evaporator 113 converts the second high temperature refrigerant gas into a slave The first end 113a of the air-cooled evaporator 113 is lost The second refrigerant liquid, the first refrigerant liquid and the second refrigerant liquid are evaporated and absorbed by the indoor fan 112 to provide cold air after being exchanged with the indoor air, and then communicated through the second shunt device 119. The two end 11% and third end 119c are circulated to the refrigerant inlet end 110b of the compressor 110. According to an embodiment of the present invention, the compressor compresses the refrigerant into an initial high-temperature refrigerant gas of 80 ° C to 90 ° C. A liquid storage may be connected between the refrigerant outlet end 11b of the multi-channel microtube heat exchanger 11 1 and the second end 112b of the indoor fan 112 and the first end 113a of the air-cooled evaporator 113. The first end 114a and the second end 114b of the liquid storage device 114 are respectively connected to the refrigerant outlet end 1 1 lb of the multi-channel microtube heat exchanger 111 and the second end 112b of the indoor fan 1 12 Connected, the third end 14c of the liquid storage device 14 is connected to the first end 113a of the air-cooled evaporator 113. A gas-liquid separator 115 may be connected in series between the second end 113b of the air-cooled evaporator 1 13 and the refrigerant inlet end 110b of the compressor 110, wherein the second end of the air-cooled evaporator 1 13 113b is connected to the inlet end 115a of the gas-liquid separator 115 through the fourth end 119d and the second end 119b of the second flow dividing device 1 19, the outlet end 1 15b of the gas-liquid separator 115 is The inlet ends 1 10b of the compressor 110 are connected. The first flow dividing device 109 further includes a fourth end 109d for refrigerant pressure relief, and is also bridged between the inlet end 115a of the gas-liquid separator 115 and the fourth end 109d of the first flow dividing device 109. There is a balancing line 1 18 of the instantaneous pressure balancer 116. FIG. 7 is a schematic illustration of one embodiment of the above described liquid storage device 114. Among them, including the liquid storage tank 1 140, the filter
1144, 毛细管 1141, 冷媒洩压器 1142和多个单向阀 1143。 本领域技术人员可以理解, 上面根据同时提供 "热水 +暖风"和 "制冷 +热水"为例来 说明了该多功能系统, 但本发明不以此为限。通过调节所述第一和第二分流装置以及储液 装置 114等的工作方式和冷媒的循环方向, 不但可以实现 "热水 +暖风"和 "制冷 +热水" 的功能, 还可以方便地实现 "热水"、 "制冷"和 "暖风"等各种功能, 而不需改变系统 基本结构。 例如, 通过控制第一、 第二分流装置的分流操作, 就可以实现单一的 "热水" (冷媒全部从 109b输出) , 单一的 "制冷风 (冷媒全部从 109c经 119d输出) "或单一 的 "暖风 (冷媒全部从 109c经 119c输出) " , 而不用改变系统的基本结构。 因此, 本领 域技术人员应当可以理解,本发明的技术方案所提及的分流的所述第一高温冷媒气体和所 述第二高温冷媒气体中的任一可以为零。 另外, 本领域技术人员应当可以理解, 由于可以 方便地调节分流的所述第一高温冷媒气体和所述第二高温冷媒气体中的比例,大大提高了 本发明的技术方案的应用范围和灵活性。 本领域技术人员可以理解, 本发明的第一和第二分流装置 109、 1 19可以用电磁四通 阀来实现, 但是本发明不以此为限。 本领域技术人员应该可以理解, 其他满足本发明功能 要求的分流装置和比例阀等均可以使用。其他部件和前述针对图 1至图 5描述的部件类似, 在此不再赘述。 总之, 本发明的实施方案以相对简单的结构、 参数, 以及可便捷控制和调整性能的方 式实现了同时提供热水和暖风和其他各种功能, 不但达到了安全、 节能和环保的目的, 而 且非常便于以较小的工作量在现有的空调和制冷系统上实现该功能。最大限度地扩展了应 用空间。 虽然已经针对实施方案对本发明进行了描述,但本领域的熟练技术人员可以从中意识 到许多修改和变化。所附的权利要求书应被视为覆盖了所有这些落入本发明真正的精神和 范围内的修改和变化。 1144, capillary 1141, refrigerant pressure relief 1142 and a plurality of one-way valves 1143. It can be understood by those skilled in the art that the multi-functional system is described above by taking "hot water + warm air" and "cooling + hot water" as examples, but the invention is not limited thereto. By adjusting the working modes of the first and second flow dividing devices and the liquid storage device 114 and the circulation direction of the refrigerant, not only the functions of "hot water + warm air" and "cooling + hot water" can be realized, but also conveniently Various functions such as "hot water", "cooling" and "warm air" are realized without changing the basic structure of the system. For example, by controlling the shunting operation of the first and second flow dividing devices, a single "hot water" (the refrigerant is all output from 109b) can be realized, and a single "refrigerating wind (the refrigerant is all output from 109c via 119d)" or a single "Warm air (all refrigerants are output from 109c via 119c)" without changing the basic structure of the system. Therefore, it should be understood by those skilled in the art that any of the first high temperature refrigerant gas and the second high temperature refrigerant gas which are branched as mentioned in the technical solution of the present invention may be zero. In addition, those skilled in the art should understand that the application range and flexibility of the technical solution of the present invention are greatly improved because the ratio of the first high temperature refrigerant gas and the second high temperature refrigerant gas that are branched can be conveniently adjusted. . It will be understood by those skilled in the art that the first and second flow dividing devices 109, 19 of the present invention can be implemented by an electromagnetic four-way valve, but the invention is not limited thereto. Those skilled in the art will appreciate that other shunting devices, proportional valves, etc. that meet the functional requirements of the present invention can be used. The other components are similar to those described above with respect to FIGS. 1 to 5 and will not be described again. In summary, the embodiment of the present invention achieves both hot water and warm air and various other functions in a relatively simple structure, parameters, and a manner that can be easily controlled and adjusted, thereby achieving safety, energy saving, and environmental protection. It is also very convenient to achieve this function on existing air conditioning and refrigeration systems with a small amount of work. Maximize application space. While the invention has been described with respect to the embodiments, the modifications The appended claims are to be construed as covering all such modifications and modifications

Claims

权利要求书 Claim
1 . 一种同时提供热水和暖风的方法, 包括: A method of providing both hot water and warm air, comprising:
采用压缩机将冷媒压缩为不低于 75°C的初始高温冷媒气体;  Compressing the refrigerant to an initial high temperature refrigerant gas of not lower than 75 ° C using a compressor;
将所述压缩机输出的所述初始高温冷媒气体通过分流装置分流为第一高温冷媒气体 和第二高温冷媒气体;  Discharging the initial high temperature refrigerant gas output by the compressor into a first high temperature refrigerant gas and a second high temperature refrigerant gas through a flow dividing device;
将所述第一高温冷媒气体输入多通道微管换热器与自来水进行热交换, 以使所述自来 水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为第一冷媒液体, 以及将 所述第二高温冷媒气体输入室内风机与室内空气进行热交换, 以提供暖风, 并使所述第二 高温冷媒气体转化为第二冷媒液体; 以及  The first high-temperature refrigerant gas is input into the multi-channel microtube heat exchanger to exchange heat with tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and convert the first high-temperature refrigerant gas a first refrigerant liquid, and the second high-temperature refrigerant gas is input into the indoor fan to exchange heat with the indoor air to provide warm air, and convert the second high-temperature refrigerant gas into a second refrigerant liquid;
将所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器和气液分离器后循环至所 述压缩机。  The first refrigerant liquid and the second refrigerant liquid are circulated to the compressor after passing through an air-cooled evaporator and a gas-liquid separator.
2. 如权利要求 1所述的方法, 其中所述 "采用压缩机将冷媒压縮为不低于 75°C的初 始高温冷媒气体" 的步骤包括将冷媒压缩为 80°C至 9(TC的初始高温冷媒气体。 2. The method according to claim 1, wherein the step of "compressing the refrigerant to an initial high-temperature refrigerant gas of not lower than 75 ° C using a compressor" comprises compressing the refrigerant to 80 ° C to 9 (TC Initial high temperature refrigerant gas.
3. 如权利要求 2所述的方法,其中所述"将所述第一高温冷媒气体输入多通道微管换 热器与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高 温冷媒气体转换为第一冷媒液体" 的步骤包括使所述第一高温冷媒气体转换为 30'C至 40°C的第一冷媒液体。 3. The method of claim 2, wherein said "inputting said first high temperature refrigerant gas into a multichannel microtube heat exchanger for heat exchange with tap water to convert said tap water to 45 ° C to 60 ° The step of converting the hot water of C to the first high-temperature refrigerant gas to the first refrigerant liquid includes converting the first high-temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C.
4. 如权利要求 2所述的方法,其中所述"将所述第一高温冷媒气体输入多通道微管换 热器与自来水进行热交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高 温冷媒气体转换为第一冷媒液体"的步骤包括使所述自来水转换为约 55°C的热水,并使所 述第一高温冷媒气体转换为约 35°C的第一冷媒液体。 4. The method of claim 2, wherein said "inputting said first high temperature refrigerant gas into a multichannel microtube heat exchanger for heat exchange with tap water to convert said tap water to 45 ° C to 60 ° The step of converting the hot water of C to the first high-temperature refrigerant gas into a first refrigerant liquid includes converting the tap water into hot water of about 55 ° C, and converting the first high-temperature refrigerant gas into about The first refrigerant liquid at 35 °C.
5. 如权利要求 2所述的方法,其中所述"将所述第二高温冷媒气体输入室内风机与室 内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转化为第二冷媒液体"的步 骤包括使所述第二高温冷媒气体转化为温度 20°C至 4(TC的第二冷媒液体。 5. The method of claim 2, wherein said "inputting said second high temperature refrigerant gas into an indoor fan for heat exchange with indoor air to provide warm air and converting said second high temperature refrigerant gas into said first The step of "two refrigerant liquids" includes converting the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of 20 ° C to 4 (TC).
6. 如权利要求 2所述的方法,其中所述"将所述第二高温冷媒气体输入室内风机与室 内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转化为第二冷媒液体"的步 骤包括使所述第二高温冷媒气体转化为温度约 25°C的第二冷媒液体。 6. The method of claim 2, wherein said "inputting said second high temperature refrigerant gas into an indoor fan for heat exchange with indoor air to provide warm air and converting said second high temperature refrigerant gas into said first The step of "two refrigerant liquids" includes converting the second high temperature refrigerant gas into a second refrigerant liquid having a temperature of about 25 °C.
7. 如权利要求 2所述的方法,其中所述第一高温冷媒气体的流量高于所述第二高温冷 媒气体的流量。 7. The method of claim 2 wherein the flow rate of the first high temperature refrigerant gas is higher than the flow rate of the second high temperature refrigerant gas.
8. 如权利要求 7所述的方法,其中所述第一高温冷媒气体的流量与所述第二高温冷媒 气体的流量之比大于 2。 8. The method of claim 7, wherein a ratio of a flow rate of the first high temperature refrigerant gas to a flow rate of the second high temperature refrigerant gas is greater than two.
9. 一种同时提供热水和暖风的装置, 包括: 9. A device that provides both hot water and warm air, including:
压缩机, 所述压缩机将冷媒压缩为不低于 75°C的高温冷媒气体;  a compressor that compresses the refrigerant into a high-temperature refrigerant gas not lower than 75 ° C;
分流装置,所述分流装置将所述压缩机输出的所述初始高温冷媒气体分流为第一高温 冷媒气体和第二高温冷媒气体;  a flow dividing device that divides the initial high temperature refrigerant gas output by the compressor into a first high temperature refrigerant gas and a second high temperature refrigerant gas;
多通道微管换热器,所述多通道微管换热器将所述第一高温冷媒气体与自来水进行热 交换, 以使所述自来水转换为 45°C至 60°C的热水, 并使所述第一高温冷媒气体转换为第 一冷媒液体;  a multi-channel microtube heat exchanger that exchanges heat between the first high-temperature refrigerant gas and tap water to convert the tap water into hot water of 45 ° C to 60 ° C, and Converting the first high temperature refrigerant gas into a first refrigerant liquid;
室内风机, 所述室内风机将第二高温冷媒气体与室内空气进行热交换, 以提供暖风, 并使第二高温冷媒气体转化为第二冷媒液体; 以及  An indoor fan that exchanges heat between the second high temperature refrigerant gas and the indoor air to provide warm air and convert the second high temperature refrigerant gas into the second refrigerant liquid;
风冷蒸发器,所述第一冷媒液体和所述第二冷媒液体通过风冷蒸发器后循环至所述压 缩机;  An air-cooled evaporator, the first refrigerant liquid and the second refrigerant liquid are circulated to the compressor after passing through an air-cooled evaporator;
其中, 所述压缩机的出口端与所述分流装置的冷媒入口端相连, 所述分流装置的第一 冷媒出口端与所述多通道微管换热器的冷媒入口端相连,所述分流装置的第二冷媒出口端 与所述室内风机的冷媒入口端相连,所述多通道微管换热器的冷媒出口端和所述室内风机 的冷媒出口端与所述风冷蒸发器的冷媒入口端相连,所述风冷蒸发器的冷媒出口端被连接 到所述压缩机的入口端。  Wherein, an outlet end of the compressor is connected to a refrigerant inlet end of the flow dividing device, and a first refrigerant outlet end of the flow dividing device is connected to a refrigerant inlet end of the multi-channel microtube heat exchanger, the flow dividing device The second refrigerant outlet end is connected to the refrigerant inlet end of the indoor fan, the refrigerant outlet end of the multi-channel microtube heat exchanger and the refrigerant outlet end of the indoor fan and the refrigerant inlet end of the air-cooled evaporator Connected, the refrigerant outlet end of the air-cooled evaporator is connected to the inlet end of the compressor.
10. 如权利要求 9所述的装置,其中所述压缩机将冷媒压缩为 80°C至 90°C的初始高温 冷媒气体。 10. Apparatus according to claim 9 wherein said compressor compresses the refrigerant to an initial high temperature refrigerant gas of from 80 °C to 90 °C.
' 11. 如权利要求 10所述的装置,其中所述多通道微管换热器将所述第一高温冷媒气体 转换为 30°C至 40°C的第一冷媒液体 12. 如权利要求 10所述的装置, 其中所述多通道微管换热器将所述自来水转换为约11. The apparatus according to claim 10, wherein the multi-channel microtube heat exchanger converts the first high-temperature refrigerant gas into a first refrigerant liquid of 30 ° C to 40 ° C. 12. The apparatus, wherein the multi-channel microtube heat exchanger converts the tap water into an approximate
55°C的热水, 并且将所述第一高温冷媒气体转换为约 35°C的第一冷媒液体。 Hot water at 55 ° C, and the first high temperature refrigerant gas is converted into a first refrigerant liquid of about 35 °C.
13. 如权利要求 10所述的装置,其中所述室内风机将所述第二高温冷媒气体转化为温 度 20°C至 40°C的第二冷媒液体。 13. Apparatus according to claim 10 wherein said indoor fan converts said second high temperature refrigerant gas to a second refrigerant liquid having a temperature of from 20 °C to 40 °C.
14. 如权利要求 10所述的装置,其中所述室内风机将所述第二高温冷媒液体转化为温 度约 25°C的第二冷媒液体。 14. Apparatus according to claim 10 wherein said indoor fan converts said second high temperature refrigerant liquid to a second refrigerant liquid having a temperature of about 25 °C.
15. 如权利要求 9所述的装置, 其中所述多通道微管换热器包括至少并行的三条冷媒 管路。 15. Apparatus according to claim 9 wherein said multi-channel microtube heat exchanger comprises at least three refrigerant lines in parallel.
16. 如权利要求 10所述的装置,其中在所述多通道微管换热器的冷媒出口端和所述室 内风机的冷媒出口端与所述风冷蒸发器的冷媒入口端之间还连接有储液装置,所述储液装 置的第一冷媒入口端和第二冷媒入口端分别与所述多通道微管换热器的冷媒出口端和所 述室内风机的冷媒出口端相连,所述储液装置的冷媒出口端与所述风冷蒸发器的冷媒入口 端相连。 16. The apparatus according to claim 10, wherein a connection between a refrigerant outlet end of the multi-channel microtube heat exchanger and a refrigerant outlet end of the indoor fan and a refrigerant inlet end of the air-cooled evaporator is further connected a liquid storage device, wherein the first refrigerant inlet end and the second refrigerant inlet end of the liquid storage device are respectively connected to a refrigerant outlet end of the multi-channel microtube heat exchanger The refrigerant outlet end of the indoor fan is connected, and the refrigerant outlet end of the liquid storage device is connected to the refrigerant inlet end of the air-cooled evaporator.
17. 如权利要求 10所述的装置,其中在所述风冷蒸发器的冷媒出口端与所述压縮机的 冷媒入口端之间还串接有气液分离器。 17. Apparatus according to claim 10 wherein a gas-liquid separator is also connected in series between the refrigerant outlet end of the air-cooled evaporator and the refrigerant inlet end of the compressor.
18. 如权利要求 10所述的装置,其中所述分流装置还包括冷媒泄压端,在所述风冷蒸 发器的冷媒出口端与所述分流装置的所述冷媒泄压端之间还跨接有瞬间压力平衡器。 18. The apparatus of claim 10, wherein the flow dividing device further comprises a refrigerant pressure relief end, further spanning between a refrigerant outlet end of the air-cooled evaporator and the refrigerant pressure relief end of the flow dividing device An instantaneous pressure balancer is attached.
19. 如权利要求 9所述的装置, 其中所述第一高温冷媒气体的流量高于所述第二高温 冷媒气体的流量。 19. The apparatus of claim 9, wherein a flow rate of the first high temperature refrigerant gas is higher than a flow rate of the second high temperature refrigerant gas.
20. 如权利要求 9所述的装置, 其中所述第一高温冷媒气体的流量与所述第二高温冷 媒气体的流量之比大于 2。 20. The apparatus according to claim 9, wherein a ratio of a flow rate of the first high temperature refrigerant gas to a flow rate of the second high temperature refrigerant gas is greater than 2.
21. 一种多功能系统, 包括- 压缩机, 包括冷媒入口端和冷媒出口端, 所述压缩机将来自所述压缩机的冷媒入口端 的冷媒压缩为从所述压缩机的冷媒出口端输出的不低于 75°C的初始高温冷媒气体;  21. A multi-functional system comprising: a compressor comprising a refrigerant inlet end and a refrigerant outlet end, the compressor compressing refrigerant from a refrigerant inlet end of the compressor to output from a refrigerant outlet end of the compressor An initial high temperature refrigerant gas not lower than 75 ° C;
第一分流装置, 所述第一分流装置的第一端与所述压缩机的所述冷媒出口端相连, 所 述第一分流装置将所述压缩机输出的所述初始高温冷媒气体分流为分别从所述第一分流 装置的第二端和第三端输出的第一高温冷媒气体和第二高温冷媒气体;  a first flow dividing device, the first end of the first flow dividing device is connected to the refrigerant outlet end of the compressor, and the first flow dividing device divides the initial high temperature refrigerant gas output by the compressor into separate a first high temperature refrigerant gas and a second high temperature refrigerant gas outputted from the second end and the third end of the first flow dividing device;
多通道微管换热器,所述多通道微管换热器的冷媒入口端与所述第一分流装置的第二 端相连, 所述多通道微管换热器将所述第一高温冷媒气体与自来水进行热交换, 以使所述 自来水转换为 45°C至 60 C的热水, 并使所述第一高温冷媒气体转换为从所述多通道微管 换热器的冷媒出口端输出的第一冷媒液体;  a multi-channel microtube heat exchanger, wherein a refrigerant inlet end of the multi-channel microtube heat exchanger is connected to a second end of the first flow dividing device, and the multi-channel microtube heat exchanger will be the first high-temperature refrigerant The gas exchanges heat with the tap water to convert the tap water into hot water of 45 ° C to 60 C, and converts the first high temperature refrigerant gas into a refrigerant outlet end of the multi-channel microtube heat exchanger First refrigerant liquid;
第二分流装置, 所述第二分流装置的第一端与所述第一分流装置的第三端相连; 室内风机, 所述室内风机的第一端与所述第二分流装置的第三端相连; 以及 风冷蒸发器,所述多通道微管换热器的冷媒出口端和所述室内风机的第二端与所述风 冷蒸发器的第一端相连,所述风冷蒸发器的第二端通过所述第二分流装置的第四端和第二 端被连接到所述压缩机的入口端,所述风冷蒸发器的第一端与所述第二分流装置的第四端 相连;  a second flow dividing device, the first end of the second flow dividing device is connected to the third end of the first flow dividing device; the indoor fan, the first end of the indoor fan and the third end of the second shunt device And an air-cooled evaporator, the refrigerant outlet end of the multi-channel micro-tube heat exchanger and the second end of the indoor fan are connected to the first end of the air-cooled evaporator, the air-cooled evaporator a second end is connected to an inlet end of the compressor through a fourth end and a second end of the second flow dividing device, a first end of the air-cooled evaporator and a fourth end of the second flow dividing device Connected
其中, 当所述第二分流装置的第一端和第三端联通并将所述来自所述第一分流装置的 第三端的所述第二高温冷媒气体传递到所述第二分流装置的第三端时,所述室内风机将所 述第二高温冷媒气体与室内空气进行热交换, 以提供暖风, 并使所述第二高温冷媒气体转 化为从所述室内风机的第一端输出的第二冷媒液体,所述第一冷媒液体和所述第二冷媒液 体通过风冷蒸发器后通过所述第二分流装置的联通的第二端和第四端循环至所述压缩机 的所述冷媒入口端;  Wherein the first end and the third end of the second flow dividing device are in communication and the second high temperature refrigerant gas from the third end of the first flow dividing device is transferred to the second shunt device At the three ends, the indoor fan exchanges heat between the second high temperature refrigerant gas and the indoor air to provide warm air, and converts the second high temperature refrigerant gas into output from the first end of the indoor fan. a second refrigerant liquid, wherein the first refrigerant liquid and the second refrigerant liquid are circulated to the compressor by the second end and the fourth end of the communication of the second flow dividing device after passing through the air-cooled evaporator Refrigerant inlet end;
其中, 当所述第二分流装置的第一端和第四端联通并将所述来自所述第一分流装置的 第三端的所述第二高温冷媒气体传递到所述第二分流装置的第四端时,所述风冷蒸发器将 所述第二高温冷媒气体转化为从风冷蒸发器的第一端输出的第二冷媒液体,所述第一冷媒 液体和所述第二冷媒液体通过室内风机蒸发吸热以通过和室内空气交换后提供冷气,然后 通过所述第二分流装置的联通的第二端和第三端循环至所述压缩机的所述冷媒入口端。 Wherein the first end and the fourth end of the second flow dividing device are in communication and the second high temperature refrigerant gas from the third end of the first flow dividing device is transferred to the second shunt device At the four ends, the air-cooled evaporator will The second high-temperature refrigerant gas is converted into a second refrigerant liquid output from the first end of the air-cooled evaporator, and the first refrigerant liquid and the second refrigerant liquid are evaporated by an indoor fan to absorb heat to exchange with indoor air. Cooling gas is then provided and then circulated through the second and third ends of the communication of the second flow dividing device to the refrigerant inlet end of the compressor.
22. 如权利要求 21所述的装置, 其中所述压缩机将冷媒压缩为 80°C至 90°C的初始高 温冷媒气体。 22. Apparatus according to claim 21 wherein said compressor compresses the refrigerant to an initial high temperature refrigerant gas of from 80 °C to 90 °C.
23. 如权利要求 21所述的装置,其中在所述多通道微管换热器的冷媒出口端和所述室 内风机的第二端与所述风冷蒸发器的第一端之间还连接有储液装置,所述储液装置的第一 端和第二端分别与所述多通道微管换热器的冷媒出口端和所述室内风机的第二端相连,所 述储液装置的第三端与所述风冷蒸发器的第一端相连。 23. The apparatus of claim 21, wherein a connection between a refrigerant outlet end of the multi-channel microtube heat exchanger and a second end of the indoor fan and a first end of the air-cooled evaporator is further a liquid storage device, wherein the first end and the second end of the liquid storage device are respectively connected to a refrigerant outlet end of the multi-channel microtube heat exchanger and a second end of the indoor fan, wherein the liquid storage device The third end is connected to the first end of the air-cooled evaporator.
24. 如权利要求 21所述的装置,其中在所述风冷蒸发器的第二端与所述压缩机的冷媒 入口端之间还串接有气液分离器,其中所述风冷蒸发器的第二端通过所述第二分流装置的 第四端和第二端被连接到所述气液分离器的入口端,所述气液分离器的出口端与所述压缩 机的入口端相连。 24. The apparatus of claim 21, wherein a gas-liquid separator is further connected in series between the second end of the air-cooled evaporator and the refrigerant inlet end of the compressor, wherein the air-cooled evaporator The second end is connected to the inlet end of the gas-liquid separator through the fourth end and the second end of the second flow dividing device, and the outlet end of the gas-liquid separator is connected to the inlet end of the compressor .
25. 如权利要求 21所述的装置, 其中所述第一分流装置还包括用于冷媒泄压的第四 端,在所述气液分离器的入口端与所述第一分流装置的第四端之间还跨接有瞬间压力平衡 器。 25. The apparatus of claim 21, wherein the first flow dividing device further comprises a fourth end for refrigerant pressure relief, at an inlet end of the gas-liquid separator and a fourth end of the first flow dividing device There is also an instantaneous pressure balancer between the ends.
PCT/CN2010/001616 2009-10-15 2010-10-15 Method, apparatus and multi-functional system for supplying hot water and warm air simultaneously WO2011044757A1 (en)

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