JP2012145309A - Heat source system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a heat source system that can efficiently output cold and/or warm air by recollection of heat supplied from the low-temperature exhaust heat made to be 50 to 60°C.SOLUTION: The heat source system 1A comprises an electric heat pump 2 provided with a turbocompressor 5 driven by an electric motor, and an absorption refrigerating machine 3. The electric heat pump 2 recollects heat supplied from the low-temperature exhaust heat of 50-60°C in an evaporator 11, and a warm air of 80-90°C is output from a condenser 7. The absorption refrigerating machine 3 obtains the warm air of 80-90°C output from the condenser 7 of the electric heat pump 2 in a regenerator 30, and a cold air is output from an evaporator 35.

Description

  The present invention relates to an electric heat pump and an absorption refrigerator or an absorption heat pump, or a heat source system using an electric heat pump and an adsorption refrigerator or an adsorption heat pump.

For example, when exhaust heat recovery is performed from low-temperature exhaust heat set to 60 to 70 ° C., only low temperature heat of 50 to 60 ° C. can be obtained by heat recovery using a heat exchanger or the like. Further, if heat is recovered from the low-temperature exhaust heat by a heat pump, high-temperature heat of 80 to 90 ° C. can be obtained, but cold heat cannot be extracted by this method.
As a method of taking out the cold using the heat as a driving heat source, it is conceivable to use an absorption refrigerator or an adsorption refrigerator. However, sufficient cold heat cannot be extracted with low-temperature exhaust heat of about 50 to 60 ° C.

The following Patent Document 1 discloses a configuration in which heat obtained by a compression heat pump is used as heat source water to recover heat by an absorption heat pump evaporator.
Patent Document 2 below discloses a method in which cooling and heating are simultaneously performed with a low-stage side as a refrigeration cycle using a compression refrigerator and a high-stage side as a heat pump cycle using an absorption heat pump.

JP 62-190364 A Japanese Patent Laid-Open No. 60-020065

However, Patent Document 1 discloses that the heat generated by the compression heat pump is used in the absorption heat pump, but the heat source for driving the absorption heat pump (heat supplied to the regenerator) is introduced from the outside. It is considered as high-temperature thermal energy such as steam and fuel to be burned (page 3, left upper column, lines 2 to 3 of Patent Document 1). This requires combustion heat such as gas or oil for the driving heat source, which hinders improvement in energy efficiency.
Patent Document 2 describes a combination of a compression refrigerator and an absorption heat pump, but does not disclose any specific configuration.

  This invention is made | formed in view of such a situation, Comprising: The heat source system which can carry out heat recovery from the supply heat from the low temperature waste heat made into 50-60 degreeC, and can output cold heat and / or heat efficiently. The purpose is to provide.

In order to solve the above problems, the heat source system of the present invention employs the following means.
That is, a heat source system according to the present invention includes a compressor that is driven by an electric motor to compress refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and an expansion that expands the liquid refrigerant condensed by the condenser. A vapor compression type electric heat pump having a valve and an evaporator for evaporating the refrigerant expanded by the expansion valve; a regenerator for heating and concentrating the solution to regenerate the solution; and being led from the regenerator A condenser for condensing the refrigerant, an evaporator for evaporating the liquid refrigerant condensed in the condenser, and an absorption refrigerator having an absorber for absorbing the refrigerant evaporated by the evaporator into the solution. The electric heat pump recovers heat from the supply heat from the low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and outputs the heat of 80 to 90 ° C. from the condenser. Freezing machine, with obtaining a 80-90 ° C. Thermal output from the condenser of the electric heat pump in the regenerator, and outputs the cold heat from the evaporator.

The heat source system of the present invention recovers heat from the supply heat from the low-temperature exhaust heat set to 50 to 60 ° C., outputs the heat from the condenser of the electric heat pump, and cools the heat from the evaporator of the absorption chiller (for example, Output about 7 ° C).
In the present invention, the heat obtained from the electric heat pump is supplied to the regenerator of the absorption refrigeration machine, and the heat obtained from the electric heat pump is used as a heat source for driving the absorption chiller. This eliminates the need for combustion heat such as gas or oil in order to drive the absorption refrigerator. Accordingly, it is possible to efficiently obtain cold and warm heat.

  Furthermore, in the heat source system of the present invention, the absorption chiller is configured so that the condenser outputs a heat of 60 to 70 ° C. and the evaporator supplies heat from the low-temperature exhaust heat of 50 to 60 ° C. or less. It is possible to switch to an absorption type heat pump configured to recover heat.

  The absorption refrigerator can also be used as an absorption type heat pump. Thereby, cold heat and warm heat can be switched according to demand.

  The heat source system of the present invention includes a compressor that is driven by an electric motor to compress the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and an expansion valve that expands the liquid refrigerant condensed by the condenser. And a vapor compression electric heat pump provided with an evaporator for evaporating the refrigerant expanded by the expansion valve, a regenerator for heating and concentrating the solution to regenerate the solution, and led from the regenerator A type of absorption system comprising a condenser that condenses refrigerant and outputs warm heat, an evaporator that evaporates liquid refrigerant condensed in the condenser, and an absorber that absorbs the refrigerant evaporated by the evaporator into the solution A heat pump, and the electric heat pump recovers heat from the supply heat from the low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and also generates heat of about 80 to 90 ° C. from the condenser. The absorption type heat pump obtains the heat of 80 to 90 ° C. output from the condenser of the electric heat pump in the regenerator and the low temperature exhaust heat of 50 to 60 ° C. in the evaporator. The heat is recovered from the supply heat from, and the heat of 60 to 70 ° C. is output from the condenser.

The heat source system of the present invention recovers heat from the low-temperature exhaust heat set to 50 to 60 ° C. with the evaporator of the electric heat pump and the evaporator of the absorption type heat pump, and 60 to 70 ° C. from the condenser of the absorption type heat pump. Output warm temperature (medium temperature).
In the present invention, the heat obtained from the electric heat pump is used as a heat source for driving the absorption type heat pump as the heat of 80 to 90 ° C. (supplied from the electric heat pump) is supplied to the regenerator. In order to drive the type 1 heat pump, combustion heat of gas, oil, etc. is not required, so that warm temperature (medium temperature) can be obtained efficiently.

  The heat source system of the present invention includes a compressor that is driven by an electric motor to compress the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and an expansion valve that expands the liquid refrigerant condensed by the condenser. And a vapor compression electric heat pump having an evaporator for evaporating the refrigerant expanded by the expansion valve, a regenerator for regenerating the solution by heating and condensing, and a condensation for condensing the refrigerant introduced from the regenerator A vaporizer that evaporates the liquid refrigerant condensed in the condenser, and an absorption type two-type heat pump that includes an absorber that absorbs the refrigerant evaporated by the evaporator into a solution and outputs heat. The electric heat pump recovers heat from the supply heat from the low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and outputs the heat of 80 to 90 ° C. from the condenser. The seed heat pump is characterized in that the regenerator and the evaporator obtain a heat of about 80 to 90 ° C. output from the condenser of the electric heat pump and also output a heat of 100 ° C. or more from the absorber. And

The heat source system of the present invention recovers heat from the low-temperature exhaust heat set to about 50 to 60 ° C. by an evaporator of an electric heat pump, and heat of 100 ° C. or more set to, for example, 130 ° C. from the absorber of the absorption type two heat pump. (High temperature heat) is output.
In the present invention, the heat obtained from the electric heat pump is supplied to the regenerator and the evaporator, and the heat obtained from the electric heat pump is used as a heat source for driving the absorption type two-type heat pump. Thereby, in order to drive an absorption type 2 type heat pump, combustion heat, such as gas and oil, is not needed. Therefore, warm heat (high temperature heat) can be obtained efficiently.

  Furthermore, the heat source system of the present invention is an adsorption refrigeration machine instead of the absorption refrigeration machine, or an adsorption heat pump instead of the absorption type heat pump or the absorption type two heat pump. Features.

  Thus, instead of the absorption type, an adsorption type using silica gel or the like may be used.

  Absorption chiller by supplying 80-90 ° C. heat obtained from an electric heat pump recovered from heat supplied from a low temperature heat source of 50-60 ° C. to the regenerator of the absorption chiller and using it as a driving heat source Therefore, it is possible to obtain cold and / or warm heat with high efficiency without requiring combustion heat such as gas or oil.

1st Embodiment concerning the heat-source system of this invention is shown, (a) Schematic block diagram, (b) is a figure which shows a heat balance. 2nd Embodiment concerning the heat-source system of this invention is shown, (a) Schematic block diagram, (b) is a figure which shows a heat balance. 3rd Embodiment concerning the heat-source system of this invention is shown, (a) Schematic block diagram, (b) is a figure which shows a heat balance. It is a schematic block diagram of 4th Embodiment concerning the heat-source system of this invention. It is the schematic block diagram which showed the case where only low temperature warm water is supplied with the heat-source system of FIG. It is the schematic block diagram which showed the case where low temperature warm water and medium temperature warm water are supplied with the heat source system of FIG. It is the schematic block diagram which showed the case where low temperature warm water, high temperature warm water, and cold water are supplied with the heat-source system of FIG. It is the schematic block diagram which showed the case where low temperature warm water, medium temperature warm water, and high temperature warm water are supplied with the heat-source system of FIG.

Embodiments according to the present invention will be described below with reference to the drawings.
[First Embodiment]
Hereinafter, a first embodiment of the present invention will be described with reference to FIG.
As shown in FIG. 1A, the heat source system 1 </ b> A includes an electric heat pump 2 and an absorption refrigerator 3.

The electric heat pump 2 is a turbo refrigerator. Although not shown, the turbo refrigerator is driven by an electric motor to compress a refrigerant, a turbo compressor 5, a condenser 7 that condenses the refrigerant compressed by the turbo compressor 5, and a condensed liquid refrigerant that expands. An expansion valve 9 and an evaporator 11 for evaporating the expanded refrigerant are provided.
The heat pump 2 typically includes a turbo refrigerator using a turbo compressor as in the present embodiment, but other vapor compression heat pumps using a screw type or scroll type compressor. But you can.

  The turbo compressor 5 may be a fixed speed that rotates at a constant speed, or may be a variable speed that is variable in frequency by inverter drive.

  The evaporator 11 is thermally connected by a low-temperature water pipe 13 to a heat recovery heat exchanger 15 that exchanges heat with low-temperature exhaust heat of 60 to 70 ° C. or less. Low temperature water as a heat medium circulates in the low temperature water pipe 13, and is circulated between the heat recovery heat exchanger 15 and the evaporator 11 by a low temperature water pump 17. For example, low-temperature water of 50 ° C. obtained from the heat recovery heat exchanger 15 flows into the evaporator 11, and the low-temperature water cooled to 45 ° C. by removing the latent heat of evaporation from the refrigerant in the evaporator 11 is heat recovery heat. It is sent back to the exchanger 15. Thus, the evaporator 11 recovers heat from the heat recovery heat exchanger 15.

  The condenser 7 is thermally connected to a thermal load (high temperature) 21 by a thermal output pipe 19. High-temperature water as a heat medium circulates in the high-temperature water output pipe 19 and is circulated between the condenser 7 and the thermal load (high temperature) 21 by a high-temperature water pump 23. For example, high-temperature water of 90 ° C. is output from the condenser 7 toward the thermal load (high temperature) 21, and the high-temperature water whose temperature is reduced to, for example, 85 ° C. at the thermal load (high temperature) 21 is the condenser. 7 is returned. Thus, the condenser 7 outputs the high temperature water set to 80-90 degreeC.

  Connected to the high temperature water output pipe 19 is a high temperature water supply pipe 25 for supplying high temperature water to the absorption refrigerator 3. A part of the high-temperature water is branched by the high-temperature water supply pipe 25, led to the regenerator 30 of the absorption refrigeration machine 3, and then returned to the high-temperature water output pipe 19 after passing through the regenerator 30. ing.

  The absorption chiller 3 includes a regenerator 30 that is supplied with warm heat to heat and concentrate the solution to regenerate, a condenser 32 that condenses the refrigerant guided from the regenerator 30, and a liquid condensed in the condenser 32. An evaporator 35 that evaporates the refrigerant and an absorber 37 that absorbs the refrigerant evaporated by the evaporator 35 into the solution are provided.

  As described above, the regenerator 30 is supplied with high-temperature water at 90 ° C., for example, via the high-temperature water supply pipe 25. That is, the high-temperature water output from the electric heat pump 2 is used as a heat source for driving the absorption refrigerator 3.

  The condenser 32 is cooled by cooling water. The cooling water is circulated between the cooling tower 41, the absorber 37, and the condenser 32 by a cooling water pump 39. The cooling water temperature before flowing into the cooling tower 41 through the condenser 32 is, for example, 37.5 ° C., and the cooling water cooled to, for example, 32 ° C. by the cooling tower 41 flows into the absorber 37. It is like that.

  The evaporator 35 is thermally connected to the cold load 45 by a cold water pipe 43. Cold water as a heat medium flows through the cold water pipe 43 and is circulated between the evaporator 35 and the cold load 45 by a cold water pump 47. From the evaporator 35, for example, chilled water at 7 ° C. is output toward the cooling load 45, and the chilled water whose temperature has increased to, for example, 12 ° C. at the cooling load 45 is returned to the evaporator 35. ing. Thus, the evaporator 35 of the absorption refrigeration machine 3 outputs cold water set to 7 ° C., for example.

  As described above, the heat source system 1A having the above configuration recovers heat from the low-temperature exhaust heat of 50 to 60 ° C. by the electric heat pump 2 and supplies high-temperature water of 80 to 90 ° C. to the heat load (high temperature) 21 and the electric heat pump. Cold water is output from the absorption refrigerator 3 that operates using the high-temperature water of 80 to 90 ° C. output by 2 as a heat source for driving.

FIG. 1B shows the heat balance of the heat source system 1A of the present embodiment. As shown in the figure, when the heat quantity of 60 to 70 ° C. of the low-temperature exhaust heat is “1”, the heat exchanger for heat recovery is caused by the heat loss due to heat exchange with the low-temperature water led from the low-temperature water pipe 13. 15 to 50 ° C. The heat quantity of “1” that has decreased to 50 ° C. is recovered by the electric heat pump 2, and if the input heat quantity of power of the turbo compressor 5 is set to “0.2”, the electric heat pump 2 has a heat quantity of “1.2” of 90 Outputs heat of ℃. A heat amount “0.6”, which is half of the heat output of the electric heat pump 2, is supplied to the heat load (high temperature) 21, and the other half of the heat amount “0.6” is supplied as a heat source for driving the absorption refrigerator 3. Use as When the COP of the absorption chiller 3 is set to 0.8, 7 ° C. cold with a calorie “0.5” can be supplied to the cold load 45. On the other hand, the heat quantity “1.1” is exhausted in the cooling tower 41.
In the COP as the entire heat source system, the input heat amount is “0.2” of the turbo compressor 5, the heat output to the heat load (high temperature) 21 is “0.6”, and the heat output to the heat load 45 is “ 0.5 ", so 5.5 ((0.6 + 0.5) /0.2).

As described above, according to the heat source system 1A according to the present embodiment, heat is recovered from the supply heat from the low-temperature exhaust heat set to 50 to 60 ° C., and the heat is output from the condenser 7 of the electric heat pump 2. Cold heat (for example, 7 ° C.) can be output from the evaporator 35 of the absorption refrigerator 3 with a high efficiency of COP 5.5.
Moreover, the high temperature water obtained from the electric heat pump 2 is supplied to the regenerator 30 of the absorption refrigeration machine 3 as high temperature water of 80 to 90 ° C., and the high temperature water obtained from the electric heat pump 2 is used as a heat source for driving the absorption refrigeration machine 3. Since it is used, combustion heat such as gas or oil is not required to drive the absorption refrigerator 3. Accordingly, it is possible to efficiently obtain cold and warm heat.

[Second Embodiment]
Next, a second embodiment of the present invention will be described with reference to FIG.
This embodiment is different from the first embodiment in that the absorption chiller 3 of the first embodiment is changed to an absorption type one-type heat pump and is configured to output intermediate temperature water without generating cold output. To do. Other common configurations are denoted by the same reference numerals and description thereof is omitted.
As shown in FIG. 2A, the heat source system 1B includes an electric heat pump 2 that recovers exhaust heat from low-temperature exhaust heat and outputs high-temperature water at 80 to 90 ° C., as in the first embodiment. A type 1 heat pump 4 is provided.

  The high-temperature water that is the heat output of the electric heat pump 2 is supplied to the regenerator 35 of the absorption type heat pump 4 through the high-temperature water output pipe 19. As described above, since all the high-temperature water is supplied to the absorption type heat pump 4, the heat source system 1B of the present embodiment is not configured to supply high-temperature water to an external thermal load.

  The evaporator 35 of the absorption type heat pump 4 is supplied with low-temperature water of about 50 ° C. that is heat-exchanged by the heat recovery heat exchanger 15. Thus, the evaporator 35 recovers heat from the low-temperature exhaust heat.

  The absorber 37 and the condenser 32 and the thermal load (intermediate temperature) 53 are thermally connected by an intermediate hot water pipe 51. In other words, the intermediate warm water heated by the intermediate warm water pump 52 through the absorber 37 and the condenser 32 is supplied to the thermal load (intermediate temperature) 53. The warm load (medium temperature) 53 is supplied with, for example, medium-temperature water of 60 to 70 ° C., and the medium-temperature water whose temperature is lowered to 55 ° C., for example, is returned to the absorber 37.

  As described above, the heat source system 1B of the present embodiment recovers heat by the electric heat pump 2 from the supply heat from the low-temperature exhaust heat of 50 to 60 ° C., and absorbs the high-temperature water of 80 to 90 ° C. as a driving heat source. 4, and the absorption type heat pump 4 supplies medium temperature water at 60 ° C., for example, to a heat load (medium temperature) 53.

  FIG. 2B shows the heat balance of the heat source system 1B of the present embodiment. As shown in the figure, the heat quantity “2” is obtained from the low-temperature exhaust heat, and the low-temperature water at 50 ° C. after heat exchange by the heat recovery heat exchanger 15 is converted into the electric heat pump 2 and the absorption type heat pump 4. Each is supplied with an amount of heat of “1”. The electric heat pump 2 supplies high-temperature water of 90 ° C. having a heat quantity of “1.2” to the absorption type heat pump 4 as a driving heat source. The absorption type heat pump 4 uses a heat quantity “1.2” obtained from the electric heat pump 2 and a heat quantity “1” recovered from the low-temperature exhaust heat to heat a medium temperature water of 60 ° C. with a heat quantity “2.2” as a thermal load. Output to (medium temperature) 53.

Thus, according to this embodiment, heat is recovered by the evaporator 11 of the electric heat pump 2 and the evaporator 35 of the absorption type heat pump 4 from the supply heat from the low-temperature exhaust heat set to about 50 ° C., and the absorption type A heat of about 60 ° C. (medium temperature) is output from the condenser 32 of the heat pump 4.
Further, since the heat obtained from the electric heat pump 2 is supplied to the regenerator 30, the heat obtained from the electric heat pump 2 is used as a heat source for driving the absorption type heat pump 4. In order to drive the heat pump 4, combustion heat such as gas or oil is not required. Therefore, warm heat (medium warm heat) can be obtained efficiently.

[Third Embodiment]
Next, a third embodiment of the present invention will be described with reference to FIG.
In the present embodiment, the absorption refrigeration machine 3 of the first embodiment is changed to an absorption type two-type heat pump, and the configuration is such that high-temperature water at 100 ° C. or higher is output without generating cold output. This is different from the first embodiment. Other common configurations are denoted by the same reference numerals and description thereof is omitted.
Further, the present embodiment is different in that the absorption type heat pump 4 of the second embodiment is changed to an absorption type 2 heat pump. A feature of this embodiment is that hot water having a temperature higher than that of the second embodiment can be output.

As shown in FIG. 3A, the heat source system 1C includes an electric heat pump 2 that recovers exhaust heat from low-temperature exhaust heat and outputs high-temperature water at 80 to 90 ° C., as in the first embodiment. A type 2 heat pump 6 is provided.
The high temperature water that is the thermal output of the electric heat pump 2 is supplied from the high temperature water output pipe 19 to the regenerator 35 of the absorption type two heat pump 6 through the high temperature water supply pipe 25 and also to the evaporator 35. It has become so. As described above, since all the high-temperature water is supplied to the absorption type two-type heat pump 6, the heat source system 1C of the present embodiment is not configured to supply high-temperature water to an external thermal load.

  The condenser 32 of the absorption type two-type heat pump 6 is cooled by cooling water. The cooling water is circulated between the cooling tower 41 and the condenser 32 by a cooling water pump 39. The cooling water temperature before passing through the condenser 32 and flowing into the cooling tower 41 is, for example, 37.5 ° C., and the cooling water cooled to, for example, 32 ° C. by the cooling tower 41 is returned to the condenser 32. It has become so.

  The absorber 37 and the thermal load (high temperature) 55 are thermally connected by a high-temperature water pipe 57. That is, the high temperature water heated through the absorber 37 by the high temperature water pump 59 is supplied to the thermal load (high temperature) 55. The hot load (high temperature) 55 is supplied with, for example, high-temperature water of about 100 ° C. or higher, which is about 130 ° C., for example, and high-temperature water whose temperature has been reduced to 120 ° C. is returned to the absorber 37.

  As described above, the heat source system 1C of the present embodiment recovers heat by the electric heat pump 2 from the supply heat from the low-temperature exhaust heat of 50 to 60 ° C., and absorbs two kinds of high-temperature water of 80 to 90 ° C. as the driving heat source. This is supplied to the heat pump 6, and the absorption type two heat pump 6 supplies high-temperature water, for example, at 130 ° C., to the heat load (high temperature) 55.

  FIG. 3B shows a heat balance of the heat source system 1C of the present embodiment. As shown in the figure, the heat quantity “1” is obtained from the low-temperature exhaust heat, and low-temperature water at 50 ° C. after heat exchange is performed by the heat recovery heat exchanger 15 is supplied to the electric heat pump 2. The electric heat pump 2 supplies high-temperature water of 90 ° C. having a heat quantity of “1.2” to the absorption type two heat pump 6 as a driving heat source. The absorption type two-type heat pump 6 outputs 130 ° C. high-temperature water having a heat quantity “0.6” to a heat load (high temperature) 55 based on the heat quantity “1.2” obtained from the electric heat pump 2.

Thus, according to this embodiment, heat is recovered by the evaporator 11 of the electric heat pump 2 from the low-temperature exhaust heat set to 50 to 60 ° C., and 130 ° C., for example, from the absorber 37 of the absorption type two-type heat pump 6. The heated heat (high temperature water) of 100 ° C. or higher is output.
Further, 90 ° C. high-temperature water obtained from the electric heat pump 2 is supplied to the regenerator 30 and the evaporator 35, and the heat obtained from the electric heat pump 2 is used as a heat source for driving the absorption type two-type heat pump 6. . Thereby, in order to drive the absorption type 2 type heat pump 6, combustion heat, such as gas and oil, is not required. Therefore, warm heat (high temperature heat) can be obtained efficiently.

[Fourth Embodiment]
Next, a fourth embodiment of the present invention will be described with reference to FIGS.
In the present embodiment, the absorption refrigerator 3 of the first embodiment can be switched to the absorption type heat pump 4 of the second embodiment. Therefore, the same reference numerals are given to configurations common to the first embodiment and the second embodiment, and description thereof is omitted.

  The heat source system 1D of the present embodiment includes an electric heat pump 2 and an absorption chiller 3 as in the first embodiment. Further, the absorption refrigerator 3 can be operated as an absorption type heat pump shown in the second embodiment by changing the flow path of the heat medium by various three-way valves as described below. ing.

As shown in FIG. 4, the low-temperature water pipe 13 branches to the low-temperature water branch pipe 61 via the low-temperature three-way valves 60 a and 60 b so that the low-temperature water is supplied to the thermal load (low temperature) 62. It has become.
The low-temperature water pipe 13 is provided with heat recovery three-way valves 64a and 64b, and these three-way valves 64a and 64b enable heat recovery when the absorption chiller 3 operates as a kind of heat pump. ing.
The high-temperature water output pipe 19 is provided with high-temperature water supply three-way valves 66 a and 66 b, and distributes the flow of high-temperature water toward the heat load (high temperature) 21 and the regenerator 30.
The chilled water pipe 43 connected to the evaporator 35 of the absorption chiller 3 is provided with chilled water three-way valves 68a and 68b. When operating as a refrigerator, the chilled water is transferred from the evaporator 11 to the cooling load 45. When supplying and operating as a kind of heat pump, low temperature water is led from the heat recovery heat exchanger 15 to the evaporator 35 so as to recover heat from the low temperature exhaust heat.
A three-way valve for intermediate temperature water 70 is provided between the thermal load (intermediate temperature) 53 and the absorber 37, and the cooling water led from the cooling tower 41 when the absorption refrigerator 3 operates as a refrigerator. When operating as a kind of heat pump, the absorber 37 and the thermal load (medium temperature) 53 are connected.
A cooling water three-way valve 72 is provided between the condenser 32 and the cooling tower 41. When the absorption chiller 3 operates as a refrigerator, the condenser 32 and the cooling tower 41 are connected to each other. When operating as a heat pump, a condenser and a thermal load (medium temperature) 53 are connected.
Each three-way valve described above may be replaced with two two-way valves.

  As will be described below, the heat source system 1D of the present embodiment can output low-temperature water of about 50 ° C., medium-temperature water of about 60 ° C., high-temperature water of about 90 ° C., and cold water of about 7 ° C. .

  When using only low-temperature water at about 50 ° C., as indicated by the thick line in FIG. 5, the low-temperature three-way valves 60a and 60b are switched, and the total amount of low-temperature water recovered from the low-temperature exhaust heat is heated ( (Low temperature) 62.

  When using low-temperature water of about 50 ° C. and high-temperature water of about 90 ° C., as indicated by the thick lines in FIG. 6, the low-temperature exhaust heat is adjusted by adjusting the valve openings of the low-temperature three-way valves 60a and 60b. While supplying a part of the low-temperature water recovered from the heat to the heat load (low temperature) 62, the remaining low-temperature water is supplied to the evaporator 11 of the electric heat pump 2. High temperature water is obtained from the condenser 7 of the electric heat pump 2 at a thermal load (high temperature) 21.

When using low-temperature water of about 50 ° C., high-temperature water of about 90 ° C. and cold water, that is, when used as in the first embodiment, as shown by the thick line in FIG. 7, the low-temperature three-way valve 60a , 60 b is adjusted to supply a part of the low-temperature water recovered from the low-temperature exhaust heat to the thermal load (low temperature) 62 and the remaining low-temperature water to the evaporator 11 of the electric heat pump 2. To do. High temperature water is obtained from the condenser 7 of the electric heat pump 2 at a thermal load (high temperature) 21. Moreover, about 90 degreeC high temperature water from the electric heat pump 2 is supplied to the regenerator 30 of the absorption refrigeration machine 2 by adjusting the opening degree of the three-way valves 66a and 66b for supplying high temperature water.
The cold water three-way valves 68 a and 68 b connect the evaporator 35 and the cold load 45 so as to supply cold water to the cold load 45.
In addition, the valve directions of the three-way valve for medium temperature water 70 and the three-way valve 72 for cooling water are determined so that the cooling water circulates through the condenser 32, the cooling tower 41, and the absorber 37.

When using low-temperature water of about 50 ° C., high-temperature water of about 90 ° C. and medium-temperature water of about 60 ° C., that is, when used as in the second embodiment, as shown by the thick line in FIG. The low-temperature three-way valves 60a and 60b are adjusted in valve opening so that a part of the low-temperature water recovered from the low-temperature exhaust heat is supplied to the thermal load (low-temperature) 62 and the remaining low-temperature water is evaporated by the electric heat pump 2 Supply to the vessel 11. High temperature water is obtained from the condenser 7 of the electric heat pump 2 at a thermal load (high temperature) 21. Moreover, about 90 degreeC high temperature water from the electric heat pump 2 is supplied to the regenerator 30 of the absorption refrigeration machine 2 by adjusting the opening degree of the three-way valves 66a and 66b for supplying high temperature water.
The three-way valves 64a and 64b for heat recovery are adjusted in valve opening so that the evaporator 35 of a kind of heat pump recovers heat from low-temperature exhaust heat. Then, the direction of the cold water three-way valves 68 a and 68 b is determined so that the heat recovery heat exchanger 15 and the evaporator 35 are connected so that the low temperature water is guided to the evaporator 35.
Further, the valve directions of the three-way valve for medium-temperature water 70 and the three-way valve 72 for cooling water are determined so that the medium-temperature water heated by the condenser 32 circulates through the heat load (medium temperature) 53 and the absorber 37. The

As described above, according to the present embodiment, the absorption refrigeration machine 2 can be used as an absorption type heat pump as well, so that it is possible to switch between cold and hot (medium and high temperature water) according to demand.
Further, the low-temperature water recovered from the low-temperature exhaust heat can be used at the heat load (low temperature) 62.

  In each of the above-described embodiments, an absorption refrigerator or an absorption heat pump has been described. However, an absorption refrigerator or an adsorption heat pump using silica gel or the like can be used instead of the absorption type.

1A, 1B, 1C, 1D Heat source system 2 Electric heat pump 3 Absorption type refrigerator 4 Absorption type 1 heat pump 5 Turbo compressor 6 Absorption type 2 heat pump 7 Condenser 9 Expansion valve 11 Evaporator 30 Regenerator 32 Condenser 35 Evaporator 37 Absorber

Claims (5)

A compressor that is driven by an electric motor to compress the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that expands the liquid refrigerant condensed by the condenser, and an expansion valve that is expanded by the expansion valve A vapor compression electric heat pump equipped with an evaporator for evaporating the refrigerant,
A regenerator that regenerates the solution by heating and concentrating by supplying warm heat, a condenser that condenses the refrigerant led from the regenerator, an evaporator that evaporates the liquid refrigerant condensed in the condenser, and the evaporation An absorption refrigerator having an absorber that absorbs the refrigerant evaporated by the vessel into the solution;
With
The electric heat pump recovers heat from supply heat from low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and outputs warm heat of 80 to 90 ° C. from the condenser.
The absorption refrigeration apparatus obtains a heat of 80 to 90 ° C. output from the condenser of the electric heat pump by the regenerator, and outputs a cold heat from the evaporator.   In the absorption refrigerator, the condenser is configured to output heat from 60 to 70 ° C., and the evaporator is configured to recover heat from supply heat from the low-temperature exhaust heat from 50 to 60 ° C. The heat source system according to claim 1, wherein the heat source system is switchable to a kind of heat pump. A compressor that is driven by an electric motor to compress the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that expands the liquid refrigerant condensed by the condenser, and an expansion valve that is expanded by the expansion valve A vapor compression electric heat pump equipped with an evaporator for evaporating the refrigerant,
A regenerator for heating and concentrating and regenerating a solution supplied with warm heat, a condenser for condensing refrigerant guided from the regenerator and outputting warm heat, and an evaporator for evaporating liquid refrigerant condensed in the condenser And an absorption type heat pump including an absorber that absorbs the refrigerant evaporated by the evaporator into a solution;
With
The electric heat pump recovers heat from supply heat from low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and outputs warm heat of 80 to 90 ° C. from the condenser.
The absorption type heat pump obtains the heat of 80 to 90 ° C. output from the condenser of the electric heat pump in the regenerator and supplies from the low temperature exhaust heat of 50 to 60 ° C. in the evaporator. A heat source system that recovers heat from heat and outputs heat of 60 to 70 ° C. from the condenser. A compressor that is driven by an electric motor to compress the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that expands the liquid refrigerant condensed by the condenser, and an expansion valve that is expanded by the expansion valve A vapor compression electric heat pump equipped with an evaporator for evaporating the refrigerant,
A regenerator that regenerates the solution by heating and concentrating, a condenser that condenses the refrigerant guided from the regenerator, an evaporator that evaporates the liquid refrigerant condensed in the condenser, and a refrigerant evaporated by the evaporator Absorption type two heat pumps equipped with an absorber that absorbs heat into the solution and outputs heat,
With
The electric heat pump recovers heat from supply heat from low-temperature exhaust heat of 50 to 60 ° C. in the evaporator and outputs warm heat of 80 to 90 ° C. from the condenser.
The absorption type two-type heat pump obtains a heat of 80 to 90 ° C. output from the condenser of the electric heat pump by the regenerator and the evaporator, and outputs a heat of 100 ° C. or more from the absorber. A heat source system characterized by that.   The absorption type refrigerator is replaced with an absorption type refrigerator, or the absorption type heat pump or the absorption type two heat pump is replaced with an absorption type heat pump. The heat source system according to any one of the above.

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