JP4887872B2 - Absorption refrigeration system - Google Patents

Description

  The present invention relates to an absorption refrigeration apparatus.

  LiBr type absorption refrigeration apparatuses that utilize changes in the concentration of LiBr aqueous solution are well known in the past. In this type of absorption refrigeration apparatus, the solution (concentrated solution) that enters the absorber is used as an air-cooled heat exchanger. In the absorber, an indirect air cooling (solution separation cooling) system in which only the refrigerant vapor (water vapor) is absorbed by the solution has been proposed (see Patent Document 1).

JP-A-7-98163.

  By the way, when the indirect air cooling (solution separation cooling) method disclosed in Patent Document 1 is adopted, the mass transfer called absorption of refrigerant vapor and the heat transfer called cooling are separated, so the absorber is downsized. However, since the absorption heat of the refrigerant vapor is processed only by the sensible heat of the supercooled solution, the solution temperature at the absorber outlet is the case of the conventional direct air cooling method. The evaporating temperature in the evaporator rises and the cold water outlet temperature (that is, the use side temperature) in the evaporator becomes difficult to decrease. In addition, when the indirect air cooling (solution separation cooling) method is adopted, the exhaust heat temperature in the generator becomes high, resulting in a problem that the amount of exchange heat in the generator is reduced.

  The present invention has been made in view of the above points, and it is an object of the present invention to make it possible to reduce the temperature of the chilled water outlet (that is, the use side temperature) and to reduce the exhaust heat temperature at the generator. It is said.

In the present invention, as a first means for solving the above problems, the generator G, the condenser C that condenses and liquefies the refrigerant vapor Rs obtained from the generator G, and the liquid condensed and liquefied by the condenser C An evaporator E for evaporating and evaporating the refrigerant Rw, and a refrigerant solution Rc evaporated and evaporated by the evaporator E is absorbed in the concentrated solution Lc obtained by the generator G, and a dilute solution Ld supplied to the generator G is obtained. In the absorption refrigeration apparatus including the absorber A to be generated, the units U and U formed by horizontally arranging and integrating the evaporator E and the absorber A are stacked in two stages in the vertical direction, and the lower side absorption is performed. A reflux circuit 6 is provided for refluxing the upper part of the upper absorber A in a state where most of the dilute solution Ld from the outlet of the vessel A is supercooled by the air-cooling heat exchanger Ha, while the upper evaporator. Absorption on the heat exchanging part 7 and the lower side in E With a refrigerant circuit 9 provided and the refrigerant circuit 9 for circulating a heat-exchange unit 8 in A is fluorocarbon refrigerant configured to natural circulation, a dilute solution Ld from the exit of the absorber A of the lower side second A second recirculation circuit 12 that recirculates in the upper part of the lower-stage absorber A in a state of being supercooled by the air-cooled heat exchanger Ha ′ is attached .

By configuring as described above, most of the diluted solution Ld from the outlet of the lower-side absorber A is refluxed to the upper portion of the upper-side absorber A in the supercooled state via the air-cooled heat exchanger Ha. However, a part of the diluted solution Ld from the outlet of the lower-stage absorber A is concentrated in the generator G to become a concentrated solution, and the concentrated solution Lc is supplied to the upper part of the upper-stage absorber A. Therefore, in the units U and U, in the upper-side absorber A, the refrigerant vapor Rs evaporated by the upper-stage evaporator E is absorbed by the concentrated solution Ld, and the solution diluted by the absorption of the refrigerant vapor Rs is the lower-stage side. It flows into the absorber A. The absorbed heat generated at that time is removed by the sensible heat of the supercooled solution. On the other hand, in the lower-stage absorber A, the refrigerant vapor Rs evaporated in the lower-stage evaporator E is absorbed and further diluted, and the heat generated at that time is the heat of the lower-stage absorber A constituting the refrigerant circuit. It is removed by the latent heat of vaporization of the chlorofluorocarbon refrigerant flowing through the exchange unit 8. As a result, the evaporation temperature in the lower-stage evaporator E can be lowered, the evaporation temperature in the upper-stage evaporator E can be increased, the refrigerating capacity on the lower stage side can be secured, and the lower stage As the concentration of the solution at the outlet of the absorber A on the side decreases, the temperature of the heating medium (for example, waste water) Wh in the generator G decreases, and the amount of heating in the generator G increases. In addition, since the refrigerant circuit 9 naturally circulates the chlorofluorocarbon-based refrigerant, no pressure-feeding means for circulating the refrigerant is required, and the cost can be reduced. The second reflux circuit 12 circulates the dilute solution Ld from the outlet of the lower-stage absorber A to the upper portion of the lower-stage absorber A while being supercooled by the second air-cooled heat exchanger Ha ′. As a result, a part of the dilute solution Ld from the lower absorber A is supercooled by the second air-cooled heat exchanger Ha ′ and then refluxed to the upper portion of the lower absorber A. Thus, the absorption heat in the lower absorber A can be more effectively removed.

In the present invention, as the second means for solving the above SL problem, generator G, condenser C to condense and liquefy the refrigerant vapor Rs obtained from the generator G, which is condensed and liquefied by the condenser C The evaporator E that evaporates and vaporizes the liquid refrigerant Rw, and the dilute solution Ld that is supplied to the generator G by absorbing the refrigerant vapor Rs evaporated and evaporated in the evaporator E into the concentrated solution Lc obtained by the generator G. In the absorption refrigeration apparatus provided with the absorber A that produces the above, the units U and U, in which the evaporator E and the absorber A are horizontally aligned and integrated, are stacked in two stages in the vertical direction, and the lower stage side While a reflux circuit 6 is attached to the upper part of the upper absorber A in a state where most of the dilute solution Ld from the outlet of the absorber A is supercooled by the air-cooling heat exchanger Ha, the upper side evaporation is performed. Absorption in the heat exchanging part 7 and the lower stage in the heater E A refrigerant circuit 9 that circulates through the heat exchange section 8 in A is provided, and the refrigerant circuit 9 is configured so that the chlorofluorocarbon refrigerant naturally circulates, and the dilute solution Ld that exits the air-cooled heat exchanger Ha is And it is constituted so that it may recirculate to the upper part of absorbers A and A of the lower stage side, respectively.

By configuring as described above, most of the diluted solution Ld from the outlet of the lower-side absorber A is refluxed to the upper portion of the upper-side absorber A in the supercooled state via the air-cooled heat exchanger Ha. However, a part of the diluted solution Ld from the outlet of the lower-stage absorber A is concentrated in the generator G to become a concentrated solution, and the concentrated solution Lc is supplied to the upper part of the upper-stage absorber A. Therefore, in the units U and U, in the upper-side absorber A, the refrigerant vapor Rs evaporated by the upper-stage evaporator E is absorbed by the concentrated solution Ld, and the solution diluted by the absorption of the refrigerant vapor Rs is the lower-stage side. It flows into the absorber A. The absorbed heat generated at that time is removed by the sensible heat of the supercooled solution. On the other hand, in the lower-stage absorber A, the refrigerant vapor Rs evaporated in the lower-stage evaporator E is absorbed and further diluted, and the heat generated at that time is the heat of the lower-stage absorber A constituting the refrigerant circuit. It is removed by the latent heat of vaporization of the chlorofluorocarbon refrigerant flowing through the exchange unit 8. As a result, the evaporation temperature in the lower-stage evaporator E can be lowered, the evaporation temperature in the upper-stage evaporator E can be increased, the refrigerating capacity on the lower stage side can be secured, and the lower stage As the concentration of the solution at the outlet of the absorber A on the side decreases, the temperature of the heating medium (for example, waste water) Wh in the generator G decreases, and the amount of heating in the generator G increases. In addition, since the refrigerant circuit 9 naturally circulates the chlorofluorocarbon-based refrigerant, no pressure-feeding means for circulating the refrigerant is required, and the cost can be reduced. In addition, the dilute solution Ld exiting the air-cooled heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, so that the air-cooled heat exchanger Ha is in a supercooled state. The diluted solution Ld is refluxed to the upper portions of the upper and lower absorbers A and A, respectively, and the removal of absorbed heat in the upper and lower absorbers A and A is more effectively performed. Yes.

In the present invention, as a third means for solving the above-described problem, in the absorption refrigeration apparatus including the first or second means, the refrigerant circuit 9 is connected to the lower-stage absorber A. A refrigerant cooler Hr positioned between the heat exchanging unit 8 and the heat exchanging unit 7 in the upper-stage evaporator E and higher than the upper-stage evaporator E can also be interposed. When configured, the heat of the evaporator E on the upper stage in a state in which the chlorofluorocarbon refrigerant that has absorbed and evaporated the heat absorbed in the heat exchanging section 8 of the absorber A on the lower stage in the refrigerant circuit 9 is cooled in the refrigerant cooler Hr. The refrigerant (liquid refrigerant) supplied to the exchange unit 7 and evaporated from the condenser C in the heat exchange unit 7 is condensed and liquefied, and the refrigerating capacity in the lower-stage evaporator E is more reliably ensured. It can be secured.

In the present invention, as a fourth means for solving the above-described problem, in the absorption refrigeration apparatus including the first , second or third means, the concentrated solution Lc from the generator G and the The dilute solution Ld from the outlet of the lower-side absorber A can also be configured to merge on the inlet side of the air-cooled heat exchanger Ha. In such a case, from the lower-side absorber A, Most of the solution is recirculated to the upper part of the upper absorber A in a state where it is supercooled by the air-cooled heat exchanger Ha after joining the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G. As a result, the temperature of the solution refluxed to the absorber A on the upper stage side can be kept low, and the absorption heat can be easily removed.

In the present invention, as a fifth means for solving the above-described problem, in the absorption refrigeration apparatus including the first , second, or third means, the concentrated solution Lc from the generator G and the The dilute solution Ld from the outlet of the lower-side absorber A can also be configured to merge on the outlet side of the air-cooled heat exchanger Ha, and in this case, from the lower-side absorber A Most of the dilute solution Ld is supercooled by the air-cooling heat exchanger Ha and then merged with the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G to the upper part of the upper absorber A. As a result, the amount of heat generated in the upper absorber A can be suppressed, and the heat absorbed can be easily removed. Although the temperature of the solution refluxed to the upper absorber A is slightly higher, there is no problem because the amount of the concentrated solution Lc from the generator G is small.

According to the first means of the present invention, the generator G, the condenser C that condenses and liquefies the refrigerant vapor Rs obtained from the generator G, and the liquid refrigerant Rw condensed and liquefied by the condenser C is evaporated. An evaporator A and an absorber A that absorbs the refrigerant vapor Rs evaporated by the evaporator E into the concentrated solution Lc obtained by the generator G to generate a diluted solution Ld supplied to the generator G. In the absorption refrigeration apparatus provided, the units U and U, in which the evaporator E and the absorber A are horizontally arranged and integrated, are stacked in two stages in the vertical direction, and from the outlet of the absorber A on the lower stage side. While a reflux circuit 6 is provided for refluxing the upper part of the upper absorber A in a state in which most of the dilute solution Ld is supercooled by the air-cooled heat exchanger Ha, the heat exchanger 7 in the upper evaporator E is provided. And the heat exchanging section 8 in the lower absorber A. The provided and the refrigerant circuit 9 refrigerant circuit 9 fluorocarbon refrigerant configured to natural circulation to the unit U, in the U, the refrigerant vapor evaporated in the evaporator E in the upper side of the absorber A, the upper side Rs is absorbed by the concentrated solution Ld, and the solution diluted by the absorption of the refrigerant vapor Rs flows into the lower absorber A, and the absorbed heat generated at this time is removed by the sensible heat held by the supercooled solution. On the other hand, in the lower-stage absorber A, the refrigerant vapor Rs evaporated in the lower-stage evaporator E is absorbed and further diluted, and the heat generated at this time is absorbed by the lower-stage absorber A constituting the refrigerant circuit. Since it is removed by the latent heat of vaporization of the chlorofluorocarbon refrigerant flowing through the heat exchanging section 8, the evaporation temperature in the lower evaporator E can be lowered and the evaporation temperature in the upper evaporator E can be increased. In Thus, the refrigeration capacity on the lower side can be ensured, and the concentration of the solution at the outlet of the lower-side absorber A decreases, so that the temperature of the heating medium (for example, waste water) Wh in the generator G is reduced. There is an effect that the amount of heating in the generator G increases as the temperature decreases. In addition, since the refrigerant circuit 9 naturally circulates the chlorofluorocarbon refrigerant, there is no need for a pressure circulating means for circulating the refrigerant, and there is an effect that the cost can be reduced. The second reflux circuit 12 circulates the dilute solution Ld from the outlet of the lower-stage absorber A to the upper portion of the lower-stage absorber A while being supercooled by the second air-cooled heat exchanger Ha ′. And the dilute solution Ld discharged from the air-cooled heat exchanger Ha is recirculated to the upper parts of the upper and lower absorbers A and A, respectively, so that the air-cooled heat exchanger Ha The supercooled dilute solution Ld is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, and the absorption heat in the upper and lower absorbers A and A is further removed. There is also an effect that it can be done effectively.

According to the second means of the present invention, the generator G, the condenser C that condenses and liquefies the refrigerant vapor Rs obtained from the generator G, and the liquid refrigerant Rw condensed and liquefied by the condenser C is evaporated. An evaporator A and an absorber A that absorbs the refrigerant vapor Rs evaporated by the evaporator E into the concentrated solution Lc obtained by the generator G to generate a diluted solution Ld supplied to the generator G. In the absorption refrigeration apparatus provided, the units U and U, in which the evaporator E and the absorber A are horizontally arranged and integrated, are stacked in two stages in the vertical direction, and from the outlet of the absorber A on the lower stage side. While a reflux circuit 6 is provided for refluxing the upper part of the upper absorber A in a state in which most of the dilute solution Ld is supercooled by the air-cooled heat exchanger Ha, the heat exchanger 7 in the upper evaporator E is provided. And the heat exchanging section 8 in the lower absorber A. In the units U and U, the refrigerant vapor evaporated by the upper evaporator E in the upper absorber A in the units U and U is provided. Rs is absorbed by the concentrated solution Ld, and the solution diluted by the absorption of the refrigerant vapor Rs flows into the lower absorber A, and the absorbed heat generated at this time is removed by the sensible heat held by the supercooled solution. On the other hand, in the lower-stage absorber A, the refrigerant vapor Rs evaporated in the lower-stage evaporator E is absorbed and further diluted, and the heat generated at this time is absorbed by the lower-stage absorber A constituting the refrigerant circuit. Since it is removed by the latent heat of vaporization of the chlorofluorocarbon refrigerant flowing through the heat exchanging section 8, the evaporation temperature in the lower evaporator E can be lowered and the evaporation temperature in the upper evaporator E can be increased. In Thus, the refrigeration capacity on the lower side can be ensured, and the concentration of the solution at the outlet of the lower-side absorber A decreases, so that the temperature of the heating medium (for example, waste water) Wh in the generator G is reduced. There is an effect that the amount of heating in the generator G increases as the temperature decreases. In addition, since the refrigerant circuit 9 naturally circulates the chlorofluorocarbon refrigerant, there is no need for a pressure circulating means for circulating the refrigerant, and there is an effect that the cost can be reduced. In addition, the dilute solution Ld exiting the air-cooled heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, so that the air-cooled heat exchanger Ha is in a supercooled state. The diluted solution Ld is refluxed to the upper portions of the upper and lower absorbers A and A, respectively, and the removal of absorbed heat in the upper and lower absorbers A and A is more effectively performed. There is also an effect that can be done.

As in the third means of the present invention, in the absorption refrigeration apparatus provided with the first or second means, the refrigerant circuit 9 is connected to the heat exchanging portion 8 and the upper stage side in the lower stage absorber A. A refrigerant cooler Hr located between the upper-stage evaporator E and the heat exchanger 7 in the evaporator E can also be interposed. The fluorocarbon refrigerant that has absorbed and absorbed the heat of absorption in the heat exchanger 8 of the lower-stage absorber A is supplied to the heat exchanger 7 of the upper-stage evaporator E while being cooled in the refrigerant cooler Hr. In the heat exchanging unit 7, the refrigerant (liquid refrigerant) supplied from the condenser C is condensed and liquefied, and the refrigerating capacity in the lower-stage evaporator E can be more reliably ensured.

As in the fourth means of the present invention, in the absorption refrigeration apparatus provided with the first , second or third means, the concentrated solution Lc from the generator G and the outlet of the lower absorber A The dilute solution Ld from the air-cooled heat exchanger Ha can be combined with the diluted solution Ld from the air-cooled heat exchanger Ha. In this case, most of the solution from the lower-stage absorber A is generated. The refrigerant vapor Rs is generated in the condenser G and merged with the concentrated solution Lc, which is then supercooled by the air-cooling heat exchanger Ha, and then returned to the upper part of the upper absorber A. The temperature of the solution refluxed to the absorber A can be kept low, and the absorption heat can be easily removed.

As in the fifth means of the present invention, in the absorption refrigeration apparatus provided with the first , second or third means, the concentrated solution Lc from the generator G and the outlet of the lower absorber A And the dilute solution Ld from the air-cooled heat exchanger Ha can be combined with each other, and in that case, most of the dilute solution Ld from the lower-stage absorber A Then, after being supercooled by the air-cooling heat exchanger Ha, the refrigerant G is generated in the generator G and merged with the concentrated concentrated solution Lc to be returned to the upper-side absorber A, where the upper-side absorption is performed. The amount of absorbed heat generated in the vessel A can be suppressed, and the absorbed heat can be easily removed. Although the temperature of the solution refluxed to the upper absorber A is slightly higher, there is no problem because the amount of the concentrated solution Lc from the generator G is small.

  Hereinafter, several preferred embodiments of the present invention will be described with reference to the accompanying drawings.

First Embodiment FIG. 1 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a first embodiment of the present invention.

In this absorption refrigeration cycle, the solution is heated so that the refrigerant absorption capability of an aqueous solution (hereinafter simply referred to as a dilute solution) of an absorbent (eg, LiBr) excellent in the capability of absorbing the refrigerant (eg, water) is enhanced. A generator G for heating and concentrating (for example, waste water) Wh, and a condenser C for liquefying by introducing steam (refrigerant) Rs separated from the solution in the generator G and cooling it. , An evaporator E that introduces the liquid refrigerant Rw liquefied by the condenser C and evaporates (vaporizes) it under a low pressure, and the generator G for absorbing the vapor (refrigerant) Rs generated in the evaporator E. The absorber A containing the concentrated solution Lc concentrated in step S3, and the solution (dilute solution) Ld diluted by absorbing the vapor (refrigerant) Rs in the absorber A are sent to the generator G again to concentrate. Solution pump P for An air-cooled heat exchanger Ha that introduces a part (most part) of the dilute solution Ld discharged from the solution pump P and cools the dilute solution Ld is provided, and the dilute solution Ld from the outlet of the lower-stage absorber A is provided. Is attached to the upper part of the upper absorber A in a state of being supercooled by the air-cooling heat exchanger Ha. In the present embodiment, the reflux circuit 6 joins the concentrated solution Lc from the generator G and the diluted solution Ld from the outlet of the lower absorber A at the inlet side of the air-cooled heat exchanger Ha. A joining point 10 is provided. Code Hw is the absorber portion of a dilute solution Ld exiting A (generator dilute solution Ld supplied to G) and generator solution heat exchanger and strong solution Lc exiting from G to heat exchange, F 1 is A cooling fan that cools the condenser C by air, and F 2 is a cooling fan that cools the air-cooling heat exchanger Ha by air.

  In the absorption refrigeration cycle, the evaporator E and the absorber A are integrated to form a unit U.

  As shown in FIG. 2, the unit U is configured by horizontally integrating an evaporator E and an absorber A, and in the present embodiment, the units U and U have two stages in the vertical direction. Are stacked. Here, the evaporators E and E and the absorbers A and A in the units U and U are configured to communicate with each other.

In each unit U, a plurality of plates 1, 1... Formed by forming an evaporator E on the left side and an absorber A on the right side are stacked, and the evaporator E is supplied from a condenser C. The condensed water (liquid refrigerant) exchanges heat with the water flowing inside to evaporate, and cold water Wc is obtained as a heat source on the use side, while in the absorber A, the concentrated solution supplied from the generator G The vapor (refrigerant) Rs obtained from the evaporator E is absorbed by Lc, so that the solution concentration is diluted. Reference numeral 2 denotes a casing constituting the outer shell of the unit U, 3 denotes a spray tray for spraying the refrigerant (liquid refrigerant) Rw and the solution (dilute solution) Ld supplied to the evaporator E and the absorber A evenly, 4 Is a cold water passage, and 5 is a porous member constituting the absorber A. In addition, each said plate 1 is manufactured with a heat good conductor (for example, a steel plate, stainless steel, etc.).

  And in this Embodiment, the refrigerant circuit 9 which circulates through the heat exchange part 7 in the evaporator E of the upper stage side, and the heat exchange part 8 in the absorber A of the lower stage side is attached, and this refrigerant circuit 9 is attached. The fluorocarbon refrigerant is configured to circulate naturally.

  By configuring as described above, most of the diluted solution Ld from the outlet of the lower-side absorber A is refluxed to the upper portion of the upper-side absorber A in the supercooled state via the air-cooled heat exchanger Ha. However, a part of the diluted solution Ld from the outlet of the lower-stage absorber A is concentrated in the generator G to become a concentrated solution, and the concentrated solution Lc is supplied to the upper part of the upper-stage absorber A. Therefore, in the units U and U, in the upper-side absorber A, the refrigerant vapor Rs evaporated by the upper-stage evaporator E is absorbed by the concentrated solution Ld, and the solution diluted by the absorption of the refrigerant vapor Rs is the lower-stage side. The absorbed heat that flows into the absorber A and is generated at that time is removed by the sensible heat that the supercooled solution has. On the other hand, in the lower-stage absorber A, the refrigerant vapor Rs evaporated in the lower-stage evaporator E is absorbed and further diluted, and the heat generated at that time is absorbed by the lower-stage absorber A constituting the refrigerant circuit 9. It will be removed by the latent heat of vaporization of the chlorofluorocarbon refrigerant flowing through the heat exchange section 8. As a result, the evaporation temperature in the lower-stage evaporator E can be lowered, the evaporation temperature in the upper-stage evaporator E can be increased, the refrigerating capacity on the lower stage side can be secured, and the lower-stage side As the concentration of the solution at the outlet of the absorber A decreases, the temperature of the heating medium (for example, waste water) Wh in the generator G decreases, and the amount of heating in the generator G increases. In addition, since the refrigerant circuit 9 naturally circulates the chlorofluorocarbon-based refrigerant, no pressure-feeding means for circulating the refrigerant is required, and the cost can be reduced.

  Further, in the present embodiment, most of the solution from the lower-side absorber A is combined with the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G and then the air-cooled heat exchanger Ha. Since the solution is refluxed to the upper portion of the upper absorber A in a supercooled state, the solution temperature returned to the upper absorber A can be kept low, and the upper absorber A can be kept low. It is easy to remove the absorbed heat.

Second Embodiment FIG. 3 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a second embodiment of the present invention.

  In this case, a junction 11 where the concentrated solution Lc from the generator G is merged is provided on the outlet side of the air-cooled heat exchanger Ha in the reflux circuit 6. In this way, most of the dilute solution Ld from the lower-stage absorber A is concentrated with the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G after being supercooled by the air-cooling heat exchanger Ha. It joins and is refluxed to the upper part of the absorber A on the upper stage side, the amount of heat generated in the absorber A on the upper stage side can be suppressed, and the removal of the absorbed heat becomes easy. Although the temperature of the solution refluxed to the upper absorber A is slightly higher, there is no problem because the amount of the concentrated solution Lc from the generator G is small.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted.

Third Embodiment FIG. 4 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a third embodiment of the present invention.

  In this case, the dilute solution Ld discharged from the air-cooled heat exchanger Ha is configured to be refluxed to the upper portions of the upper and lower absorbers A and A, respectively. In this way, the dilute solution Ld that has been supercooled by the air-cooling heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, and the upper and lower absorbers. The absorption heat in A and A can be removed more effectively.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted.

Fourth Embodiment FIG. 5 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a fourth embodiment of the present invention.

  In this case, the dilute solution Ld discharged from the air-cooled heat exchanger Ha is configured to be refluxed to the upper portions of the upper and lower absorbers A and A, respectively. In this way, the dilute solution Ld that has been supercooled by the air-cooling heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, and the upper and lower absorbers. The absorption heat in A and A can be removed more effectively.

  Further, a confluence point 11 where the concentrated solution Lc from the generator G is merged is provided on the outlet side of the air-cooled heat exchanger Ha in the reflux circuit 6. In this way, most of the dilute solution Ld from the lower-stage absorber A is concentrated with the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G after being supercooled by the air-cooling heat exchanger Ha. It joins and is refluxed to the upper part of the absorber A on the upper stage side, the amount of heat generated in the absorber A on the upper stage side can be suppressed, and the removal of the absorbed heat becomes easy. Although the temperature of the solution refluxed to the upper absorber A is slightly higher, there is no problem because the amount of the concentrated solution Lc from the generator G is small.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted.

Fifth Embodiment FIG. 6 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a fifth embodiment of the present invention.

In this case, the second recirculation circuit 12 that recirculates the dilute solution Ld from the outlet of the lower-stage absorber A to the upper portion of the lower-stage absorber A while being supercooled by the second air-cooled heat exchanger Ha ′. It is attached. In this way, a part of the dilute solution Ld from the lower-side absorber A is supercooled by the second air-cooled heat exchanger Ha ′ and then refluxed to the upper portion of the lower-stage absorber A. The absorption heat in the lower absorber A can be more effectively removed. Reference numeral F 2 ′ is a cooling fan for air-cooling the second air-cooled heat exchanger Ha ′.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted.

Sixth Embodiment FIG. 7 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a sixth embodiment of the present invention.

  In this case, a junction 11 where the concentrated solution Lc from the generator G is merged is provided on the outlet side of the air-cooled heat exchanger Ha in the reflux circuit 6. In this way, most of the dilute solution Ld from the lower-stage absorber A is concentrated with the concentrated solution Lc generated by generating the refrigerant vapor Rs in the generator G after being supercooled by the air-cooling heat exchanger Ha. It joins and is refluxed to the upper part of the absorber A on the upper stage side, the amount of heat generated in the absorber A on the upper stage side can be suppressed, and the removal of the absorbed heat becomes easy. Although the temperature of the solution refluxed to the upper absorber A is slightly higher, there is no problem because the amount of the concentrated solution Lc from the generator G is small.

In addition, a second reflux circuit 12 is provided for refluxing the dilute solution Ld from the outlet of the lower-stage absorber A to the upper portion of the lower-stage absorber A while being supercooled by the second air-cooled heat exchanger Ha ′. Has been. In this way, a part of the dilute solution Ld from the lower-side absorber A is supercooled by the second air-cooled heat exchanger Ha ′ and then refluxed to the upper portion of the lower-stage absorber A. The absorption heat in the lower absorber A can be more effectively removed. Reference numeral F 2 ′ is a cooling fan for air-cooling the second air-cooled heat exchanger Ha ′.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted.

Seventh Embodiment FIG. 8 shows an absorption refrigeration cycle in an absorption refrigeration apparatus according to a seventh embodiment of the present invention.

  In this case, similarly to the third embodiment, the dilute solution Ld discharged from the air-cooling heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively. . In this way, the dilute solution Ld that has been supercooled by the air-cooling heat exchanger Ha is recirculated to the upper portions of the upper and lower absorbers A and A, respectively, and the upper and lower absorbers. The absorption heat in A and A can be removed more effectively.

Further, in the present embodiment, the refrigerant circuit 9 includes the upper evaporator E between the heat exchanger 8 in the lower absorber A and the heat exchanger 7 in the upper evaporator E. A refrigerant cooler Hr located at a higher position is interposed. If it does in this way, in the state which the refrigerant | coolant Hr cooled the refrigerant | coolant freon-type refrigerant | coolant which absorbed the heat of absorption in the heat exchanging part 8 of the absorber A of the lower stage in the refrigerant circuit 9, it cooled in the refrigerant | coolant cooler Hr, The refrigerant (liquid refrigerant) supplied to the heat exchanging unit 7 and evaporated from the condenser C in the heat exchanging unit 7 is condensed and liquefied, and the refrigerating capacity in the lower-stage evaporator E is more reliably ensured. Can be secured. Reference numeral F 3 is a cooling fan for cooling the air-cooled cooler Hr.

  Since other configurations and operational effects are the same as those in the first embodiment, the description thereof is omitted. The present embodiment can also be applied to the absorption refrigeration apparatus according to the first, second, and fourth to sixth embodiments.

  The invention of the present application is not limited to the above-described embodiments, and it goes without saying that the design can be changed as appropriate without departing from the scope of the invention.

1 is a system diagram showing an absorption refrigeration cycle in an absorption refrigeration apparatus according to a first embodiment of the present invention. 1 is a front view of an evaporator / absorber unit in an absorption refrigeration apparatus according to a first embodiment of the present invention. It is a systematic diagram which shows the absorption refrigeration cycle in the absorption refrigeration apparatus concerning 2nd Embodiment of this invention. It is a systematic diagram which shows the absorption refrigeration cycle in the absorption refrigeration apparatus concerning 3rd Embodiment of this invention. It is a systematic diagram which shows the absorption refrigerating cycle in the absorption refrigeration apparatus concerning 4th Embodiment of this invention. It is a systematic diagram which shows the absorption refrigeration cycle in the absorption refrigeration apparatus concerning 5th Embodiment of this invention. It is a systematic diagram which shows the absorption refrigeration cycle in the absorption refrigeration apparatus concerning the 6th Embodiment of this invention. It is a systematic diagram which shows the absorption refrigerating cycle in the absorption refrigeration apparatus concerning 7th Embodiment of this invention.

6 is a reflux circuit 7 is a heat exchange unit 8 is a heat exchange unit 9 is a refrigerant circuit 10 is a junction point 11 is a junction point 12 is a second reflux circuit G is a generator C is a condenser E is an evaporator A is an absorber Ha Is air cooling heat exchanger Ha 'is second air cooling heat exchanger Hw is solution heat exchanger U is unit Lc is concentrated solution Ld is dilute solution Rs is refrigerant vapor (water vapor)
Rw is liquid refrigerant (condensed water)
Wh is the heating medium (waste water)

Claims (5)

Generator (G), condenser (C) for condensing and liquefying refrigerant vapor (Rs) obtained from generator (G), and vaporizing and condensing liquid refrigerant (Rw) condensed and liquefied by condenser (C) The evaporator (E) to be evaporated and the refrigerant vapor (Rs) evaporated by the evaporator (E) are absorbed by the concentrated solution (Lc) obtained by the generator (G) and supplied to the generator (G). An absorption refrigeration apparatus provided with an absorber (A) for generating a dilute solution (Ld) to be supplied, wherein the evaporator (E) and the absorber (A) are horizontally aligned and integrated. A state where (U) and (U) are stacked in two stages in the vertical direction, and most of the diluted solution (Ld) from the outlet of the lower-side absorber (A) is supercooled by the air-cooled heat exchanger (Ha) A reflux circuit (6) for refluxing is attached to the upper part of the upper absorber (A), while the upper evaporator (E). As the definitive heat exchanger (7) and the lower side of the absorber the refrigerant circuit for circulating the heat exchange portion (8) in (A) (9) the provided and fluorocarbon refrigerant the refrigerant circuit (9) is natural circulation And the lower absorber (A) in a state where the dilute solution (Ld) from the outlet of the lower absorber (A) is supercooled by the second air-cooled heat exchanger (Ha ′). An absorption refrigeration apparatus comprising a second reflux circuit (12) that circulates at the top of the refrigeration unit. Generator (G), condenser (C) for condensing and liquefying refrigerant vapor (Rs) obtained from generator (G), and vaporizing and condensing liquid refrigerant (Rw) condensed and liquefied by condenser (C) The evaporator (E) to be evaporated and the refrigerant vapor (Rs) evaporated by the evaporator (E) are absorbed by the concentrated solution (Lc) obtained by the generator (G) and supplied to the generator (G). An absorption refrigeration apparatus provided with an absorber (A) for generating a dilute solution (Ld) to be supplied, wherein the evaporator (E) and the absorber (A) are horizontally aligned and integrated. A state where (U) and (U) are stacked in two stages in the vertical direction, and most of the diluted solution (Ld) from the outlet of the lower-side absorber (A) is supercooled by the air-cooled heat exchanger (Ha) A reflux circuit (6) for refluxing is attached to the upper part of the upper absorber (A), while the upper evaporator (E). And a refrigerant circuit (9) that circulates through the heat exchange section (7) and the heat exchange section (8) in the lower-side absorber (A), and the chlorofluorocarbon refrigerant naturally circulates through the refrigerant circuit (9). And the dilute solution (Ld) from the air-cooled heat exchanger (Ha) is recirculated to the upper and lower absorbers (A) and (A), respectively. absorption Osamushiki refrigeration equipment said. The refrigerant circuit (9) includes a heat exchange section (8) in the lower-stage absorber (A) and a heat exchange section (7) in the upper-stage evaporator (E). The absorption refrigeration apparatus according to any one of claims 1 and 2, further comprising a refrigerant cooler (Hr) positioned above the side evaporator (E). The concentrated solution (Lc) from the generator (G) and the dilute solution (Ld) from the outlet of the lower absorber (A) are merged at the inlet side of the air-cooled heat exchanger (Ha). claim 1, 2 and 3 absorption refrigerating apparatus according to any one claim of which is characterized by being configured to. The concentrated solution (Lc) from the generator (G) and the dilute solution (Ld) from the outlet of the lower absorber (A) are merged on the outlet side of the air-cooled heat exchanger (Ha). claim 1, 2 and 3 absorption refrigerating apparatus according to any one claim of which is characterized by being configured to.

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