SE2050399A1 - A reversible refrigeration system - Google Patents

Abstract

A reversible refrigeration system comprises a compressor (C) arranged to compress gaseous refrigerant, a four way valve (FWV) switchable between a heating position in which a pay load is heated and a cooling position in which the pay load is cooled. A pay load heat exchanger (PLHE) is connected to the pay load requiring heating or cooling, a dump heat exchanger (DHE), two one way valves (OWV1, OWV2), and two controllable expansion valves (EXPV1, EXPV2), wherein the oneway valves (OWV1, OWV2) each are connected parallel to a corresponding expansion valve, wherein switching of the four-way valve between the heating position and the cooling position controls a flow of pressurized refrigerant to either of the pay load heat exchanger (PLHE) or the dump heat exchanger (DHE) and wherein the heat exchanger which receives the flow of pressurized refrigerant functions as a condenser and the other heat exchanger functions as an evaporator. The dump heat exchanger (DHE), when the four-way valve is in the heating position, is connected to a suction gas heat exchanger arranged to exchange heat between liquid high pressure refrigerant having exited the pay load heat exchanger (PLHE) when the pay load heat exchanger (PLHE) functions as a condenser and low pressure gaseous refrigerant having exited the dump heat exchanger (DHE). The dump heat exchanger (DHE) is arranged to exchange heat between the refrigerant and a heat carrier to which heat can be dumped in a co-current mode.

Description

A REVERSIBLE REFRIGERATION SYSTEM FIELD OF THE INVENTION The present invention relates to a reversible refrigeration system comprising a Compressor arranged to compress gaseous refrigerant, a four way valve switchable between a heating position in which a pay load is heated and a cooling position in which the pay load is cooled, a pay load heat exchanger connected to the pay load requiring heating or cooling, a dump heat exchanger, two one way valves, and two controllable expansion valves, wherein the one-way valves each are connected parallel to a corresponding expansion valve, wherein switching of the four-way valve between the heating position and the cooling position controls a flow of pressurized refrigerant to either of the pay load heat exchanger or the dump heat exchanger and wherein the heat exchanger which receives the flow of pressurized refrigerant functions as a condenser and the other heat exchanger functions as an evaporator.

PRIOR ART In the art of refrigeration, so-called “suction gas heat exchange” is a way to improve e. g. stability of a refrigeration system. In short, suction gas heat exchange is achieved by providing for a heat exchange between warrn liquid, high pressure refrigerant from a condenser outlet and cold gaseous refrigerant from an evaporator outlet. By the suction gas heat exchange, the temperature of the cold gaseous refrigerant will increase, while the temperature of the warrn liquid will decrease. This has two positive effects: Firstly, problems with flash boiling after the warrn liquid has passed a subsequent expansion valve will decrease; Secondly, the risk of droplets in the gaseous refrigerant leaving the evaporator will decrease.

Suction gas heat exchanging is well known. Often, suction gas heat exchange is achieved by simply brazing or soldering pipes carrying refrigerant in the states between which heat exchange is desired to one another. This way of achieving the heat exchange is, however, costly in terms of refrigerant volume required - it is always benef1cial if the piping between different components of a refrigeration system is as short as possible. Suction gas heat exchange by brazing or soldering piping carrying fluids having different temperatures together necessitates longer piping than otherwise would be the case - hence, the intemal volume of the piping will increase, requiring more refrigerant in the refrigeration system. This is detrimental not only from an economical point of view, but also since the amount of refrigerant is limited in several jurisdictions.

Another option is to provide a separate heat exchanger for the suction gas heat exchange. Separate heat exchangers are more efficient than simply brazing different piping portions to one another, but the provision of a separate heat exchanger also necessitates piping connecting the evaporator and the condenser to the suction gas heat exchanger, which piping will increase the refrigerant volume of the refrigeration system.

Moreover, refrigeration systems are often required to being able to operate in both heating mode and in chiller mode, depending on the required/ desired load. Usually, the shift between heating and chilling mode is achieved by shifting a four-way valve such that an evaporator becomes a condenser and a condenser becomes an evaporator. Unfortunately, this means that the heat exchange in either or both the condenser/evaporator units will be a co-current heat exchange, i.e. a heat exchange wherein the media to exchange heat travels in the same general direction, in either heating or cooling mode. As well known by persons skilled in the art, a co-current heat exchange is inferior to a counter-current heat exchange. In evaporators, a decrease of heat exchanging performance might lead to an increased risk of droplets in the refrigerant vapor that leaves the heat exchanger. Such droplets might seriously damage a compressor and are thus highly undesirable. However, devices to shift the flow direction of the medium to exchange heat with the refrigerant in the evaporator are costly and add complexity to the refrigeration system.

It is the object of the present invention to solve or at least mitigate the above and other problems.

SUMMARY OF THE INVENTION According to the invention, the above and other problems are solved, or at least mitigated, by reversible refrigeration system comprising a compressor arranged to compress gaseous refrigerant, a four way valve switchable between a heating position in which a pay load is heated and a cooling position in which the pay load is cooled, a pay load heat exchanger connected to the pay load requiring heating or cooling, a dump heat exchanger, two one way valves, and two controllable expansion valves, wherein the one-way valves each are connected parallel to a corresponding expansion valve, wherein switching of the four-way valve between the heating position and the cooling position controls a flow of pressurized refrigerant to either of the pay load heat exchanger or the dump heat exchanger and wherein the heat exchanger which receives the flow of pressurized refrigerant functions as a condenser and the other heat exchanger functions as an evaporator, characterized in that the dump heat exchanger when the four-way valve is in the heating position is connected to a suction gas heat exchanger arranged to exchange heat between liquid high pressure refrigerant having exited the pay load heat exchanger when the pay load heat exchanger functions as a condenser and low pressure gaseous refrigerant having exited the dump heat exchange, and in that the dump heat exchanger is arranged to exchange heat between the refrigerant and a heat carrier to which heat can be dumped in a co-current mode.

Due to provision of one-way valves in the refrigeration system, the suction gas heat exchanger is inactivated when the four way valve is in the heating position.

BREF DESCRIPTION OF THE DRAWINGS In the following, the invention will be described with reference to appended drawings, wherein: Fig. 1a is a plan view of a heat exchanger according to one embodiment of the present invention; Fig. lb is a section view of the heat exchanger of Fig. la taken along the line A-A; Fig. 1c is a section view of the heat exchanger of Fig. la taken along the line B-B; Fig. 2 is an exploded perspective view of the heat exchanger of Fig. 1; Fig. 3 is an exploded perspective view of a heat exchanger according to another embodiment of the present invention, Fig. 4 is an exploded perspective view of heat exchanger according to another embodiment of the present invention; Fig 5 is an exploded perspective view of a heat exchanger according to another embodiment of the present invention; Fig. 6 is a schematic view of one embodiment of a reversible refrigeration system shown in a heating mode; Fig. 7 is a schematic view of the reversible refrigeration system of Fig. 6 shown in a cooling mode; Fig. 7b is a schematic view of another embodiment of a reversible refrigeration system; and Fig. 8 is a schematic view of four heat exchanger plates comprised in a “multi circuit” heat exchanger.

DESCRIPTION OF EMBODIMENTS In Figs. la-2, a brazed heat exchanger 100 having a second heat exchanging portion usable as an integrated suction gas heat exchanger portion is shown. The heat exchanger 100 is made from sheet metal plates 110a-10h stacked in a stack to form the heat exchanger 100 and provided with a pressed pattem of ridges R and grooves G adapted to keep the plates on a distance from one another under formation of interplate flow channels for media to exchange heat. Large port openings 02 and 03 are provided near comers of each heat exchanger plate, whereas large openings 01 and 04 are provided centrally close to a short side of each heat exchanger plate. Areas surrounding the port openings 01 to 04 are provided at different heights such that selective communication between the port openings and the interplate flow channels is achieved. In the heat exchanger 100, the areas surrounding the port openings are arranged such that the large openings 01 and 02 are in fluid communication with one another by some plate interspaces, whereas the openings 03 and 04 are in fluid communication with one another by neighboring plate interspaces.

The heat exchanger plates 110a-110h are also provided with a dividing surface DW extending from one long side of each heat exchanger plate to the other longside thereof.

The heat exchanger plate 110h is not provided with port opening. This is in order to provide a seal for the port openings, such that fluid introduced at one end of the plate stack does not immediately escape the plate pack at the other sided thereof.

With special reference to Fig. 2, a number of heat exchanger plates 210a - 210h are shown. Each of the heat exchanger plates, except the heat exchanger plate 210h, is provided with port openings 01, 02, 03, 04, S01 and S02. The port openings are surrounded by areas provided at different levels, such that selective communication is provided between the port openings and the interplate flow channels formed between neighbouring heat exchanger plates, as mentioned above. Moreover, each of the heat exchanger plate is surrounded by a skirt S, which extends generally perpendicular to a plane of the heat exchanger plate and is adapted to contact skirts of neighbouring plates in order to provide a seal along the circumference of the heat exchanger.

In order to seal the interplate flow channel for brine flow between the large port opening 04 and 03, a dividing surface DS is provided between long sides of the heat exchanger plates. The dividing surface DS comprises an elongate flat surface provided on different heights of different plates; when the surfaces of neighbouring plates contact one another, the channel will be sealed, whereas it will be open if they do not. In the present case, the dividing surface DS is provided at the same height as the areas surrounding the large port openings 01 and 02, meaning that for interplate flow channels fluidly connecting large port openings 01 and 02, the dividing surface will be open, whereas for the flow channel fluidly connecting the large port openings 03 and 04, the dividing surface will block fluid in this plate interspace.

Since the dividing surface will block fluid flow in the plate interspace communicating with the large port openings 03 and 04, there will be separate interplate channels on either side of the dividing surface DS. The interplate flow channel on the side of the dividing surface DS not communicating with the large opening 03 and 04 communicates with two small port opening S01 and S02. It should be noted that the dividing surface DS does not block the interplate flow channels communicating with the large port openings 01 and 02; hence, medium flowing in the interplate flow channels communicating with the small port openings S01 and S02 will exchange heat with med medium flowing in the flow channels communicating with the large openings 01 and 02 - just like medium flowing in the interplate flow channels communicating with the large port openings 03 and 04.

In an embodiment shown in Fig. 2, the dividing surface DS extends in a straight line from one longside to the other, passing between large port openings 01 and 04. The small openings S01 and S02 are situated on either sides of the large port opening 01. It should be noted that the large port opening 01 is placed such that medium flowing in the interplate flow channel communicating with the small port openings S01 and S02 may pass on both sides of the large port opening 01. This arrangement is benef1cial in that the port opening 01 will have an even temperature along its circumference.

In an embodiment shown in Fig. 3, the dividing surface does not extend in a straight line, but is slightly bent away from the port opening 01, which is placed near a comer of the heat exchanger. This provides for a more uniform flow area from the small opening S01 to the small opening S02.

In an embodiment shown in Fig. 4, the dividing portion extends in a semi- circular fashion around the port opening 01. This embodiment is beneficial in that the large port openings 01-04 may be placed close to the corners of the heat exchanger, hence providing for a large heat exchanging area. This embodiment is also beneficial in that the flow area of the interplate flow channel on the side of the dividing surface DS not communicating with the large opening 03 and 04 will have an even cross section all the way between the small opening S01 and the small opening S02.

In Fig5, an embodiment resembling the embodiment of Fig. 2 is shown. Just like the previously shown embodiment, the dividing surface DS extends in a straight line from one longside of the heat exchanger to the other, passing between large port openings 01 and 04. The small openings S01 and S02 are situated on either sides of the large port opening 01. However, the large port opening 01 is located and arranged such that no fluid may pass between the large port opening 01 and the short side of the heat exchanger. This is beneficial in that the heat exchange between fluid flowing between the small openings S01 and S02 and fluid about to exit the heat exchanger through the large opening 01 is improved, since the “dead area” between the port opening 01 and the short side of the heat exchanger is avoided.

In Figs. 6 and 7, a preferred embodiment of a chiller system that can use a heat exchanger according to any of the above heat exchanger embodiments is shown in in heating mode and cooling mode, respectively.

The chiller system according to the first embodiment comprises a compressor C, a four-way valve FWV, a pay load heat exchanger PLHE connected to a brine system requiring heating or cooling, a first controllable expansion valve EXPV1, a first one- way valve 0V1, a dump heat exchanger DHE connected to a heat source to which undesired heat or cold could be dumped, a second expansion valve EXPV2 and a second one-way valve 0WV2. The heat exchangers PLHE and DHE are each provided with the four large openings 01-04 as disclosed above and the two small openings S01 and S02, wherein the large openings 01 and 02 of each heat exchanger communicate with one another, the large openings 03 and 04 of each heat exchanger communicate with one another and wherein the small openings S01 and S02 of each heat exchanger communicate with one another. Heat exchange will occur between fluids flowing from 01 to 02 and fluids flowing between 03 and 04 and S01 and S02. There will, however, be no heat exchange between fluids flowing from 03 to 04 and fluids flowing from S01 to S02.

In heating mode, shown in Fig. 6, the Compressor C will deliver high pressure gaseous refrigerant to the four-way Valve FWV. In this heating mode, the four-way Valve is controlled to convey the high pressure gaseous refrigerant to the large opening 01 of the pay load heat exchanger PLHE. The high pressure, gaseous refrigerant will then pass the pay load heat exchanger PLHE and exit at the large opening 02. While passing the pay-load heat exchanger PLHE, the high pressure gaseous refrigerant will exchanger heat with a brine solution connected to a pay-load requiring heating and flowing from the large opening 04 to the large opening 03, i.e. in a counterflow direction compared to the refrigerant, which flows from the large opening 01 to the large opening 02. While exchanging heat with the brine solution, the high pressure gaseous refrigerant will condense, and when exiting the Pay-load heat exchanger PLHE through the large opening 02, it will be fully condensed, i.e. be in the liquid state.

In the heating mode, the first expansion Valve EXPV1 will be fully closed, and the flow of liquid refrigerant exiting the pay-load heat exchanger will pass the first one- way Valve 0WVl, which allows for a refrigerant flow in this direction, while it will block flow in the other direction (which will be explained later in connection to the description of the cooling mode).

After having passed the first one-way Valve 0WVl , the liquid refrigerant (still comparatively hot) will enter the small opening S02 of the dump heat exchanger DHE, and exit the heat exchanger through the small opening S01. During the passage between the small openings S02 and S01, the temperature of the refrigerant will drop significantly due to heat exchange with cold, primarily gaseous refrigerant about to exit the dump heat exchanger DHE.

After leaving the dump heat exchanger DHE through the small opening S01, the liquid refrigerant will pass the second expansion Valve EXPV2, where the pressure of the refrigerant will drop, causing flash boiling of some of the refrigerant, which will cause the temperature to drop. From the second expansion valve, the refrigerant will pass a branch connected to both the second one-way Valve 0WV2, which is connected between the high pressure side and the low pressure side of the refrigerant circuitry and closed for refrigerant flow due to the pressure difference between the high pressure side and the low pressure side. After having passed the branch, the cold, low pressure semi liquid refrigerant will enter the large opening 02 and pass the dump heat exchanger DHE under heat exchange with a brine solution connected to a source from which low temperature heat can be collected, e. g. an outside air collector, a solar collector or a hole drilled in the ground. Due to the heat exchange with the brine solution, which flows from the large opening O4 to the large opening O3, the primarily liquid refrigerant will vaporize. The heat exchange between the brine solution and the refrigerant will take place under co-current conditions, which is well known to give an inferior heat exchange perforrnance as compared to counter-current heat exchange.

Just prior to the exiting the dump heat exchanger DHE through the large opening Ol, the refrigerant (now almost completely vaporized) will exchange heat with the comparatively hot, liquid refrigerant that entered the dump heat exchanger through the small opening S02 and exited the dump heat exchanger through the small port opening SOl. Consequently, the temperature of the refrigerant about to exit the dump heat exchanger DHE through the opening Ol will increase, hence ensuring that all of this refrigerant is completely vaporized.

It is well known by persons skilled in the art that co-current heat exchange is inferior to counter-current heat exchange. However, due to the provision of the heat exchange between the relatively hot liquid brine entering the small opening SO2 and the mainly gaseous refrigerant about to leave the dump heat exchanger DHE (i.e. a so- called “suction gas heat exchange”), it is not necessary to vaporize the refrigerant completely during the brine-refrigerant heat exchange. Instead, the refrigerant may be only semi-vaporized when it enters the suction gas heat exchange with the hot liquid refrigerant, since the remaining liquid phase refrigerant will evaporate during this heat exchange. It is well known that liquid-to-liquid heat exchange is much more efficient than Gas-to-liquid heat exchange.

From the opening Ol of the dump heat exchanger, the gaseous refrigerant will enter the four-way valve FWV, which is controlled to direct the flow of gaseous refrigerant to the compressor, in which the refrigerant is compressed again.

In Fig. 7, the chiller system is shown in cooling mode. In order to switch mode from heating mode to cooling mode, the four-way valve FWV is controlled such that the compressor feeds compressed gaseous refrigerant to the opening O1 of the dump heat exchanger DHE. The expansion valve EXPV2 will be entirely closed, the one-way valve OWV2 will be open, the one-way valve OWVl will be closed and the expansion valve EXPVl will be open to control the pressure before and after the refrigerant has passed the expansion valve EXPVl.

Hence, in cooling mode, the dump heat exchanger will function as a co-current condenser, and the “suction gas heat exchanger” thereof will not perform any heat exchange, whereas the pay-load heat exchanger PLHE will function as a co-current condenser. However, due to the provision of the suction gas heat exchange between the hot liquid refrigerant and semi-vaporised refrigerant about to leave the pay-load heat exchanger PLHE, the efficiency of the co-current heat exchange can be maintained at acceptable levels.

It should be noted that the suction gas heat exchanging parts are integrated with the dump heat exchanger DHE and the pay-load heat exchanger PLHE in Figs. 6 and 7. In other embodiments, however, the suction gas heat exchangers may be separated from the dump heat exchanger and/or the pay-load heat exchanger.

In Fig. 7b, a second embodiment of a reversible refrigeration system according to the invention is shown. In general, this system is similar to the system shown in Figs 6 and 7, however with the difference that the dump heat exchanger DHE is not provided with a suction gas heat exchanging function. Also, the dump heat exchanger according to this embodiment is an outside air/refrigerant heat exchanger. Such heat exchangers are often used when it is not possible to dump the heat in e. g. a brine solution. Generally, air/refrigerant heat exchangers function in cross-current mode, meaning that the benefit of connecting an air/refrigerant heat exchanger to a suction gas heat exchanger in the manner disclosed for both the pay load heat exchanger (PLHE) and the dump heat exchanger DHE.

In Fig. 7b, the reversible refrigeration system is shown in a heating mode, i.e. the pay load heat exchanger functions as a condenser. Gaseous refrigerant is compressed in the compressor C and conveyed to the large opening Ol, from which it will pass the pay load heat exchanger PLHE and exchange heat with a medium requiring heating, i.e. the pay load. The heat exchange will take place in a counter- current mode. The refrigerant, now liquid, will thereafter pass the one-way valve OWVl and thereafter pass the expansion valve EXPV2, in which the refrigerant pressure will decrease, resulting in a corresponding decrease of boiling temperature. The decrease of the boiling temperature will enable the refrigerant to vaporize in the dump heat exchanger DHE by heat exchange with outside air, which in this embodiment will function as the heat dump. The evaporated, i.e. gaseous refrigerant will thereafter be conveyed to the compressor C, which again will compress the refrigerant. It should be noted that in this mode, i.e. when the four way valve FVW is in the heating position, there will be no or only a minor flow of refrigerant between the small openings SOl and S02. Hence, there will be no heat exchange in this part of the heat exchanger.

The reversible refrigeration system of Fig. 7b may also be used in the reverse mode, just like the embodiment shown in Figs. 6 and 7. In this mode, compressed refrigerant is directed to the dump heat exchanger DHE. Just like in the embodiment sown in Figs. 6 and 7, this is achieved by switching the four-way valve FWV. In the dump heat exchanger, the high pressure gaseous refrigerant will exchange heat with the outside air, and as a result, the refrigerant will condense. The condensed refrigerant will leave the dump heat exchanger and pass the one way valve 0WVl (which allows for a flow in this direction). Then, the refrigerant will be transferred to the small opening S02 of the pay load heat exchanger PLHE, and, under heat exchange with cold gaseous refrigerant, pass the pay-load heat exchanger PLHE under heat exchange with cold, gaseous refrigerant about to leave the pay load heat exchanger PLHE.

In still another embodiment of the invention, at least one integrated suction gas heat exchanger is provided in a so-called “multi circuit” heat exchanger, such as schematically shown in Fig. 8. A multi circuit heat exchanger is a heat exchanger having inlet and outlet port openings for three different media to exchange heat, i.e. six port openings.

In Fig. 8, an exemplary embodiment of a plate and port arrangement in a multi circuit heat exchanger 200 with integrated suction gas heat exchange possibility is shown. In the shown embodiment, four plates 20l, 202, 203, 204 are each provided with six large port openings 210a-210f and a pressed pattern of ridges R and grooves G adapted to keep the grooves on a distance from one another when the plates are stacked on top of one another, such that interplate flow channels for media to exchange heat are formed between the heat exchanger plates 2l0a-2l0f The port openings 2l0a-2l0f are provided at different heights, such that selective fluid communication between the port openings and the interplate flow channels is obtained.

In the present case, the port openings 2l0a and 2l0b are provided at the same height, meaning that they will communicate with the plate interspace between the plates 20l and 202. The port openings 2l0c and 2l0d are communicating with the plate interspace between the plates 202 and 203 and the port openings 2l0e and 2l0f communicate with the plate interspace between the plates 203 and 204.

Moreover, dividing surfaces DW are provided such that the interplate flow channels between the plates 202 and 203 is sealed off for communication, hence forrning first and second heat exchanging portions that communicate with small port openings S0l-S04, wherein the small port openings S0l and S02 communicate with the heat exchanging portion being located closest to the port opening 2l0b and wherein the small port openings S03 and S04 communicate with the heat exchanging portion being located closest to the port opening 2l0f. ll Usually, a multi Circuit heat exchanger is used where the requirements for heating and/or cooling varies within wide boundaries. In a typical setup, every other interplate flow channel (the channels communicating with the port openings 2l0c and 2l0d) is arranged for a flow of brine solution, wherein one of its neighboring interplate flow channels is arranged for a flow of a first refrigerant and its other neighboring flow channel is arranged for a flow of a second refrigerant. The first and second refrigerants are connected to separate refrigeration systems, each having its own compressor and expansion valve. When high power cooling or heating is required, both compressors are energized, whereas only one compressor is energized when the cooling or heating requirement is lower.

A multi circuit heat exchanger can be used in basically the same way as disclosed above with reference to Figs 6 and 7, however with dual compressors C, dual expansion valves EXPVl , dual expansion valves EXPV2, dual four way valves FWV, dual one-way valves OWVl and dual one-way valves OWV2.

Claims (6)

1. A reversible refrigeration system comprising a compressor (C) arranged to compress gaseous refrigerant, a four way Valve (FWV) switchable between a heating position inwhich a pay load is heated and a cooling position in which the pay load is cooled, a payload heat exchanger (PLHE) connected to the pay load requiring heating or cooling, adump heat exchanger (DHE), two one way valves (OWV1, OWV2), and twocontrollable expansion valves (EXPV1, EXPV2), wherein the one-way valves (OWV1,OWV2) each are connected parallel to a corresponding expansion valve, whereinswitching of the four-way valve between the heating position and the cooling positioncontrols a flow of pressurized refrigerant to either of the pay load heat exchanger(PLHE) or the dump heat exchanger (DHE) and wherein the heat exchanger whichreceives the flow of pressurized refrigerant functions as a condenser and the other heatexchanger fianctions as an evaporator, characterized in that the dump heat exchanger(DHE) when the four-way valve is in the heating position is connected to a suction gasheat exchanger arranged to exchange heat between liquid high pressure refrigeranthaving exited the pay load heat exchanger (PLHE) when the pay load heat exchanger(PLHE) functions as a condenser and low pressure gaseous refrigerant having exited thedump heat exchanger (DHE), and in that the dump heat exchanger (DHE) is arranged toexchange heat between the refrigerant and a heat carrier to which heat can be dumped in a co-current mode.

2. The reversible refrigeration system according to claim 1, wherein, when the four way valve (FW V) is in the heating position, the suction gas heat exchanger is inactivated.

3. The reversible refrigeration system of claim 1 or 2, wherein a second suction gasheat exchanger is arranged to exchange heat between liquid refrigerant having exited thedump heat exchanger (DHE) and gaseous refrigerant having exited the pay load heatexchanger (PLHE) when the four way valve (FWV) is in the cooling position.

4. The reversible refrigeration system of any of the preceding claims, wherein the suction gas heat exchanger is integrated in the dump heat exchanger (DHE). 13

5. The reversible refrigeration system of claini 3 or 4, Wherein the second suction gas heat exchanger is integrated in the pay load heat exchanger (PLHE).

6. The reversible refrigeration system of claini 3 or 4, Wherein the second suction gas heat exchanger is integrated in the pay load heat exchanger (PLHE).