COOLING DEVICE WITH A SUCTION TUBE HEAT EXCHANGER AND METHOD FOR OPERATING A COOLING DEVICE WITH A SUCTION TUBE HEAT EXCHANGER

Abstract

A refrigeration device has a coolant circuit with a compressor, a first evaporator assembly, and a high-pressure tube connected upstream of the first evaporator assembly. A second evaporator assembly is connected in parallel with the first evaporator assembly. A low-pressure tube is connected downstream of the first and second evaporator assemblies. A suction tube heat exchanger has a high-pressure tube section of the high-pressure tube and a low-pressure tube section of the low-pressure tube heat-conductively coupled. The suction tube heat exchanger has three temperature sensors in three positions from a group of positions at the inlet and outlet of the low-pressure tube section, and at the inlet and outlet of the high-pressure tube section. A ratio of the mass flow of coolant to the first evaporator assembly relative to the total mass flow of the coolant can be determined.

Claims

1-14. (canceled)

15. A refrigeration appliance, comprising: a refrigerant circuit with a compressor, a first evaporator assembly having at least one first evaporator, a high-pressure tube connected upstream of said first evaporator assembly, a second evaporator assembly connected in parallel with said first evaporator assembly and having at least one second evaporator, and a low-pressure tube connected downstream of said first evaporator assembly and said second evaporator assembly; a suction tube heat exchanger, in which a high-pressure tube section of said high-pressure tube and a low-pressure tube section of said low-pressure tube are heat-conductively coupled; said suction tube heat exchanger having three temperature sensors at three positions selected from a group of positions at an inlet and at an outlet of said low-pressure tube section, and at an inlet and at an outlet of said high-pressure tube section.

16. The refrigeration appliance according to claim 15, wherein said high-pressure tube section leads exclusively to said first evaporator assembly and does not lead to said second evaporator assembly.

17. The refrigeration appliance according to claim 15, which comprises a variably adjustable flow restriction element connected upstream and downstream respectively of said first evaporator and said second evaporator.

18. The refrigeration appliance according to claim 17, wherein said variably adjustable flow restriction element is an expansion valve.

19. The refrigeration appliance according to claim 15, wherein said suction tube heat exchanger has a temperature sensor at each position of the group of positions.

20. The refrigeration appliance according to claim 15, further comprising a facility for determining a ratio of mass flows in said high-pressure tube section and in said low-pressure tube section.

21. The refrigeration appliance according to claim 20, further comprising a facility for determining a ratio of the mass flows to said first evaporator assembly and to said second evaporator assembly.

22. The refrigeration appliance according to claim 15, further comprising a third evaporator between said parallel-connected first and second evaporators and said low-pressure tube.

23. The refrigeration appliance according to claim 22, which comprises a further suction tube heat exchanger, in which a refrigerant tube section at an outlet of said first evaporator and a further tube section of said low-pressure tube are heat-conductively coupled, or said third evaporator having a temperature sensor, which replaces a temperature sensor at the inlet of said low-pressure tube section.

24. A method of determining a ratio of mass flows in a refrigeration appliance with a refrigerant circuit having a compressor, a first evaporator assembly with at least one first evaporator and with a high-pressure tube connected upstream of the first evaporator assembly, a second evaporator assembly connected in parallel with the first evaporator assembly with at least one second evaporator, a low-pressure tube connected downstream of the first evaporator assembly and the second evaporator assembly, and a suction tube heat exchanger, in which a high-pressure tube section of the high-pressure tube and a low-pressure tube section of the low-pressure tube are heat-conductively coupled, and wherein the suction tube heat exchanger has a group of positions at the inlet and at the outlet of the low-pressure tube section, and at the inlet and at the outlet of the high-pressure tube section; the method comprising the following steps: (a) determining respective temperatures at three positions of the group of positions; b) determining a ratio of a mass flow through the high-pressure tube section to a mass flow through the low-pressure tube section from the temperatures determined in step a).

25. The method according to claim 24, wherein step a) further comprises: a′) determining the temperatures at all positions of the group of positions.

26. The method according to claim 24, wherein the step of determining the ratio of the mass flow through the high-pressure tube section to the mass flow through the low-pressure tube section comprises determining specific thermal capacities of a refrigerant, under an assumption that a refrigerant in the high-pressure tube section is a liquid refrigerant and a refrigerant in the low-pressure tube section is a gaseous refrigerant.

27. The method according to claim 24, which comprises: c) determining the mass flow through the low-pressure tube section from a delivery of the compressor.

28. The method according to claim 24, which comprises: d) determining a mass flow through the second evaporator assembly from a ratio of the mass flow through the high-pressure tube section to the mass flow through the low-pressure tube section.

29. The method according to claim 24, which further comprises: controlling the refrigeration appliance based on the ratio of the mass flow through the high-pressure tube section to the mass flow through the low-pressure tube section.

Description

[0044] Further features and advantages of the invention are indicated by the following description of exemplary embodiments by reference to the attached figures.

[0045] These show as follows:

[0046] FIG. 1 a schematic representation of a refrigeration appliance according to the invention;

[0047] FIG. 2 a schematic representation of the refrigerant circuit of a refrigeration appliance according to the invention with parallel evaporator lines;

[0048] FIG. 3 a schematic representation of an internal heat exchanger of the refrigerant circuit of a refrigeration appliance according to the invention;

[0049] FIG. 4 a schematic representation of the refrigerant circuit of a refrigeration appliance according to the invention with parallel evaporator lines and an evaporator following in series;

[0050] FIG. 5 a schematic representation of the refrigerant circuit of a refrigeration appliance according to the invention with parallel evaporator lines and a further evaporator following in series;

[0051] FIG. 6 a flow diagram of an embodiment of the method according to the invention; and

[0052] FIG. 7 a flow diagram of a further embodiment of the method according to the invention.

[0053] In the various embodiments functionally identical elements are provided with the same reference numerals, and similar elements with dashed reference numerals.

[0054] FIG. 1 shows a refrigerator representative of a refrigeration appliance 10 according to the invention with a refrigeration compartment door 12 to a refrigeration compartment 15, a flex compartment door 13 to a flex compartment 16 with an extended temperature range and a door 14 to a simple flex compartment 17. The refrigerator serves, for example, for the storage of food items and comprises as storage chambers a refrigeration compartment, a flex compartment with an extended temperature range and a simple flex compartment. These storage chambers are in each case cooled by an associated evaporator. The refrigeration appliance 10 also has a display and control unit 18, which controls the refrigeration appliance. The display and control unit 18 has a facility 19 for determining a ratio of mass flows. The refrigeration appliance 10 has a refrigerant circuit, which can be designed in various embodiments of the invention.

[0055] FIG. 2 shows a refrigerant circuit 20 of a refrigeration appliance according to the invention. The refrigerant circuit 20 has a compressor 22, a condenser 24, a first evaporator assembly 26 with a first evaporator 28 and a further evaporator 30 of the first evaporator assembly 26, and a second evaporator assembly 32 with a second evaporator 34 parallel to the first evaporator assembly 26.

[0056] The compressor is a speed-controlled compressor with variable speed. The compressor is designed to work in continuous operation.

[0057] In the first evaporator assembly 26 the first evaporator 28 and the further evaporator 30 of the first evaporator assembly 26 are disposed parallel to each other. In the direction of flow before the first evaporator 28 an expansion valve 36 is disposed, which controls the refrigerant inflow into the evaporator 28. In the direction of flow after the first evaporator 28 an expansion valve 38 is disposed, which controls the refrigerant outflow from the first evaporator 28.

[0058] Before and after the further evaporator 30 of the first evaporator assembly 26 expansion valves 40 and 42 are also disposed. In the first evaporator assembly further evaporators of the first evaporator assembly could be disposed parallel to the first evaporator, to provide further storage compartments with their own evaporator.

[0059] The evaporators 28, 30 of the first evaporator assembly 26 are associated with storage compartments, which can be cooled to temperatures below the ambient temperature. Thus the first evaporator 28 is associated with a refrigeration compartment, and the further evaporator 30 of the first evaporator assembly 26 is associated with a simple flex compartment with variable temperature, so that this compartment can be operated optionally as a further refrigeration compartment, chiller compartment or freezer compartment. The variable temperatures of the evaporators of the first evaporator assembly 26 are made possible by the expansion valves before and after the evaporators, which allow an evaporating pressure of the refrigerant in the evaporator to be adjusted such that the desired temperatures are reached independently of temperatures in other evaporators.

[0060] In the second evaporator assembly 32, in the embodiment shown in FIG. 2, there is only a single evaporator present, namely the second evaporator 34. In the direction of flow before the second evaporator 34 an expansion valve 44 is disposed, which controls the refrigerant inflow into the evaporator 34. In the direction of flow after the second evaporator 34 an expansion valve 46 is disposed, which controls the refrigerant outflow from the second evaporator 34.

[0061] The second evaporator 34 of the second evaporator assembly 32 is associated with a flex compartment with an extended temperature range, which can be operated in a wide temperature range both below and above the ambient temperature. The variable temperatures of the second evaporator 34 are made possible by the expansion valves before and after the second evaporator 34, which allow an evaporating pressure of the refrigerant to be adjusted such that the desired temperatures are reached independently of temperatures in other evaporators.

[0062] The arrangement shown in FIG. 2 with the evaporators 28, 30 and 32 corresponds to an embodiment of the refrigeration appliance 10 from FIG. 1, wherein the evaporators 28, 30 and 32 are associated with the storage compartments 15, 17 and 16.

[0063] The refrigerant circuit 20 has a circulation system with pipelines that connect together the described elements of the refrigerant circuit 20. The refrigerant circuit 20 has a high-pressure range between the outlet of the compressor 22 and the expansion valves 36, 40 and 44. The refrigerant circuit 20 has a low-pressure range between the valves 36, 40 and 46 and the inlet of the compressor 22.

[0064] With the second evaporator 34, the association of the pipe region between the expansion valve 44 before the second evaporator 34 and the expansion valve 46 after the second evaporator 34 with the high-pressure range or the low-pressure range is dependent upon the respective operating condition of the second evaporator 34 and the prevailing pressure therein. If the second evaporator 34 is operated at a temperature higher than the ambient temperature, then in this operating condition it has the function of a condenser and can be operated at high pressure.

[0065] The refrigerant circuit 20 has a high-pressure tube 48, which is connected upstream of the evaporators of the first evaporator assembly. The high-pressure tube 48 terminates at the flow restrictors of the evaporators of the first evaporator assembly, and so here at the expansion valves 36 and 40.

[0066] The refrigerant circuit 20 has a low-pressure tube 49, which is connected downstream of the first evaporator assembly 26 and the second evaporator assembly 32. The low-pressure tube 49 runs between the expansion valves 38, and 46 and the inlet to the compressor 22.

[0067] The refrigerant circuit 20 also has a suction tube heat exchanger 50, in which a high-pressure tube section 52 of the high-pressure tube 48 and a low-pressure tube section 54 of the low-pressure tube 49 are coupled in a heat-conducting manner.

[0068] The suction tube heat exchanger 50 has four preferred positions for temperature sensors, namely position 56 at the inlet of the high-pressure tube section 52, position 58 at the outlet of the high-pressure tube section 52, position 60 at the inlet of the low-pressure tube section 54 and position 62 at the outlet of the low-pressure tube section 54. The reason these positions for temperature sensors are preferred, is because when the refrigeration appliance is in operation a maximum temperature difference of the refrigerant of the high-pressure tube section 52 occurs and between positions 60 and 62 a maximum temperature difference of the refrigerant of the low-pressure tube section 54 occurs in the heat exchanger 50 due to the heat exchange between positions 56 and 58.

[0069] In one embodiment of the invention, at each of the four positions 56, 58, 60 and 62 the refrigerant circuit 20 has a temperature sensor. This embodiment has the advantage that the temperature differences in the high-pressure tube section 52 and in the low-pressure tube section 54 can be determined by simple temperature measurements with the temperature sensors.

[0070] From these, the display and control unit 16 of the refrigeration appliance 10 can determine a ratio between the mass flows in the high-pressure section and the low-pressure section.

[0071] In the arrangement shown in FIG. 2 with a single evaporator 34 in the second evaporator assembly 32 the ratio can thus be calculated between the mass flow through the evaporator 34 and the total mass flow.

[0072] In another embodiment of the invention, at three positions from the group of positions 56, 58, 60 and 62, the refrigerant circuit 20 has a temperature sensor. This embodiment has the advantage that there is less need for a temperature sensor. The temperature at the position of the missing temperature sensor can be determined by considerations from thermodynamics. All four temperatures are thereby then known, and the ratios of mass flows can be determined as in the above-mentioned embodiment.

[0073] In the refrigerant circuit 20 represented in FIG. 2, in accordance with the invention the evaporators of the first evaporator assembly 26, here therefore the evaporators 28 and 30, are exclusively intended for compartments that are cooled, so that the evaporators 28 and 30 are also operated as evaporators. The second evaporator assembly 32 with the single evaporator 34, in accordance with the invention, is intended for flex compartments with an extended temperature range, like the flex compartment 16 from FIG. 1. Since the evaporators of the second evaporator assembly 32 can be operated not only as evaporators, but also as condensers, the refrigerant of the second evaporator assembly 32 is fed via a branch 64 of the high-pressure tube 48, which is not involved in a suction tube heat exchange. Therefore, the second evaporator assembly can receive refrigerant which has approximately the same temperature as the condenser 24.

[0074] Apart from that, the improvement in the energy efficiency made possible by the suction tube heat exchange is used in such a way that in addition the refrigerant, which is fed to the first evaporator assembly, is cooled by the suction tube heat exchange.

[0075] In the refrigerant circuit 20 the condenser 24 has a fan 66. The fan 66 has the task of preventing excessive condenser temperatures and is able to cool the condenser 24 if in the second evaporator assembly no evaporator in a heating mode is being operated to reach a temperature above the ambient temperature in the evaporator or in its flex compartment with extended temperature range.

[0076] The evaporators 28, 30 and 34 have fans 68, 70 and 72. These fans can be used both for improving the heat transfer between evaporator and the respective compartment or also for humidity control of the respective compartment.

[0077] In the second evaporator assembly further evaporators of the second evaporator assembly could be disposed parallel to the second evaporator, to provide further storage compartments, particularly flex compartments with an extended temperature range, with their own evaporator. The evaporators of these compartments are preferably disposed parallel to the second evaporator 34 and also with an expansion valve disposed before and an expansion valve after each evaporator, respectively.

[0078] FIG. 3 shows schematically the suction tube heat exchanger 50, also referred to as internal heat exchanger or suction tube heat transfer system, from FIG. 3 with the high-pressure tube section 52 of the high-pressure tube 48 and the low-pressure tube section 54 of the low-pressure tube 49. The direction of flow of the refrigerant is shown by the arrows 74 and 76. The suction tube heat exchanger 50 has four preferred positions for temperature sensors, namely externally on the tube of the respective tube section position 56 at the inlet of the high-pressure tube section 52, position 58 at the outlet of the high-pressure tube section 52, position 60 at the inlet of the low-pressure tube section 54, and position 62 at the outlet of the low-pressure tube section 54.

[0079] Alternatively, it is possible to provide the positions for temperature sensors internally on the tube of the respective tube section.

[0080] A coordinate line 77 is for example indicated, with end points 78 and 79 and a section, along which in the suction tube heat exchanger 50 a heat exchange occurs. By means of the coordinate line 77 a temperature profile within the suction tube heat exchanger 50 can be determined using thermodynamics.

[0081] FIG. 4 shows schematically a refrigerant circuit 80 of a refrigeration appliance of an embodiment of the invention in an embodiment with a different arrangement of evaporators compared to the embodiment in FIG. 2. Therefore the essential differences from FIG. 2 are described. The first evaporator assembly 26′ has only the first evaporator 28 and the second evaporator assembly 32 has only the second evaporator 34. Before and after the evaporators 28, 34 the expansion valves already described are again disposed. A suction tube heat exchanger 50′ is also disposed at the same point with respect to the first evaporator assembly.

[0082] In this embodiment the refrigerant circuit has a third evaporator 82 between the first and second evaporator assemblies 26′, 32 disposed in parallel and the low-pressure tube 49′. In the direction of flow of the refrigerant the third evaporator 82 follows the evaporators 28, 34 of the parallel evaporator assemblies 26′, 32 in series.

[0083] The low-pressure tube 49′ runs from the third evaporator 82 to the compressor 22. A low-pressure tube section 54′ of the low-pressure tube 49′ is located in the suction tube heat exchanger 50′.

[0084] The refrigerant circuit 80 has an optional further internal heat transfer system 84, in which a further tube section 81 of the low-pressure tube 49′ and a refrigerant tube section 83 at the outlet of the first evaporator 28 are coupled in a heat-conducting manner. However, the further internal heat transfer system 84 does not provide any information regarding a mass flow distribution that at the outlet of the evaporator 28 the refrigerant is two-phase. The suction gas then sees in the further internal heat transfer system 84, as it were, an isothermal heat source.

[0085] The refrigerant circuit 80 is suitable for a refrigeration appliance 10 according to FIG. 1. In this embodiment of the invention the evaporator 28 is again associated with a refrigeration compartment 15, the evaporator 34 with a flex compartment with extended temperature range 16, and the evaporator 82 with a simple flex compartment, which can be operated, for example, as a chiller compartment or as a freezer compartment. The evaporator 82 has a blower 85.

[0086] The refrigerant circuit 80 advantageously uses the low suction pressure of the compressor 22 for an evaporator 82 disposed in series, which is associated with a particularly cold compartment.

[0087] The evaporator 82 is associated with a cold compartment, preferably a freezer compartment, and has a temperature sensor 86.

[0088] Together with the temperature sensor 86 the refrigerant circuit 80 has the following advantage. At the location of the temperature sensor 86 for the entire refrigerant mass flow the temperature and pressure are known, and from these, using a temperature sensor at the end of the low-pressure tube section, position 62′, the suction gas density there can be determined. In turn, by means of the compressor speed, from the delivery of the compressor, the absolute total mass flow can thereby be determined.

[0089] This, in turn, allows a determination of the absolute mass flow through the evaporator 34.

[0090] An embodiment of the invention without the further internal heat exchanger 84 furthermore allows, instead of a temperature sensor at the inlet of the low-pressure tube section 54′ the temperature sensor 86 at position 60′ to be used to determine the temperature at the inlet to the low-pressure tube section 54′.

[0091] FIG. 5 shows a refrigerant circuit in a further embodiment, which builds upon the embodiment shown in FIG. 4. Now, downstream of the third evaporator 82′ in a serial arrangement, a fourth evaporator 88 is added. The third evaporator 82′ has a temperature sensor 86′.

[0092] The third evaporator 82′ has a blower 85′ and the fourth evaporator 88 has a blower 90.

[0093] In this arrangement the evaporator 86′ is operated as a freezer compartment evaporator for the supply of a freezer compartment and the additional evaporator 88 is operated as an evaporator for a chiller compartment or a refrigeration compartment. Control of the refrigeration appliance with this refrigerant circuit takes place in such a way that the refrigerant fed to the evaporator 86′ is substantially evaporated in the evaporator 86′ and the next evaporator 88 is cooled with cold gaseous refrigerant.

[0094] In turn, the temperature sensor 86′ is in the coldest compartment, and therefore the temperature and evaporating pressure at its position can be determined based on the prevailing temperature there and with this information with a temperature sensor at the end of the low-pressure tube section, position 62′, the suction gas density there can be determined. In turn, by means of the compressor speed, from the delivery of the compressor, the absolute total mass flow can thereby be determined.

[0095] FIG. 6 shows a flow diagram 100 of an embodiment of the method according to the invention for determining a ratio of mass flows in a refrigeration appliance. The refrigeration appliance, for example the refrigeration appliance ten from FIG. 1, has a refrigerant circuit, for example the refrigerant circuit 20 from FIG. 2 or the refrigerant circuit 80 from FIG. 4, the refrigerant circuit 20, 80 has a compressor 22, a first evaporator assembly 26, 26′ with at least one first evaporator 28 and with a high-pressure tube 48 connected upstream of the first evaporator assembly 26, 26′, a second evaporator assembly 32 with at least one second evaporator 34 connected in parallel with the first evaporator assembly 26, 26′, a low-pressure tube 49, 49′ connected downstream of the first evaporator assembly 26, 26′ and the second evaporator assembly 32, and a suction tube heat exchanger 50, 50′, in which there is a high-pressure tube section 52, 52′ of the high-pressure tube 48 and a low-pressure tube section 54, 54′ of the low-pressure tube 49, 49′ coupled in a heat-conducting manner. The suction tube heat exchanger has a group of positions 60, 60′; 62, 62′; 56, 56′; 58, 58′ at the inlet and at the outlet of the low-pressure tube section, and at the inlet and at the outlet of the high-pressure tube section.

[0096] The method has the method steps: [0097] a) determination 102 of temperatures at three positions from the group of positions; [0098] b) determination 104 of a ratio of a mass flow flowing through the high-pressure tube section to a mass flow flowing through the low-pressure tube section using the temperatures determined.

[0099] One embodiment of the method, instead of the method step a), contains the method step [0100] a′) determination 102 of temperatures at all positions from the group of positions.

[0101] The determination of a temperature at one of the positions at the suction tube heat exchanger normally takes place using a temperature sensor at the position at the suction tube heat exchanger. Alternatively, however, the determination of the temperature can also take place with a temperature sensor at an adjacent position on the suction tube in the refrigerant circuit outside the suction tube heat exchanger, if no heat transfer takes place from or to the suction tube between the two positions. Then it can reasonably be concluded that the prevailing temperature at both positions is the same.

[0102] FIG. 7 shows a flow diagram 110 of a further embodiment with embodiments of the method according to the invention. The additional method steps compared to FIG. 6 are in each case optional in their own right and can be combined. The method again starts with method step [0103] a) determination 102 of temperatures at three positions from the group of positions; [0104] then follows method step [0105] c) determination 112 of a mass flow through the low-pressure tube section from [0106] a delivery by the compressor.

[0107] In a further method step [0108] d) determination 114 of a mass flow through the second evaporator assembly takes place from the ratio of the mass flow through the high-pressure tube section to the mass flow through the low-pressure tube section.

[0109] If the refrigerant circuit 20, when the refrigeration appliance 10 is in operation, is in a stationary state, and so the temperatures in the evaporators 28, 30, 34 and in the suction tube heat exchanger 50 are substantially constant, the entire mass flow of the refrigerant delivered by the compressor 22 flows through the low-pressure tube section 52 of the suction tube heat exchanger 50. The entire mass flow can then be determined from the delivery by the compressor 22.

[0110] In a further method step [0111] e) control 116 of the refrigeration appliance 10 takes place based on the temperatures determined.

[0112] Alternatively to method step e), [0113] e′) control 118 of the refrigeration appliance 10 based on the ratio of the mass flow through the high-pressure tube section to the mass flow through the low-pressure tube section takes place. Here the ratio of the mass flow through the high-pressure section to the mass flow through low-pressure section is determined by means of the temperatures from method step a).

LIST OF REFERENCE CHARACTERS

[0114] 10 refrigeration appliance [0115] 12 refrigeration compartment door [0116] 13 flex compartment door [0117] 14 door [0118] 15 refrigeration compartment [0119] 16 flex compartment [0120] 17 simple flex compartment [0121] 18 display and control unit [0122] 19 facility for determining a ratio of mass flows [0123] 20 refrigerant circuit [0124] 22 compressor [0125] 24 condenser [0126] 26, 26′ first evaporator assembly [0127] 28 first evaporator [0128] 30 further evaporator [0129] 32 second evaporator assembly [0130] 34 second evaporator [0131] 36, 38, 40, 42, 44, 46 expansion valves [0132] 48 high-pressure tube [0133] 49, 49′ low-pressure tube [0134] 50, 50′ suction tube heat exchanger [0135] 52, 52′ high-pressure tube section [0136] 54, 54′ low-pressure tube section [0137] 56, 56′, 58, 58′, 60, 60′, 62, 62′ positions at the suction tube heat exchanger [0138] 64 branch of the high-pressure tube [0139] 66, 68, 70, 72 fans [0140] 74, 76 arrows [0141] 77 coordinate line [0142] 78, 79 end points [0143] 80 refrigerant circuit [0144] 81 further tube section [0145] 82, 82′ third evaporator [0146] 83 refrigerant tube section [0147] 84 further internal heat transfer system [0148] 85, 85′ fan [0149] 86, 86′ temperature sensor [0150] 90 refrigerant circuit [0151] 92 fourth evaporator [0152] 94 fan [0153] 100 flow diagram [0154] 102 determination of temperatures [0155] 104 determination of a ratio of mass flows [0156] 110 flow diagram [0157] 112 determination of a mass flow [0158] 114 determination of a mass flow [0159] 116, 118 control of the refrigeration appliance