Water source heat pump dual functioning condensing coil

Abstract

A heat pump system includes a compressor, a usage side heat exchanger, a heat source side heat exchanger, an expansion mechanism, a main refrigerant flow control device switchable between cooling and heating modes, a gas reheat heat exchanger, a fan, and a secondary refrigerant flow control device switchable between first, second, and third modes. Refrigerant flows from the compressor discharge line to the main refrigerant flow control device in the first mode. Refrigerant flows from discharge line to gas reheat heat exchanger and then main refrigerant flow control device in the second mode. Refrigerant flows both from discharge line to gas reheat heat exchanger and then main refrigerant flow control device, and from discharge line to main refrigerant flow control device without flowing through the gas reheat heat exchanger in the third mode. Refrigerant may flow to the usage side and hot gas reheat heat exchanger in the heating mode.

Claims

1. A heat pump system comprising: a compressor, the compressor delivering compressed refrigerant to a discharge line and receiving a refrigerant from a suction line; a usage side heat exchanger; a heat source side heat exchanger arranged to exchange heat between a heat transfer medium and refrigerant flowing therethrough; an expansion valve; a main refrigerant flow control valve switchable between a cooling mode in which refrigerant is configured to flow from the discharge line through part of a refrigerant circuit, to the heat source side heat exchanger, to the expansion valve and then to the usage side heat exchanger, and a heating mode in which refrigerant is configured to flow from the discharge line through part of the refrigerant circuit to the usage side heat exchanger, to the expansion valve and then to the heat source side heat exchanger; a hot gas reheat heat exchanger connected in the refrigerant circuit; a fan disposed to direct an airflow across the usage side heat exchanger and the hot gas reheat heat exchanger into a target space; a receiver connected in the refrigerant circuit between the heat source side heat exchanger and the expansion valve in a flow direction of the refrigerant, the receiver being configured such that refrigerant flows through the receiver to an inlet side of the expansion valve when the main refrigerant flow control valve is in the cooling mode, and configured such that refrigerant does not flow to the receiver when the main refrigerant control valve is in the heating mode; and a secondary refrigerant flow control valve switchable between a first mode in which refrigerant is configured to flow from the discharge line to the main refrigerant flow control valve, a second mode in which refrigerant is configured to flow from the discharge line to the hot gas reheat heat exchanger and then flows to the main refrigerant flow control valve, and a third mode in which refrigerant is configured to flow both from the discharge line to the hot gas reheat heat exchanger and then flows to the main refrigerant flow control valve, and from the discharge line to the main refrigerant flow control valve without flowing through the hot gas reheat heat exchanger, the refrigerant circuit and the main and secondary refrigerant flow control valves being configured such that refrigerant flows to the usage side heat exchanger and the hot gas reheat heat exchanger when the main refrigerant flow control valve is in the heating mode, and the refrigerant circuit and the main and secondary refrigerant flow control valves are configured such that the refrigerant flows to the hot gas reheat heat exchanger before flowing to the heat source side heat exchanger when the main refrigerant flow control valve is in the cooling mode.

2. The heat pump according to claim 1, wherein the refrigerant circuit and the main and secondary refrigerant flow control valves are configured such that refrigerant flows to the usage side heat exchanger and the hot gas reheat heat exchanger when the main refrigerant flow control valve is in the cooling mode.

3. The heat pump according to claim 1, wherein the refrigerant circuit and the main and secondary refrigerant flow control valves are configured such that refrigerant flows to the usage side heat exchanger and the hot gas reheat heat exchanger when the secondary refrigerant flow control valve is in at least one of the second and third modes.

4. The heat pump according to claim 3, wherein the refrigerant circuit and the main and secondary refrigerant flow control valves are configured such that refrigerant flows to the usage side heat exchanger and the hot gas reheat heat exchanger when the secondary refrigerant flow control valve is in both of the second and third modes, one of the second and third modes including series flow through the hot gas reheat heat exchanger and the usage side heat exchanger, and the other of the second and third modes including parallel flow through to the usage side heat exchanger and the hot gas reheat heat exchanger.

5. The heat pump according to claim 1, wherein the heat transfer medium of the heat source side heat exchanger is a liquid.

6. The heat pump according to claim 5, wherein the heat transfer medium of the heat source side heat exchanger is water.

7. The heat pump according to claim 5, wherein the heat source side heat exchanger is a brazed plate heat exchanger.

8. The heat pump according to claim 1, wherein the secondary refrigerant flow control valve is a modulating three way valve.

9. The heat pump according to claim 1, wherein the compressor includes at least one of two stages and two compressors.

10. The heat pump according to claim 9, wherein the compressor includes at least two compressors with each compressor including at least two stages.

11. The heat pump according to claim 10, wherein the compressor is an uneven tandem compressor configured to provide at least 8 different output stage levels.

12. The heat pump according to claim 9, wherein the compressor output is controlled by an electronic controller based on saturated suction temperature on a suction side of the compressor.

13. The heat pump according to claim 12, wherein the refrigerant circuit includes at least one of a suction pressure sensor and a suction temperature sensor utilized to determine the saturated suction temperature.

14. The heat pump according to claim 13, wherein the refrigerant circuit includes a suction pressure sensor and a suction temperature sensor disposed on the suction side of the compressor, which are utilized to determine the saturated suction temperature.

15. The heat pump according to claim 1, wherein the refrigerant flows to the receiver when the main refrigerant flow control valve is in the cooling mode.

16. The heat pump according to claim 1, wherein the receiver is an inclined tube receiver configured to promote phase separation and to ensure liquid seat is maintained at the expansion valve.

17. The heat pump according to claim 1, wherein the main refrigerant flow control valve is a four-way valve.

18. The heat pump according to claim 1, wherein in the heating mode the heat pump is configured to heat 0 degree air to 65 degrees or more.

19. The heat pump according to any of claim 18, wherein the heat pump is configured to heat 0 degree air to 65 degrees or more when the main refrigerant flow control valve is in a heating mode and the secondary refrigerant flow control valve is in the second position.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Referring now to the attached drawings which form a part of this original disclosure:

(2) FIG. 1 illustrates a conventional water source refrigerant heat pump schematic, in a cooling mode;

(3) FIG. 2 illustrates the heat pump schematic of FIG. 1, in a heating mode;

(4) FIG. 3 illustrates the heat pump schematic of FIGS. 1-2, but in a hot gas reheat mode;

(5) FIG. 4 illustrates the heat pump schematic of FIG. 3, in a hot gas reheat mode and with system parts identified for convenience;

(6) FIG. 5 illustrates an embodiment of a water source refrigerant heat pump schematic, which is a modification of the schematic of FIGS. 1-4, in a full cooling mode and with system parts identified for convenience like FIG. 4, including parts not present in FIG. 4;

(7) FIG. 6 is a schematic view of the heat pump illustrated in FIG. 5, in a modulating hot gas reheat mode;

(8) FIG. 7 is a schematic view of the heat pump illustrated in FIGS. 5-6, in a full hot gas reheat mode;

(9) FIG. 8 is a schematic view of the heat pump illustrated in FIGS. 5-7, in a dual condensing full heating mode;

(10) FIG. 9 is a schematic view of the heat pump illustrated in FIGS. 5-8, in a dual condensing modulating heating mode;

(11) FIG. 10 is a schematic view of the heat pump illustrated in FIGS. 5-9, in a dual condensing Dx coil only heating mode; and

(12) FIGS. 11-21 are schematic illustrations of the heat pump shown in FIGS. 5-10.

DETAILED DESCRIPTION OF EMBODIMENT(S)

(13) Selected embodiments will now be explained with reference to the drawings. It will be apparent to those skilled in the art from this disclosure that the following descriptions of the embodiments are provided for illustration only and not for the purpose of limiting the invention as defined by the appended claims and their equivalents.

(14) Referring initially to FIGS. 1-4, a conventional water source heat pump (1) is illustrated. FIG. 1 shows the cooling mode, FIG. 2 shows the heating mode and FIG. 3 shows the hot gas reheat mode. FIG. 4 also shows the hot gas reheat mode just like FIG. 3 but further includes labels for the parts of system. These parts are the same in FIGS. 1-4, and thus, may not be included in all the Figures for the sake of convenience.

(15) In the cooling mode of FIG. 1, compressed high pressure refrigerant flow (HPRF) exits the compressor and flows through the hot gas reheat valve (10) to the reversing valve (12), through the water coil (16) to the thermostatic expansion valve (TEV). The TEV then reduces the pressure of the refrigerant. The resulting low pressure refrigerant flow (LPRF) then flows through a distributor (D) and then through the DX coil or the Evaporator (14), back through the reversing valve (12) and back to the suction side of the compressor (C). Note the refrigerant does not flow through the hot gas reheat coil (18) (note the “x” on the flow path at several locations).

(16) In the heating mode of FIG. 2, compressed high pressure refrigerant flow (HPRF) exits the compressor and flows through the hot gas reheat valve (10) to the reversing valve (12), through the DX coil or the Evaporator (14), and through the distributor (D) to the thermostatic expansion valve (TEV). The TEV then reduces the pressure of the refrigerant. The resulting low pressure refrigerant flow (LPRF) then flows through the water coil (16), back through the reversing valve (12) and back to the suction side of the compressor (C). Note the refrigerant does not flow through the hot gas reheat coil (18) (note the “x” on the flow path at several locations).

(17) In the hot gas reheat mode shown in FIGS. 3-4, compressed high pressure refrigerant flow (HPRF) exits the compressor and flows through the hot gas reheat valve (10) (the flow at the hot gas reheat valve (10) is switched as compared to the cooling and heating modes) to the hot gas reheat coil (18), through the hot gas reheat coil (18), through the hot gas check valve, through the reversing valve (12), and through the water coil (16) to the TEV. The TEV then reduces the pressure of the refrigerant. The resulting low pressure refrigerant flow (LPRF) then flows through the distributor (D), the DX coil or evaporator (14), back through the reversing valve (12) and back to the suction side of the compressor (C).

(18) In FIGS. 1-4, the gas reheat valve (10) is a conventional three-way valve that sends refrigerant out of only one of the outlets as shown in the Figures.

(19) Referring now to FIGS. 5-10, an example of a heat pump (1′) in accordance with the present invention will not be explained. The piping layout and the manner/order in which components are connected and operated result in a heat pump (1) in accordance with the present invention, even if certain parts themselves are conventional. In the heat pump (1′) illustrated in these FIGS. 5-10 parts that are the same as those in FIGS. 1-4 will not be discussed. However, parts that are different from those in FIGS. 1-4 will be discussed.

(20) First a modified compressor (C′) is included. The compressor (C′) includes two compressors A and B, with one of A and B being smaller than the other of A and B. In addition, each compressor A and B includes two stages. All of the stages can have different capacities. Therefore, even though the compressor (C′) does not require a relatively complicated inverter control, the compressor (C′) has multiple output levels, preferably at least 8. The compressor (C′) is available from Emmerson or Copeland, and by itself is conventional. Because the compressor (C′) is conventional, the compressor (C′) will not be discussed in great detail herein except how the compressor (C′) is connected and operated in the heat pump system (1′) of FIGS. 5-10.

(21) Second, a modulating 3 way valve (10′) (hot gas reheat valve) is disposed at an outlet (O) of the compressor (C′). The modulating 3 way valve (10′) (hot gas reheat valve) has a single inlet from the compressor (C′). However, the modulating 3 way valve (10′) (hot gas reheat valve) has two outlets, one leading to a hot gas T valve and another leading to the hot gas reheat coil (18). The modulating 3 way valve (10′) (hot gas reheat valve) by itself is conventional, and thus, will not be discussed in great detail herein except how the modulating 3 way valve (10′) (hot gas reheat valve) is connected and operated in the heat pump system (1′) of FIGS. 5-10. A conventional high pressure switch and a conventional pressure transducer are disposed between the compressor outlet (O) and the modulating 3 way valve (10′) (hot gas reheat valve). The modulating 3 way valve (10′) (hot gas reheat valve) can be controlled by a PID controller available from the manufacturer of the modulating 3 way valve (10′) (hot gas reheat valve) in a conventional manner. In this embodiment, the modulating 3 way valve (10′) (hot gas reheat valve) can be set in a first mode or position (FIGS. 5 and 10), a second position or mode (FIGS. 7 and 8) and a third position or mode (FIGS. 6 and 9) with feedback from a supply air sensor to control discharge air temperature by modulating refrigerant to the hot gas reheat coil (18).

(22) Third, in this embodiment, an electronic expansion valve EEV is provided instead of a TEV in FIGS. 1-4. The EEV is conventional and can be controlled in a conventional manner. In addition, the EEV can be controlled in conjunction with control of the compressor (C′) and the modulating 3 way valve (10′) (hot gas reheat valve).

(23) Fourth, the water coil in this embodiment is a brazed plate heat exchanger (16′) (BPHE) unlike the coax water coil (16) in FIGS. 1-4. The brazed plate heat exchanger (BPHE) by itself is conventional, and thus, will not be discussed in great detail herein except how the brazed plate heat exchanger (BPHE) is connected and operated in the heat pump system (1′) of FIGS. 5-10.

(24) Fifth, a receiver (R) is disposed between the brazed plate heat exchanger (BPHE) and the EEV. The receiver (R) only stores liquid refrigerant when the reversing valve (12) is in a so-called cooling mode (FIGS. 5-7) not when the reversing valve (12) is in a so-called heating mode (FIGS. 8-10). A check valve arrangement facilitates the functionality of the receiver (R).

(25) Sixth, a suction pressure transducer and a suction temperature sensor are disposed between an inlet of the compressor (C′) and the reversing valve (12). The suction pressure transducer and a suction temperature sensor are used to determine saturated suction temperature using an algorithm embedded in the controller. The compressor (C′) staging is then controlled (set to the appropriate one of the at least 8 stages) to maintain facilitating leaving air state point of 55° F. dew point temperature. More specifically, minimum and maximum parameters of saturated suction temperature for each stage are determined in order to maintain a 55° F. dew point temperature. In a first or lowest stage the minimum allowable parameter goes down to 100 psi (31.5° F. saturate vapor temperature), which assists in protecting the system against potential coil freeze.

(26) Seventh, and finally, there are or can be additional conventional T valves, check valves, bleed valves etc. that may be necessary to create the heat pump system (1′) shown in FIGS. 5-10. The function/operating of these parts are self-evident to those of ordinary skill in the art from FIGS. 5-10 and the flow shown therein, and thus, will not be discussed in further detail herein.

(27) Referring initially to FIGS. 5-7, different operations of the heat pump system (1′) when the reversing valve (12) is in a so-called cooling mode will now be explained. In these modes, the reversing valve (12) is in a same position in which the Dx coiling (14) performs cooling, and thus, the position of the reversing valve (12) can be considered a cooling position or mode. However, even if the reversing valve (12) is in the cooling mode, the compressor (C′) and the modulating 3 way valve (10′) (hot gas reheat valve) can be controlled to provide different levels of cooling and dehumidification.

(28) In FIG. 5, a full cooling mode is illustrated. In the full cooling mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a first position or mode in which the hot gas reheat coil (18) is not performing any function because there is no flow therethrough. Rather, all refrigerant discharged from the compressor (C′) is sent to the brazed plate heat exchanger (BPHE) via the modulating three way valve (10′). In this mode, the compressor (C′) and/or the EEV can be controlled to provide the desired amount of cooling of air provided to the target space.

(29) In FIG. 6, a modulating hot gas reheat mode is illustrated. In the modulating hot gas reheat mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a third position or mode in which the hot gas reheat coil (18) receives some refrigerant and the brazed plate heat exchanger receives some refrigerant from the compressor (C′). The refrigerant that is received by the hot gas reheat coil (18) joins the refrigerant to be supplied to the brazed plate heat exchanger after flowing through the hot gas reheat coil (18). The modulating 3 way valve (10′) can modulate the amount of refrigerant supplied from both of the outlets thereof to modulate the amount of dehumidification (hot gas reheat). In addition, the temperature of air supplied to the target space can be finely adjusted in this mode. In this mode, the compressor (C′) and/or the EEV can also be controlled to provide the desired amount of cooling, which can also be used to finely adjust the temperature of air supplied to the target space.

(30) In FIG. 7, a full hot gas reheat mode is illustrated. In the full hot gas reheat mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a second position or mode in which the hot gas reheat coil (18) receives all refrigerant from the compressor (C′), and the brazed plate heat exchanger only receives refrigerant that has already passed through the hot gas reheat coil (18). In this mode, maximum dehumidification can be provided. However, more air warming may also be provided by the hot gas reheat coil (18). Thus, the compressor (C′) and/or the EEV can also be controlled to provide the desired amount of cooling, which can also be used to finely adjust the temperature of air supplied to the target space.

(31) It should be noted that in FIGS. 5-7, the receiver (R) receives and delivers refrigerant. Therefore, even if the compressor is operated at a lower capacity sufficient refrigerant for sufficient cooling can be provided to the EEV and then the Dx coil (14).

(32) Referring now to FIGS. 8-10, different operations of the heat pump system (1′) when the reversing valve (12) is in a so-called heating mode will now be explained. In these modes, the reversing valve (12) is in a same position in which the Dx coiling performs heating, and thus, the position of the reversing valve (12) can be considered a heating position or mode. However, even if the reversing valve (12) is in the heating mode, the compressor (C′) and the modulating 3 way valve (10′) (hot gas reheat valve) can be controlled to provide different levels of heating.

(33) In FIG. 8, a dual condensing full heating mode is illustrated. In the dual condensing full heating mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a second position or mode in which the hot gas reheat coil (18) receives all refrigerant from the compressor (C′), and then the Dx coil (14) receives the refrigerant that has already passed through the hot gas reheat coil (18). The refrigerant exiting the Dx coil (14), then flows to the EEV before being supplied to the brazed plate heat exchanger (BPHE). In this mode, maximum heating can be provided. Specifically, the compressor (C′) and/or the EEV can also be controlled to provide the desired amount of heating, which can also be used to adjust the temperature of air supplied to the target space. In this mode, 0 degree air can be heated to at least 65 degrees without the need for preheat. Preheat can be considered heating of the air by a device other than a heat exchanger containing refrigerant of the heat pump system (1′). For example an electric heater or gas furnace would be considered a preheater. The multi stage compressor (C′) assists with capability. In the past, it has not been possible to heat 0 degree air to 65 degrees or more without a preheater. Degrees referred to herein are Fahrenheit.

(34) In FIG. 9, a dual condensing modulating heating mode is illustrated. In the dual condensing modulating heating mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a third position or mode in which the hot gas reheat coil (18) receives some refrigerant and the Dx Coil (14) receives some refrigerant from the compressor (C′). The refrigerant that is received by the hot gas reheat coil (18) joins the refrigerant to be supplied to the Dx coil (14) after flowing through the hot gas reheat coil (18). The modulating 3 way valve (10′) can modulate the amount of refrigerant supplied from both of the outlets thereof to modulate the amount of hot gas reheat and heating by the Dx coil. In addition, the temperature of air supplied to the target space can be finely adjusted in this mode. In this mode, the compressor (C′) and/or the EEV can also be controlled to provide the desired amount of heating, which can also be used to finely adjust the temperature of air supplied to the target space.

(35) In FIG. 10, a dual condensing Dx coil only heating mode is illustrated. In the dual condensing Dx coil only heating mode, the modulating 3 way valve (10′) (hot gas reheat valve) is in a first position or mode in which the hot gas reheat coil (18) is not performing any function because there is no flow therethrough. Rather, all refrigerant discharged from the compressor (C′) is sent to the Dx coil (14) via the modulating three way valve (10′). In this mode, the compressor (C′) and/or the EEV can be controlled to provide the desired amount of heating of air provided to the target space.

(36) It should be noted that in FIGS. 8-10, the receiver (R) does not receive and deliver refrigerant.

(37) FIGS. 11-21 illustrate operations and/or connections of various parts including electrical, low voltage, data transfer, material exchange (water or liquid), refrigerant, physical connections such as brazing, and adhesive. Those of ordinary skill in the art are familiar with such schematics in order to connect/operate the heat pump (1′) in accordance with the present invention.

(38) As can be understood from the above the heat pump system (1′) in accordance with the present invention includes a compressor, a usage side heat exchanger, a heat source side heat exchanger, an expansion mechanism, a main refrigerant flow control device, a gas reheat heat exchanger, a fan (20), and a secondary refrigerant flow control device.

(39) The compressor delivers compressed refrigerant to a discharge line (DL) and receives a refrigerant from a suction line (SL). Examples of compressors include scroll, piston/cylinder, screw, and centrifugal compressor. The compressor of the illustrated embodiment is not limited to a particular type. However, as explained above, the compressor (C′) preferably has two different sized compressors, each having two stages. The usage side heat exchanger is an air/refrigerant heat exchanger, which is identified as a Dx coil or Evaporator (14) in the drawings. One example is a fin and tube heat exchanger. However, the usage side heat exchanger of the illustrated embodiment is not limited to a particular type. The heat source side heat exchanger in the illustrated embodiment is a liquid/refrigerant heat exchanger, more specifically a water/refrigerant heat exchanger, even more specifically a brazed plate heat exchanger arranged to exchange heat between a heat transfer medium (water) and refrigerant flowing therethrough. However, the heat source side heat exchanger of the illustrated embodiment is not limited to a particular type. The expansion mechanism in the illustrated embodiment is an EEV. However, other examples of expansion mechanisms include thermal expansion valves (TEV), and orifices. However, the expansion mechanism is not intended to be limited to any particular type. The main refrigerant flow control device is switchable between a cooling mode in which refrigerant flows from the discharge line (DL) through part of a refrigerant circuit, to the heat source side heat exchanger, to the expansion mechanism and then to the usage side heat exchanger, and a heating mode in which refrigerant flows from the discharge line (DL) through part of the refrigerant circuit to the usage side heat exchanger, to the expansion device and then to the heat source side heat exchanger. The main refrigerant flow control device of the illustrated embodiment is a 4-way reversing valve (12). Other examples include multiple one, two and/or three way valves. However, the main refrigerant flow control device is not intended to be limited to any particular type. The gas reheat heat exchanger connected in the refrigerant circuit is an air/refrigerant heat exchanger. One example is a fin and tube heat exchanger. However, the gas reheat heat exchanger of the illustrated embodiment is not limited to a particular type. The fan (20), identified in the drawings as “fan system” is disposed to direct an airflow across the usage side heat exchanger and the gas reheat heat exchanger into a target space. Examples of suitable fans include, an axial flow fan, a cross-flow fan and a centrifugal fan. However, the fan (20) of the illustrated embodiment is not limited to a particular type. The secondary refrigerant flow control device is switchable between a first mode in which refrigerant flows from the discharge line (DL) to the main refrigerant flow control device, a second mode in which refrigerant flows from the discharge line (DL) to the gas reheat heat exchanger and then flows to the main refrigerant flow control device, and a third mode in which refrigerant flows both from the discharge line (DL) to the gas reheat heat exchanger and then flows to the main refrigerant flow control device, and from the discharge line (DL) to the main refrigerant flow control device without flowing through the gas reheat heat exchanger. The secondary refrigerant flow control device in the illustrated embodiment is a modulating three-way valve (10′). However, the secondary refrigerant flow control device is not intended to be limited to any particular type. The refrigerant circuit and the main and secondary refrigerant flow control devices are arranged and configured such that refrigerant may flow to the usage side heat exchanger and the hot gas reheat heat exchanger when the main refrigerant flow control device is in the heating mode.

(40) The refrigerant circuit and the main and secondary refrigerant flow control devices are arranged and configured such that refrigerant may flow to the usage side heat exchanger and the hot gas reheat heat exchanger when the main refrigerant flow control device is in the cooling mode (FIGS. 6-7). The refrigerant circuit and the main and secondary refrigerant flow control devices are arranged and configured such that refrigerant may flow to the usage side heat exchanger and the hot gas reheat heat exchanger when the secondary refrigerant flow control device is in at least one of the second and third modes (FIGS. 6-7). More specifically, the refrigerant circuit and the main and secondary refrigerant flow control devices are arranged and configured such that refrigerant may flow to the usage side heat exchanger and the hot gas reheat heat exchanger when the secondary refrigerant flow control device is in both of the second and third modes (FIGS. 6-7), one of the second and third modes includes series flow through the hot gas reheat heat exchanger and the usage side heat exchanger (e.g., the second mode of FIG. 7), and the other of the second and third modes includes parallel flow through to the usage side heat exchanger and the hot gas reheat heat exchanger (e.g., the third mode of FIG. 6).

(41) As mentioned above, the heat transfer medium of the heat source side heat exchanger is a liquid, e.g., water. In addition, the heat source side heat exchanger is a brazed plate heat exchanger. Also, in the illustrated embodiment, the secondary refrigerant flow control device is a modulating three way valve. Also, the compressor includes at least one of two stages and two compressors, preferably at least two compressors with each compressor including at least two stages. Thus, in the illustrated embodiment, the compressor is an uneven tandem compressor that is operable to provide at least 8 different output stage levels. The compressor output is controlled based on saturated suction temperature on a suction side of the compressor. The refrigerant circuit includes at least one of a suction pressure sensor and a suction temperature sensor utilized to determine the saturated suction temperature. In the illustrated embodiment, the refrigerant circuit includes a suction pressure sensor and a suction temperature sensor disposed on the suction side of the compressor, which are utilized to determine the saturated suction temperature.

(42) As mentioned above, the refrigerant circuit further includes a receiver (R) disposed on an inlet side of the expansion mechanism when the main refrigerant flow control device is in the cooling mode. In the illustrated embodiment, refrigerant flows to the receiver (R) when the main refrigerant flow control device is in the cooling mode, and refrigerant does not flow to the receiver (R) when the main refrigerant flow control device is in the heating mode. In the illustrated embodiment, the receiver (R) is an inclined tube receiver (R), promotes phase separation, and ensures liquid seat is maintained at the EEV.

(43) As mentioned above, in the heating mode the heat pump (1) is configured to heat 0 degree air to 65 degrees or more. More specifically, the heat pump (1) is configured to heat 0 degree air to 65 degrees or more when the main refrigerant flow control device is in a heating mode and the secondary refrigerant flow control device is in the second position, which can be considered 100% hot gas.

(44) It will be apparent to those skilled in the art from this disclosure that an electronic controller can be used to control the compressor (C′), the EEV, and the modulating 3 way valve (10′) based on signals received from the various sensors. Of course, separate electronic controllers for separate parts can also be used, e.g., the PID controller for the modulating three way valve, which should preferably communicate with each other via wires or wired communications. If an electronic controller is used (e.g., for the main controller) the electronic controller is conventional, and thus, includes at least one microprocessor or CPU, an Input/output (I/O) interface, Random Access Memory (RAM), Read Only Memory (ROM), a storage device (either temporary or permanent) forming a computer readable medium programmed to execute one or more control programs to control the heat pump. The heat pump controller may optionally include an input interface such as a keypad to receive inputs from a user and a display device used to display various parameters to a user. The parts and programming are conventional, except as related to controlling surge, and thus, will not be discussed in detail herein, except as needed to understand the embodiment(s).

General Interpretation of Terms

(45) In understanding the scope of the present invention, the term “comprising” and its derivatives, as used herein, are intended to be open ended terms that specify the presence of the stated features, elements, components, groups, integers, and/or steps, but do not exclude the presence of other unstated features, elements, components, groups, integers and/or steps. The foregoing also applies to words having similar meanings such as the terms, “including”, “having” and their derivatives. Also, the terms “part,” “section,” “portion,” “member” or “element” when used in the singular can have the dual meaning of a single part or a plurality of parts.

(46) The term “detect” as used herein to describe an operation or function carried out by a component, a section, a device or the like includes a component, a section, a device or the like that does not require physical detection, but rather includes determining, measuring, modeling, predicting or computing or the like to carry out the operation or function.

(47) The term “configured” as used herein to describe a component, section or part of a device includes hardware and/or software that is constructed and/or programmed to carry out the desired function.

(48) The terms of degree such as “substantially”, “about” and “approximately” as used herein mean a reasonable amount of deviation of the modified term such that the end result is not significantly changed.

(49) While only selected embodiments have been chosen to illustrate the present invention, it will be apparent to those skilled in the art from this disclosure that various changes and modifications can be made herein without departing from the scope of the invention as defined in the appended claims. For example, the size, shape, location or orientation of the various components can be changed as needed and/or desired. Components that are shown directly connected or contacting each other can have intermediate structures disposed between them. The functions of one element can be performed by two, and vice versa. The structures and functions of one embodiment can be adopted in another embodiment. It is not necessary for all advantages to be present in a particular embodiment at the same time. Every feature which is unique from the prior art, alone or in combination with other features, also should be considered a separate description of further inventions by the applicant, including the structural and/or functional concepts embodied by such feature(s). Thus, the foregoing descriptions of the embodiments according to the present invention are provided for illustration only, and not for the purpose of limiting the invention as defined by the appended claims and their equivalents.