JP4924092B2 - Refrigeration cycle equipment - Google Patents

Description

  The present invention relates to a positive displacement expander, an expander-integrated compressor, and a refrigeration cycle apparatus.

  Conventionally, a power recovery type refrigeration cycle apparatus that recovers expansion energy of a refrigerant (working fluid) with an expander and uses the recovered energy as part of an input of a compressor has been proposed. As such a refrigeration cycle apparatus, for example, a refrigeration cycle apparatus including a fluid machine (hereinafter referred to as an “expander-integrated compressor”) in which an expander and a compressor are connected by a rotating shaft is known (for example, , See Patent Document 1 below).

  As will be described later, in a refrigeration cycle apparatus equipped with an expander-integrated compressor, the ratio between the refrigerant density on the compressor inlet side and the refrigerant density on the expander inlet side is always constant. Conversely, in a refrigeration cycle apparatus equipped with an expander-integrated compressor, the operation is performed under the constraint that the density ratio is always constant. Therefore, there is a problem that highly efficient operation is difficult.

  Therefore, a refrigeration cycle apparatus has been proposed in which an injection passage is provided for the expander and the restriction of the density ratio is avoided by adjusting the amount of refrigerant injected (see, for example, Patent Document 2 below). .

  The conventional refrigeration cycle apparatus will be described with reference to FIG. This refrigeration cycle apparatus includes a main refrigerant circuit 108 and an injection passage 109. The main refrigerant circuit 108 includes a compressor 101, a gas cooler (heat radiator) 102, an expander 103, and an evaporator 104. The compressor 101, the expander 103, and the rotary electric motor 106 are connected by a rotary shaft 107. The upstream side of the injection passage 109 is connected between the gas cooler 102 and the expander 103, and the downstream side of the injection passage 109 is connected to the injection port 113 of the expander 103. The injection passage 109 is provided with a valve 105 whose opening degree can be freely adjusted.

  The refrigerant discharged from the compressor 101 is cooled by the gas cooler 102 and then divided into a refrigerant flowing through the main refrigerant circuit 108 and a refrigerant flowing through the injection passage 109. One of the divided refrigerant is sucked into the expander 103 through the suction port 111 and expands in the expander 103. The other refrigerant that has been diverted is decompressed and expanded by the valve 105 of the injection passage 109 and is sucked into the expander 103 through the injection port 113. The refrigerant sucked from the injection port 113 merges with the refrigerant sucked from the suction port 111, expands in the expander 103, and is discharged from the discharge port 112. The discharged refrigerant is heated by the evaporator 104 and returns to the compressor 101.

  Here, assuming the case where the valve 105 of the injection passage 109 is fully closed, the above-described restriction of the density ratio is described.

  When the suction volume of the compressor 101 is Vcs, the suction volume of the expander 103 is Ves, and the rotation speed of the rotary shaft 107 is N, the refrigerant volume flow rate on the inlet side of the compressor 101 and the inlet side of the expander 103 are The volume flow rate of the refrigerant is (Vcs × N) and (Ves × N), respectively. Here, since the mass flow rate of the refrigerant flowing through the injection passage 109 is zero, the mass flow rate in the compressor 101 and the mass flow rate in the expander 103 are equal. When this mass flow rate is G, the refrigerant density on the inlet side of the compressor 101 and the refrigerant density on the inlet side of the expander 103 are {G / (Vcs × N)} from the ratio of the respective volume flow rate and mass flow rate. , {G / (Ves × N)}. From these equations, the ratio of the refrigerant density on the inlet side of the compressor 101 and the refrigerant density on the inlet side of the expander 103 is {G / (Vcs × N)} / {G / (Ves × N)}, that is, , (Ves / Vcs).

FIG. 16 shows a Mollier diagram of the refrigeration cycle. In the figure, the compression process in the compressor 101 corresponds to the line AB, the heat release process in the gas cooler 102 corresponds to the line BC, the expansion process in the expander 103 corresponds to the line CD, and the evaporation process in the evaporator 104 corresponds to the line DA. Since the density ratio of the refrigerant at the point A on the inlet side of the compressor 101 and the point C on the inlet side of the expander 103 is constant at (Ves / Vcs), the density of the working fluid at the point A is ρ ₀ . Then, the density ρc at point C is (Vcs / Ves) ρ _0. Assuming that the density of the point A is constant, when the pressure at the point C is increased, the point C changes along the line ρc = (Vcs / Ves) ρ ₀ toward the point C ′. In other words, it becomes impossible to change the point C to the point C ″ increased by the pressure along the isotherm (T = Tc), and the free control of the refrigeration cycle is hindered. Since there is an optimum high pressure that maximizes the coefficient of performance (COP) at temperature, efficient operation cannot be achieved unless the temperature and pressure are freely controlled.

The restriction on the density ratio is due to the fact that the mass flow rate in the compressor 101 and the mass flow rate in the expander 103 are equal, and the ratio of the volume flow rate is constant. However, this restriction can be avoided by opening the valve 105 of the injection passage 109 and allowing a part of the refrigerant to flow through the injection passage 109.
JP 2001-116371 A International Publication No. 2006/004047 Pamphlet

  However, in the refrigeration cycle apparatus provided with the injection passage 109, the refrigerant flowing through the injection passage 109 expands to some extent in the valve 105 unless the valve 105 is fully opened. Therefore, there is a problem that a part of the expansion energy cannot be recovered.

  FIG. 17 is a graph for explaining the energy recovery efficiency of the expander in the refrigeration cycle apparatus provided with the injection passage 109. The horizontal axis of the graph in FIG. 17 represents the season, and the vertical axis represents the energy recovery efficiency. As shown in FIG. 17, the recovery efficiency is high in the winter season when the valve 105 of the injection passage 109 is fully closed or close to fully closed, or in the summer when the valve 105 is fully open or close to fully open. On the other hand, in the intermediate period when the valve 105 is throttled to some extent, the recovery efficiency is greatly reduced.

  Thus, in the conventional refrigeration cycle apparatus provided with the injection passage, the operation range in which the recovery efficiency can be improved is narrow. For this reason, the recovery efficiency could not be increased over a wide operating range.

  The present invention has been made in view of this point, and an object of the present invention is to improve recovery efficiency over a wide operating range in an expander or the like that recovers expansion energy of a working fluid.

The refrigeration cycle apparatus according to the present invention includes a suction port that sucks a working fluid, a working fluid chamber that expands the working fluid sucked from the suction port when the volume changes, and an operation that is expanded in the working fluid chamber. a discharge port for discharging the fluid, leads to the working fluid chamber, respectively, first Lee emissions jection port and the second injection to the injection of working fluid into the working fluid chamber at a different timing of the expansion process of the working fluid in the working fluid chamber An expansion mechanism comprising a positive displacement expander provided with a port , a compression mechanism for compressing a working fluid, a rotating shaft connecting the expansion mechanism and the compression mechanism, the compression mechanism, a radiator, A main refrigerant circuit in which an expansion mechanism and an evaporator are sequentially connected in an annular shape; and the radiator and the expansion in the main refrigerant circuit A first injection passage for supplying the working fluid to the first injection port via a first valve whose opening degree is adjustable, the first valve, and the first valve. A second injection passage for branching the working fluid to and from the injection port and supplying the working fluid to the second injection port via a second valve whose opening degree is adjustable, the second valve, and the second valve A passage for branching the working fluid between the two injection ports and supplying the working fluid between the expansion mechanism and the evaporator via a third valve whose opening degree is adjustable. is there.

  Further, another refrigeration cycle apparatus according to the present invention is a refrigeration cycle apparatus including the expander-integrated compressor, wherein the compression mechanism, the radiator, the expansion mechanism, and the evaporator are sequentially annular. A main refrigerant circuit connected to the plurality of injection passages, a plurality of injection passages for guiding refrigerant between the radiator and the expansion mechanism in the main refrigerant circuit to each of the plurality of injection ports, and the injection passages. And an opening adjustable valve.

  The valve is preferably an electromagnetic valve whose opening degree is adjustable.

  The plurality of injection ports include a first injection port and a second injection port, and the injection passage has a first valve whose opening degree is adjustable, and is connected to the first injection port. A first injection passage and a second injection passage having a second valve whose opening degree is adjustable and connected to the second injection port, the first injection passage and the second injection passage, May be arranged in parallel to each other.

  The plurality of injection ports include a first injection port and a second injection port. The injection passage has a first valve whose opening degree is adjustable, and the first injection port includes A first injection passage connected; and a second injection passage having a second valve whose opening degree is adjustable and connected to the second injection port. The first injection passage and the second injection The passages may be arranged in series with each other.

  The refrigerant may be carbon dioxide.

  According to the present invention, it is possible to improve the recovery efficiency of expansion energy in the expander over a wide operating range.

<Embodiment 1>
As shown in FIGS. 1 and 5, in the present embodiment, first and second injection ports 72 and 76 are provided in the expansion mechanism (volumetric expander) 3 of the expander-integrated compressor 10. The first and second injection ports 72 and 76 are connected to the first and second injection passages 81 and 82 arranged in parallel with each other, respectively.

<Configuration of expander-integrated compressor>
As shown in FIG. 1, the expander-integrated compressor 10 according to the present embodiment includes a sealed container 11, a scroll-type compression mechanism 1 disposed on the upper side in the sealed container 11, and a lower part in the sealed container 11. And a rotary type expansion mechanism 3 disposed on the side. Between the compression mechanism 1 and the expansion mechanism 3, a rotary electric motor 6 including a rotor 6a and a stator 6b is disposed. The compression mechanism 1, the rotor 6 a of the rotary electric motor 6, and the expansion mechanism 3 are connected by a rotation shaft 7.

<Configuration of compression mechanism>
The compression mechanism 1 includes a fixed scroll 21, a turning scroll 22, an Oldham ring 23, a bearing member 24, and a muffler 25. A suction pipe 26 and a discharge pipe 27 are connected to the sealed container 11. The orbiting scroll 22 is fitted to the eccentric shaft 7 a of the rotating shaft 7, and the rotation motion is restricted by the Oldham ring 23. The orbiting scroll 22 is provided with a spiral wrap 22a, and the fixed scroll 21 is also provided with a spiral wrap 21a. The wrap 22a and the wrap 21a mesh with each other to form a working chamber 28 having a crescent-shaped cross section.

  The wrap 22 a of the orbiting scroll 22 performs the orbiting motion with the rotation of the rotary shaft 7 while meshing with the wrap 21 a of the fixed scroll 21. As a result, the crescent-shaped working chamber 28 formed between the wrap 21a and the wrap 22a compresses the refrigerant sucked from the suction pipe 26 by reducing the volume while moving from the outside in the radial direction to the inside. To do. The compressed refrigerant passes through a discharge hole 21b formed in the central portion of the fixed scroll 21, an inner space 25a of the muffler 25, and a flow path 29 passing through the fixed scroll 21 and the bearing member 24 in this order, 11 is discharged into the internal space 11a. The refrigerant discharged into the internal space 11a is discharged from the discharge pipe 27 after separating the lubricating oil mixed in the refrigerant by gravity or centrifugal force while staying in the internal space 11a.

<Configuration of expansion mechanism>
The expansion mechanism 3 includes a first cylinder 41, a second cylinder 42 that is thicker than the first cylinder 41, and an intermediate plate 43 that partitions the cylinders 41 and 42. The first cylinder 41 and the second cylinder 42 are both formed in a cylindrical shape, and are arranged in a straight line up and down so that their centers coincide.

  The expansion mechanism 3 further includes a cylindrical first piston 44, a first vane 46, and a first spring 48 that biases the first vane 46 toward the first piston 44. An eccentric portion 7b of the rotating shaft 7 is inserted into the first piston 44, and the first piston 44 performs an eccentric rotational motion inside the first cylinder 41 as the eccentric portion 7b rotates. The first cylinder 41 is formed with a vane groove 41a (see FIG. 2) extending in the radial direction. The first vane 46 is held in the vane groove 41a so as to freely reciprocate. One end of the first vane 46 is in contact with the first piston 44, and the other end of the first vane 46 is in contact with the first spring 48.

  The expansion mechanism 3 includes a cylindrical second piston 45, a second vane 47, and a second spring 49 that urges the second vane 47 toward the second piston 45. The eccentric part 7c of the rotating shaft 7 is inserted into the second piston 45, and the second piston 45 eccentrically rotates inside the second cylinder 42 as the eccentric part 7c rotates. The second cylinder 42 is formed with a vane groove 42a (see FIG. 3) extending in the radial direction. The second vane 47 is held in the vane groove 42a so as to freely reciprocate. One end of the second vane 47 is in contact with the second piston 45, and the other end of the second vane 47 is in contact with the second spring 49.

  The expansion mechanism 3 further includes an upper end plate 50 and a lower end plate 51 that are disposed so as to sandwich the first cylinder 41, the intermediate plate 43, and the second cylinder 42. The upper end plate 50 and the middle plate 43 sandwich the first cylinder 41 from above and below, and the middle plate 43 and the lower end plate 51 sandwich the second cylinder 42 from above and below. By the upper end plate 50, the middle plate 43, and the lower end plate 51, working chambers are formed in the first cylinder 41 and the second cylinder 42, the volumes of which change according to the rotation of the pistons 44 and 45, respectively. ing. The upper end plate 50 and the lower end plate 51 function as a bearing member that rotatably supports the rotary shaft 7 together with the bearing member 24 of the compression mechanism 1. Similarly to the compression mechanism 1, the expansion mechanism 3 also includes a muffler 52. A suction pipe 53 and a discharge pipe 58 (not shown in FIG. 1, see FIG. 5) are connected to the expansion mechanism 3.

  As shown in FIG. 2, a suction-side working chamber 55a and a discharge-side working chamber 55b are formed inside the first cylinder 41 and outside the first piston 44. The working chamber 55a and the working chamber 55b are partitioned by the first vane 46. As shown in FIG. 3, a suction-side working chamber 56 a and a discharge-side working chamber 56 b are also formed inside the second cylinder 42 and outside the second piston 45. The working chamber 56 a and the working chamber 56 b are partitioned by the second vane 47. Since the second cylinder 42 is thicker (that is, the length in the vertical direction) than the first cylinder 41, the total volume of the two working chambers 56 a and 56 b in the second cylinder 42 is the two operations in the first cylinder 41. It is larger than the total volume of the chambers 55a and 55b. The discharge side working chamber 55 b of the first cylinder 41 and the suction side working chamber 56 a of the second cylinder 42 communicate with each other through a communication hole 43 a formed in the intermediate plate 43. The working chamber 55b, the communication hole 43a, and the working chamber 56a function as one working chamber. Hereinafter, the working chamber formed by the working chamber 55b, the communication hole 43a, and the working chamber 56a is referred to as an expansion chamber.

  As shown in FIGS. 1 and 2, the upper end plate 50 is formed with a suction passage 90 extending in the radial direction and a suction port 71 opening downward from the suction passage 90 toward the working chamber 55a. A suction pipe 53 is connected to the outer end of the suction path 90. Thus, the refrigerant sucked from the suction pipe 53 is supplied to the suction side working chamber 55 a through the suction path 90 and the suction port 71.

  As shown in FIGS. 1 and 2, the upper end plate 50 includes a first flow path 73 extending in the radial direction, and a working chamber in the first cylinder 41 from the first flow path 73 (that is, the working chamber 55a). Alternatively, a first injection port 72 opening downward toward the working chamber 55b) is formed. A first injection pipe 74 is connected to the outer end of the first flow path 73. Thereby, the refrigerant sucked from the first injection pipe 74 is supplied to the working chamber in the first cylinder 41 through the first flow path 73 and the first injection port 72.

  As shown in FIG. 2, the upper end plate 50 further includes a second flow path 77 extending in the radial direction, and a working chamber (that is, the working chamber 55a or the working chamber 55b) in the first cylinder 41 from the second flow path 77. ) And a second injection port 76 opening downward. A second injection pipe 75 is connected to the outer end of the second flow path 77. Thereby, the refrigerant sucked from the second injection pipe 75 is supplied to the working chamber in the first cylinder 41 through the second flow path 77 and the second injection port 76.

  The first injection port 72 and the second injection port 76 are arranged to inject the refrigerant at different timings, although the refrigerant is injected as the first piston 44 rotates. In the present embodiment, the first injection port 72 and the second injection port 76 are formed at positions shifted by 90 degrees with respect to the center of the rotating shaft 7. However, the positions of the first injection port 72 and the second injection port 76 are not limited to the positions in the present embodiment, and the positions can be freely set.

  A first suction valve 82 a is disposed in the first injection port 72. The first suction valve 82a is a differential pressure valve that opens when the pressure on the upstream side (= the first flow path 73 side) becomes higher than the pressure on the downstream side (the working chamber side of the first cylinder 41). Similarly, a second suction valve 82b is disposed in the second injection port 76. The second suction valve 82b is also a differential pressure valve that opens when the pressure on the upstream side (= the second flow path 77 side) becomes higher than the pressure on the downstream side (the working chamber side of the first cylinder 41). The first suction valve 82a and the second suction valve 82b also function as check valves that prevent the refrigerant from flowing backward from the downstream side to the upstream side. The specific configuration of the first suction valve 82a and the second suction valve 82b is not limited at all, and for example, as shown in FIG. 4, a metal thin plate or the like can be suitably used. However, the suction valves 82a and 82b are not always necessary. That is, the injection ports 72 and 76 may always open toward the working chamber of the first cylinder 41.

  As shown in FIGS. 1 and 3, the lower end plate 51 is formed with a discharge port 51a that opens upward toward the working chamber 56b. The discharge-side working chamber 56b in the second cylinder 42 communicates with the internal space 52a of the muffler 52 through the discharge port 51a. The first cylinder 41 and the second cylinder 42 are formed with flow paths 57 that pass through the first cylinder 41 and the second cylinder 42. The downstream side of the flow path 57 is connected to a discharge pipe 58 (see FIG. 5). With such a configuration, the expanded refrigerant in the working chamber 56 b is once discharged into the internal space 52 a through the discharge port 51 a, passes through the flow path 57, and is discharged from the discharge pipe 58.

<< Configuration of refrigeration cycle apparatus >>
As shown in FIG. 5, the refrigeration cycle apparatus 9 according to the present embodiment includes a radiator (gas cooler) 2 and an evaporator 4 together with the expander-integrated compressor 10. The refrigeration cycle apparatus 9 includes a compression mechanism 1 of an expander-integrated compressor 10, a radiator 2, an expansion mechanism 3 of the expander-integrated compressor 10, and an evaporator 4 that are connected in an annular fashion in this order. A refrigerant circuit 80 is provided. The refrigeration cycle apparatus 9 includes a first injection passage 81, a second injection passage 82, and a bypass passage 83.

  The refrigeration cycle apparatus 9 is filled with carbon dioxide as a refrigerant. In the present embodiment, the refrigerant is in a supercritical state on the high-pressure side of the refrigerant circuit (specifically, the portion from the compression mechanism 1 through the radiator 2 to the expansion mechanism 3). However, the type of refrigerant is not particularly limited.

  The first injection passage 81 is a passage that supplies the refrigerant of the main refrigerant circuit 80 to the first injection port 72 of the expansion mechanism 3. One end of the first injection passage 81 is connected between the radiator 2 and the suction port 71 of the expansion mechanism 3, and the other end is connected to the first injection port 72 of the expansion mechanism 3. In the present embodiment, the first injection pipe 74 and the first flow path 73 described above form part of the first injection passage 81. The first injection passage 81 is provided with a first flow rate adjusting valve 91 made up of an electromagnetic valve whose opening degree can be adjusted.

  The second injection passage 82 is a passage for supplying the refrigerant of the main refrigerant circuit 80 to the second injection port 76 of the expansion mechanism 3. One end of the second injection passage 82 is connected between the radiator 2 and the first flow rate adjustment valve 91 of the first injection passage 81, and the other end is connected to the second injection port 76 of the expansion mechanism 3. In the present embodiment, the second injection pipe 75 and the second flow path 77 described above form part of the second injection passage 82. The second injection passage 82 is also provided with a second flow rate adjustment valve 92 made of an electromagnetic valve whose opening degree can be adjusted.

  The bypass passage 83 is a passage for supplying the refrigerant from the radiator 2 to the evaporator 4 without passing through the expansion mechanism 3. That is, it is a passage that bypasses the expansion mechanism 3. One end of the bypass passage 83 is connected to the downstream side of the first flow rate adjusting valve 91 in the first injection passage 81, and the other end is connected between the discharge pipe 58 of the expansion mechanism 3 and the evaporator 4 in the main refrigerant circuit 80. Has been. The bypass passage 83 is provided with a valve 93 that can be freely opened and closed. The valve 93 may be a valve whose opening degree can be adjusted freely, or may be a valve which cannot adjust the opening degree.

<Operation of expansion mechanism>
Next, the operation of the expansion mechanism 3 of the expander-integrated compressor 10 will be described with reference to FIGS. 6 to 8 show the states of the pistons 44 and 45 when the rotation angle θ of the rotating shaft 7 is 45 °. Here, the position where the contact point between the first cylinder 41 and the first piston 44 contacts the first vane 46 is a so-called top dead center (θ = 0 °), and the clockwise rotation direction, which is the rotation direction of the rotary shaft 7, is rotated. Display as the positive direction of the angle θ. The expansion mechanism 3 performs one cycle from the suction process to the discharge process while the rotary shaft 7 rotates three times. Therefore, in FIGS. 6 to 8, the rotation angle θ is expressed using an integer n (n = 0, 1, 2).

-Non-injection operation-
First, an operation that does not perform injection (= non-injection operation) will be described. In the non-injection operation, the first flow rate adjustment valve 91 of the first injection passage 81 is set to a fully closed state, and the second flow rate adjustment valve 92 of the second injection passage 82 is also set to a fully closed state.

  First, the cycle is started from θ = 0 ° of the first round (n = 0) of the pistons 44, 45, and the contact between the first cylinder 41 and the first piston 44 is sucked at θ = 20 ° (not shown). After passing through the port 71, the working chamber 55a and the suction port 71 communicate with each other and the suction process starts.

  Thereafter, the rotation angle θ increases as the pistons 44 and 45 rotate, and the volume of the working chamber 55a increases as the rotation angle θ increases. Eventually, when the contact between the first cylinder 41 and the first piston 44 passes θ = 360 ° at the start of the second round (n = 1), the working chamber 55a changes to the working chamber 55b, and the working chamber 55b One working chamber (= expansion chamber) is formed by communicating with the working chamber 56a of the second cylinder 42 through the communication hole 43a. When the rotating shaft 7 further rotates, at θ = 380 ° (not shown), the contact point between the first cylinder 41 and the first piston 44 passes through the suction port 71, and the communication between the working chamber 55b and the suction port 71 is established. Refused. At this point, the inhalation process ends and the expansion process begins.

  When the rotating shaft 7 further rotates, the volume of the working chamber 55b decreases. However, since the second cylinder 42 has a greater thickness (vertical length) than the first cylinder 41 as described above, The volume increases at a higher rate. As a result, the volume of the expansion chamber (= working chamber 55b + communication hole 43a + working chamber 56a) increases and the refrigerant expands.

  When the rotating shaft 7 further rotates and reaches θ = 700 ° (not shown), the contact point between the second cylinder 42 and the second piston 45 passes through the discharge port 51a, and the expansion chamber (specifically, the working chamber 56a). ) Communicates with the discharge port 51a. At this point, the expansion process ends and the discharge process begins.

  At θ = 720 ° at the start of the third round (n = 2), the working chamber 55b of the first cylinder 41 disappears, the working chamber 56a of the second cylinder 42 changes to the working chamber 56b, and the rotating shaft 7 As the motor rotates, the volume of the working chamber 56b decreases, and the refrigerant is discharged from the discharge port 51a. Thereafter, the working chamber 56b disappears at θ = 1080 °, and the discharge process ends.

-First injection operation-
Next, an operation (= first injection operation) in which the refrigerant is injected from the first injection passage 81 and the refrigerant is not injected from the second injection passage 82 will be described. In this first injection operation, the first flow rate adjustment valve 91 of the first injection passage 81 is controlled to a predetermined opening other than full closing, and the second flow rate adjustment valve 92 of the second injection passage 82 is set to a fully closed state. The

  In the first injection passage 81, the refrigerant is decompressed to some extent by the first flow rate adjustment valve 91. Therefore, the refrigerant pressure on the near side of the first injection port 72 is lower than the refrigerant pressure in the suction pipe 53.

  Also in this operation, the cycle is started from θ = 0 ° of the first round (n = 0) of the pistons 44 and 45, and the first cylinder 41 and the first piston 44 are connected at θ = 20 ° (not shown). When the contact passes through the suction port 71, the working chamber 55a and the suction port 71 communicate with each other to start a suction process (hereinafter referred to as a first suction process).

  Thereafter, the rotation angle θ increases as the pistons 44 and 45 rotate, and the contact between the first cylinder 41 and the first piston 44 passes through the first injection port 72 at θ = 180 °. However, since the first injection port 72 is provided with the suction valve 82a, so long as the refrigerant pressure in the working chamber 55a is equal to or higher than the refrigerant pressure in the first flow path 73, the first injection port 72 to the working chamber 55a. The refrigerant is not injected into the inside. Therefore, the refrigerant continues to flow into the working chamber 55a only from the suction port 71.

  As the θ increases, the volume of the working chamber 55a increases. When θ = 360 ° at the start of the second round (n = 1) is passed, the working chamber 55a changes to the working chamber 55b, and the working chamber 55b One working chamber (expansion chamber) is formed by communicating with the working chamber 56a of the second cylinder 42 through the communication hole 43a. When the rotating shaft 7 further rotates, at θ = 380 ° (not shown), the contact point between the first cylinder 41 and the first piston 44 passes through the suction port 71, and the communication between the working chamber 55b and the suction port 71 is established. Refused. At this point, the first inhalation process ends.

  When the rotating shaft 7 further rotates, the volume of the expansion chamber increases and the refrigerant expands (hereinafter, this expansion process is referred to as a first expansion process). As the refrigerant expands, the pressure drops. When the refrigerant pressure in the expansion chamber becomes lower than the refrigerant pressure in the first flow path 73, the suction valve 82a of the first injection port 72 opens, and the refrigerant flows from the first injection port 72 to the expansion chamber (specifically, the working chamber 55b). Inflow. As a result, the first expansion process ends, and the suction process starts again. Hereinafter, this inhalation process is referred to as a second inhalation process.

  When the rotation shaft 7 further rotates and reaches θ = 540 °, the contact point between the first cylinder 41 and the first piston 44 passes through the first injection port 72, and the communication between the expansion chamber and the first injection port 72 is established. Refused. This ends the second inhalation process.

  Thereafter, the refrigerant in the expansion chamber expands as the rotating shaft 7 rotates. Hereinafter, this expansion process is referred to as a second expansion process. When the rotating shaft 7 further rotates and reaches θ = 700 ° (not shown), the contact point between the second cylinder 42 and the second piston 45 passes through the discharge port 51a, and the expansion chamber (specifically, the working chamber 56a). ) Communicates with the discharge port 51a. At this point, the second expansion process ends.

  When the second expansion process ends, a refrigerant discharge process is started. At θ = 720 ° at the start of the third round (n = 2), the working chamber 55b of the first cylinder 41 disappears, the working chamber 56a of the second cylinder 42 changes to the working chamber 56b, and the rotating shaft 7 As the motor rotates, the volume of the working chamber 56b decreases, and the refrigerant is discharged from the discharge port 51a. Then, at θ = 1080 °, the working chamber 56b disappears, and the discharge process ends.

-Second injection operation-
Next, an operation (= second injection operation) in which refrigerant is injected from the second injection passage 82 will be described. In the second injection operation, it is possible to inject the refrigerant from the first injection passage 81 together with the second injection passage 82. However, in the following explanation, the refrigerant is injected from the second injection passage 82 and the first injection is performed. It is assumed that the refrigerant is not injected from the passage 81. Therefore, in the second injection operation, the first flow rate adjustment valve 91 of the first injection passage 81 is set to a fully closed state, and the second flow rate adjustment valve 92 of the second injection passage 82 is set to a predetermined opening other than the fully closed state. Be controlled.

  By controlling the second flow rate adjustment valve 92 to a predetermined opening, the refrigerant is decompressed by the second flow rate adjustment valve 92 in the second injection passage 82. For this reason, the pressure of the refrigerant on the near side of the second injection port 76 is lower than the pressure of the refrigerant in the suction pipe 53.

  Also in this operation, the cycle is started from θ = 0 ° of the first round (n = 0) of the pistons 44 and 45, and the first cylinder 41 and the first piston 44 are connected at θ = 20 ° (not shown). When the contact passes through the suction port 71, the working chamber 55a and the suction port 71 communicate with each other and the suction process (first suction process) starts.

  Thereafter, the rotation angle θ increases as the pistons 44 and 45 rotate, and the contact between the first cylinder 41 and the first piston 44 passes through the second injection port 76 at θ = 270 °. However, since the second injection port 76 is provided with the suction valve 82b, as long as the refrigerant pressure in the working chamber 55a is equal to or higher than the refrigerant pressure in the second flow path 77, the working chamber 55a is connected from the second injection port 76. The refrigerant is not injected into the inside. Therefore, the refrigerant continues to flow into the working chamber 55a only from the suction port 71.

  The volume of the working chamber 55a increases as θ increases, and after passing θ = 360 ° at the start of the second round (n = 1), the working chamber 55a changes to the working chamber 55b, and the working chamber 55b One working chamber (expansion chamber) is formed by communicating with the working chamber 56a of the second cylinder 42 through the communication hole 43a. When the rotating shaft 7 further rotates, at θ = 380 ° (not shown), the contact point between the first cylinder 41 and the first piston 44 passes through the suction port 71, and the communication between the working chamber 55b and the suction port 71 is established. Refused. At this point, the first inhalation process ends.

  When the rotating shaft 7 further rotates, the volume of the expansion chamber increases and the refrigerant expands. As the refrigerant expands, the pressure drops. When the refrigerant pressure in the expansion chamber becomes lower than the refrigerant pressure in the second flow path 77, the suction valve 82b of the second injection port 76 opens, and the expansion chamber (specifically, the working chamber 55b) is opened from the second injection port 76. The refrigerant flows in. As a result, the first expansion process ends, and the second suction process starts.

  When the rotating shaft 7 further rotates and reaches θ = 630 °, the contact between the first cylinder 41 and the first piston 44 passes through the second injection port 76, and the communication between the expansion chamber and the second injection port 76 is established. Refused. This ends the second inhalation process.

  Thereafter, the refrigerant in the expansion chamber expands as the rotating shaft 7 rotates, and the second expansion process is performed. When the rotating shaft 7 further rotates and reaches θ = 700 ° (not shown), the contact point between the second cylinder 42 and the second piston 45 passes through the discharge port 51a, and the expansion chamber (specifically, the working chamber 56a). ) Communicates with the discharge port 51a. At this point, the second expansion process ends.

  When the second expansion process ends, a refrigerant discharge process is started. At θ = 720 ° at the start of the third round (n = 2), the working chamber 55b of the first cylinder 41 disappears, the working chamber 56a of the second cylinder 42 changes to the working chamber 56b, and the rotating shaft 7 As the motor rotates, the volume of the working chamber 56b decreases, and the refrigerant is discharged from the discharge port 51a. Then, at θ = 1080 °, the working chamber 56b disappears, and the discharge process ends.

-Bypass operation-
The bypass operation is an operation in which a part of the refrigerant flowing from the radiator 2 is bypassed without passing through the expansion mechanism 3. In the bypass operation, the on-off valve 93 is opened, and a part of the refrigerant passes through the on-off valve 93 without passing through the expansion mechanism 3, and is decompressed by the on-off valve 93 before being supplied to the evaporator 4.

《Relationship between rotation angle and each process》
FIG. 9 shows the relationship between the rotation angle θ of the rotating shaft 7 and each process in each operation. As described above, in the non-injection operation, the suction process, the expansion process, and the discharge process are performed in this order. On the other hand, in the first injection operation and the second injection operation, the first suction process, the first expansion process, the second suction process, the second expansion process, and the discharge process are performed in this order.

  In each injection operation, at the end point X of the first expansion process, the refrigerant pressure in the expansion chamber (specifically, the working chamber 55b) and the refrigerant pressure in the flow paths 73 and 77 of the injection passages 81 and 82 become equal. This depends on the amount of pressure reduction of the refrigerant in the injection passages 81 and 82. In other words, it depends on the opening degree of the flow rate adjusting valves 91 and 92 in the injection passages 81 and 82, that is, the degree of throttle. Therefore, the end point X of the first expansion process can be adjusted by adjusting the opening degree of the flow rate adjusting valves 91, 92 in the injection passages 81, 82.

  By the way, when the flow rate adjusting valves 91 and 92 of the injection passages 81 and 82 are gradually throttled from the fully opened state, the amount of pressure reduction of the refrigerant in the flow rate adjusting valves 91 and 92 gradually increases. As a result, the energy that can be recovered by the expansion mechanism 3 is reduced by the amount of the reduced pressure of the refrigerant. Therefore, the recovery efficiency in the expansion mechanism 3 decreases as the opening degree of the flow rate adjusting valves 91 and 92 decreases from the fully open state. On the other hand, when the flow rate adjusting valves 91 and 92 are throttled, the mass flow rate of the refrigerant flowing through the injection passages 81 and 82, that is, the injection amount decreases. Therefore, if the flow rate adjusting valves 91 and 92 are throttled to a certain extent, the amount of decompression of the refrigerant increases, but the mass flow rate of the refrigerant flowing through the injection passages 81 and 82 decreases. As a result, the flow rate adjusting valves 91 and 92 are opened. The recovery efficiency increases as the degree decreases. Therefore, as schematically shown in FIGS. 10A and 10B, the energy recovery efficiency of the expansion mechanism 3 is such that the flow rate adjusting valves 91 and 92 of the injection passages 81 and 82 go from the fully closed state to the fully open state. As it decreases, it tends to increase after decreasing. As described above, the energy recovery efficiency of the expansion mechanism 3 is large when the flow rate adjusting valves 91 and 92 are close to the fully closed state or the fully open state, and decreases as the flow control valves 91 and 92 are separated from the fully closed state or the fully open state.

  If the injection passage is only one of the second injection passages 82, it is necessary to control the flow rate adjusting valve 92 over a wide operating range W from the fully open state to the fully closed state as shown in FIG. 10 (b). . For this reason, for example, in the intermediate period, the flow control valve 92 must be operated to a certain degree, and the operation must be performed under operating conditions with poor recovery efficiency between the fully closed state and the fully open state.

  However, the refrigeration cycle apparatus 9 according to the present embodiment includes a first injection passage 81 and a second injection passage 82, and a plurality of injection passages are provided. Therefore, the operation range W can be divided into a first operation range W1 for performing the first injection operation and a second operation range W2 for performing the second injection operation. And in the 1st operation range W1, the 1st flow control valve 91 can be operated on the conditions near a full open state or a fully closed state, and in the 2nd operation range W2, the 2nd flow control valve 92 is near a full open state. You can drive under conditions. As a result, an operation with high energy recovery efficiency can be performed in both the first operation range W1 and the second operation range W2, and the recovery efficiency can be maintained high over a wide operation range W.

  FIG. 11 shows the relationship between the rotation angle θ of the rotating shaft 7 and the working chamber volume in the expansion mechanism 3. The refrigerant moves in the order of the working chamber 55a, the working chamber 55b, the working chamber 56a, and the working chamber 56b. In this process, the volume of the working chamber changes in a sinusoidal curve. In FIG. 11, the presence of the communication hole 43a is ignored for the sake of simplicity.

<< Effect of this embodiment >>
As described above, according to the present embodiment, the expansion mechanism 3 of the expander-integrated compressor 10 includes the plurality of injection ports 72 and 76, and the injection ports 72 and 76 include the flow rate adjusting valves 91 and 76. The injection passages 81 and 82 having 92 are connected to each other. Therefore, the energy recovery efficiency of the expansion mechanism 3 can be kept high over a wide operation range by appropriately switching the injection passages 81 and 82 to be used according to the operation conditions. That is, as described above, the operating range W can be divided into a plurality of operating ranges W1 and W2, and the energy recovery efficiency can be increased in each of the operating ranges W1 and W2, so that the energy recovery efficiency can be increased over the entire operating range W. It can be kept high.

  Further, according to the present embodiment, the injection ports 72 and 76 are provided with the suction valves 82a and 82b for preventing the backflow, respectively. Therefore, the flow paths 73 and 77 outside the injection ports 72 and 76 (more specifically, the flow paths between the flow rate adjusting valves 91 and 92 and the injection ports 72 and 76 in the injection passages 81 and 82) are the dead volume. It can be prevented that the energy recovery efficiency is reduced.

  The positive displacement expander according to the present invention may be a rotary expander having a single cylinder, but in the present embodiment, the expansion mechanism 3 includes a first expander 41 and a second expander 42. The working chamber 55b in the first cylinder 41 and the working chamber 56a in the second cylinder 42 communicate with each other through the communication hole 43a. By the way, in a rotary expander having only one cylinder, a refrigerant suction process, an expansion process, and a discharge process must be performed while the piston rotates once in the cylinder. At that time, the flow rate of the refrigerant into the working chamber in the cylinder gradually increases with the rotation of the piston in the cylinder after the intake port is opened, but instantaneously becomes zero at the end of the intake process and rapidly decreases. . For this reason, sudden pressure fluctuations occur at the suction port, and so-called pulsation is likely to occur. On the other hand, according to the present embodiment, the refrigerant suction process, the expansion process, and the discharge process are performed by the entire first cylinder 41, the communication hole 43a, and the second cylinder 42. Further, the flow rate of the refrigerant into the working chamber 55a gradually increases with the rotation of the piston 44 after the suction port 71 is opened, and then gradually decreases to zero. Therefore, a rapid change in the refrigerant inflow rate is suppressed. Therefore, according to this embodiment, the pulsation of the refrigerant can be suppressed, and the operation can be stabilized or the efficiency can be further improved.

  In addition, according to the present embodiment, the injection ports 72 and 76 both open toward the working chamber (that is, the working chamber 55a or 55b) in the first cylinder 41. Therefore, a suitable injection operation can be performed. By the way, if the injection ports 72 and 76 are opened toward the working chamber in the discharge process, the refrigerant pressure in the discharge process becomes the lowest pressure in the refrigeration cycle, so that the discharge port 51a is discharged from the injection ports 72 and 76. The refrigerant may bypass the However, in this embodiment, in the working chamber in the first cylinder 41, the suction process and the expansion process are performed, but the discharge process is not performed. Therefore, the injection operation can be performed stably. The injection ports 72 and 76 may be opened toward the communication hole 43a that is always exposed to the expansion process. Also in this case, the injection operation can be performed stably.

  Further, according to the present embodiment, the injection ports 72 and 76 are open along the axial direction of the first cylinder 41. Therefore, the refrigerant flows from the injection ports 72 and 76 more smoothly.

  In the present embodiment, the expansion mechanism 3 that is a positive displacement expander is configured as a part of the expander-integrated compressor 10, and is connected to the compression mechanism 1 via the rotary shaft 7. Therefore, the rotation speed of the expansion mechanism 3 and the rotation speed of the compression mechanism 1 are always constant. Therefore, it is highly necessary to provide an injection passage in order to avoid the restriction of the constant density ratio described above. Therefore, the effect of the present embodiment, that is, the effect of improving the energy recovery efficiency at the time of operation accompanied by injection, is more remarkably exhibited.

  In the present embodiment, the flow rate adjusting valves 91 and 92 of the injection passages 81 and 82 are constituted by electromagnetic valves whose opening degrees can be adjusted. Therefore, a suitable flow rate adjustment valve can be realized at a relatively low cost. Further, the flow rate adjusting valves 91 and 92 can be easily controlled, and the injection operation can be controlled easily and accurately.

  As shown in FIG. 5, according to the present embodiment, the first injection passage 81 and the second injection passage 82 are arranged in parallel to each other. Therefore, each of the injection passages 81 and 82 can be used individually. When an abnormality occurs in one of the injection passages, the injection operation can be executed by using the other injection passage. For example, even if an abnormality occurs in the flow rate adjustment valve 91 in the first injection passage 81, the energy recovery efficiency is reduced by expanding the control range of the flow rate adjustment valve 92 in the second injection passage 82, but the entire operation range W It is possible to perform the injection operation over a wide range.

  In the present embodiment, carbon dioxide is used as the refrigerant. When carbon dioxide is used as the refrigerant, the difference between the high-pressure side pressure and the low-pressure side pressure in the refrigeration cycle increases. Therefore, the effect of power recovery in the expansion mechanism 3 becomes more remarkable.

<Embodiment 2>
As shown in FIG. 12, in the second embodiment, a first injection passage 81 and a second injection passage 82 are arranged in series with each other.

  Specifically, in the second embodiment, the upstream end of the first injection passage 81 is connected between the radiator 2 in the main refrigerant circuit 80 and the suction port 71 of the expansion mechanism 3, and downstream of the first injection passage 81. The end is connected to the first injection port 72 of the expansion mechanism 3. The upstream end of the second injection passage 82 is connected to the downstream side of the first flow rate adjusting valve 91 in the first injection passage 81, and the downstream end of the second injection passage 82 is connected to the second injection port 76 of the expansion mechanism 3. Has been. The upstream side of the bypass passage 83 is connected to the downstream side of the second flow rate adjustment valve 92 of the second injection passage 82, and the downstream side of the bypass passage 83 is between the expansion mechanism 3 and the evaporator 4 in the main refrigerant circuit 80. It is connected to the.

  Since other configurations are the same as those of the first embodiment, the description thereof is omitted.

  Also in this embodiment, a non-injection operation that does not inject the expansion mechanism 3, a first injection operation that injects refrigerant from the first injection port 72, and a second injection operation that injects refrigerant from the second injection port 76. And can be executed. Also, bypass operation is possible.

  In the present embodiment, the first flow rate adjustment valve 91 is set to a fully closed state during non-injection operation. During the first injection operation, the first flow rate adjusting valve 91 is controlled to a predetermined opening other than fully closed, and the second flow rate adjusting valve 92 is set to a fully closed state. During the second injection operation, the first flow rate adjustment valve 91 is set to an open state (not necessarily fully open), and the second flow rate adjustment valve 92 is controlled to a predetermined opening other than full close. The During the bypass operation, both the first flow rate adjustment valve 91 and the second flow rate adjustment valve 92 are set to the open state, and the on-off valve 93 is set to the open state.

  Also in the present embodiment, for the same reason as in the first embodiment, it is possible to maintain high energy recovery efficiency of the expansion mechanism 3 over a wide operation range.

  In the present embodiment, the first injection passage 81 and the second injection passage 82 are arranged in series with each other. Therefore, the refrigerant supplied to the second injection port 76 can be depressurized again by the second flow rate adjusting valve 92 after being first depressurized by the first flow rate adjusting valve 91. Therefore, the amount of pressure reduction required for the second flow rate adjustment valve 92 can be suppressed. Therefore, the size of the second flow rate adjustment valve 92 can be reduced.

<Embodiment 3>
In the above embodiment, the positive displacement expander according to the present invention constitutes the expansion mechanism 3 of the expander-integrated compressor 10, but the positive displacement expander according to the present invention is an expander-integrated compressor. It is not limited to what was incorporated in 10. The positive displacement expander according to the present invention may be used alone.

  As shown in FIG. 13, the refrigeration cycle apparatus 9 according to the third embodiment is a power recovery type refrigeration cycle apparatus using a separation type expander 63. The refrigeration cycle apparatus 9 has substantially the same configuration as the refrigeration cycle apparatus 9 according to the first embodiment, but instead of the expander-integrated compressor 10, a compressor 61 and an expander 63 that are separated from each other, and a rotary shaft A rotary electric motor 66 connected to the compressor 61 through 7d and a generator 67 connected to the expander 63 through the rotary shaft 7e are provided. In addition, the same code | symbol is attached | subjected to the part similar to Embodiment 1, and the description is abbreviate | omitted.

  The expander 63 includes a working chamber (not shown) that performs suction, expansion, and discharge of the refrigerant by changing the volume, a suction port 71, a discharge port 51a, a first injection port 72, and a first injection port. A second injection port 76 for injecting the refrigerant at a timing different from that of 72 is formed.

  The refrigeration cycle apparatus 9 includes a main refrigerant circuit 80 formed by annularly connecting a compressor 61, a radiator 2, an expander 63, and an evaporator 4 in this order. The upstream end of the first injection passage 81 is connected between the radiator 2 and the suction port 71 of the expander 63, and the downstream end thereof is connected to the first injection port 72 of the expander 63. The first injection passage 81 is provided with a first flow rate adjusting valve 91 similar to that of the first embodiment. The upstream end of the second injection passage 82 is connected to the upstream side of the first flow rate adjusting valve 91 of the first injection passage 81, and the downstream end of the second injection passage 82 is connected to the second injection port 76 of the expander 63. Has been.

  The compressor 61 is driven by a rotary electric motor 66, and in the expander 63, the expansion energy of the refrigerant is converted into electric energy by a generator 67. This electrical energy is used as part of the input of the rotary motor 66.

  FIG. 14 shows an efficiency curve of a general generator 67. Since the generator 67 is designed to have the highest power generation efficiency at a predetermined rated rotational speed Nr, the power generation efficiency decreases as the rotational speed goes away from the rated rotational speed Nr. For this reason, it is desirable that the rotational speed of the generator 67 be as close to the rated rotational speed Nr as possible.

  However, in the refrigeration cycle, since the circulation amount and density of the refrigerant change, it is difficult to operate an expander without an injection port only near the rated speed Nr. However, in this embodiment, the expander 63 is provided with injection ports 72 and 76. Therefore, by performing the injection operation, the rotational speed of the generator 67 can be made close to the rated rotational speed Nr, and the power generation efficiency can be improved. Moreover, according to the present embodiment, as described above, the energy recovery efficiency can be increased in a wide operation range of the injection operation. Therefore, it is possible to further improve the power generation efficiency.

<< Other modifications >>
In each of the embodiments described above, the injection ports 72 and 76 are formed in the upper end plate 50 and open along the axial direction of the first cylinder 41 toward the working chamber 55a or 55b. However, the injection ports 72 and 76 may be formed in portions other than the upper end plate 50. Further, the opening direction of the injection ports 72 and 76 may not be a direction parallel to the axial direction of the first cylinder 41. For example, the first flow path 73 and the first injection port 72 may be formed in the first cylinder 41, and the first injection port 72 may open radially inward on the inner peripheral surface of the first cylinder 41. Further, the second flow path 77 and the second injection port 76 may be formed in the first cylinder 41, and the second injection port 76 may open radially inward on the inner peripheral surface of the first cylinder 41.

  The positive displacement expander according to the present invention is not limited to the rotary expander as in the above embodiment.

  Although the refrigeration cycle apparatus 9 according to the embodiment is an apparatus in which the refrigerant flows only in one direction, the refrigeration cycle apparatus according to the present invention may be an apparatus in which the refrigerant distribution direction can be changed. That is, the refrigeration cycle apparatus according to the present invention may be a refrigeration cycle apparatus capable of so-called reversible operation, for example, cooling operation and heating operation.

  In the embodiment, the number of injection ports of the positive displacement expander is two, and the number of injection passages of the refrigeration cycle apparatus is two. However, there may be three or more injection ports, and there may be three or more injection passages.

  In the embodiment, the injection ports 72 and 76 are open toward the working chamber in the first cylinder 41, but at least one of the plurality of injection ports is directed toward the working chamber in the second cylinder 42. It may be open.

  As described above, the present invention is useful for positive displacement expanders, expander-integrated compressors, and refrigeration cycle apparatuses.

Vertical section of an expander-integrated compressor according to an embodiment II-II sectional view of FIG. III-III sectional view of FIG. Configuration diagram of intake valve Refrigerant circuit diagram of refrigeration cycle apparatus according to Embodiment 1 (A)-(c) is a figure which shows the operation principle of the expansion mechanism of an expander integrated compressor. (A)-(c) is a figure which shows the operation principle of the expansion mechanism of an expander integrated compressor. (A)-(b) is a figure which shows the operating principle of the expansion mechanism of an expander integrated compressor. The figure which shows the relationship between the rotation angle of the rotating shaft in the expansion mechanism of an expander integrated compressor, and each process of a working chamber. (A) to (c) are characteristic curve diagrams of energy recovery efficiency. The figure which shows the relationship between the rotation angle of the rotating shaft in an expansion mechanism of an expander integrated compressor, and a working chamber volume. Refrigerant circuit diagram of refrigeration cycle apparatus according to Embodiment 2 Refrigerant circuit diagram of refrigeration cycle apparatus according to Embodiment 3 Diagram showing the relationship between generator speed and efficiency Refrigerant circuit diagram of conventional refrigeration cycle equipment Mollier diagram of refrigeration cycle Characteristic curve of energy recovery efficiency in conventional refrigeration cycle equipment

Explanation of symbols

1 Compression mechanism (compressor)
2 Radiator 3 Expansion mechanism (volumetric expander)
DESCRIPTION OF SYMBOLS 4 Evaporator 7 Rotating shaft 9 Refrigeration cycle apparatus 10 Expander-integrated compressor 41 First cylinder 42 Second cylinder 43 Middle plate (second closing member)
43a Communication hole 44 First piston 45 Second piston 50 Upper end plate (first closing member)
51 Lower end plate (third closing member)
51a Discharge port 55a, 55b, 56a, 56b Working chamber (working fluid chamber)
71 Suction Port 72 First Injection Port 76 Second Injection Port 80 Main Refrigerant Circuit 81 First Injection Passage 82 Second Injection Passage 82a First Suction Valve (Check Valve)
82b Second intake valve (check valve)
91 1st flow control valve (valve with adjustable opening)
92 Second flow rate adjustment valve (valve with adjustable opening)

Claims (4)

A suction port for sucking the working fluid;
A working fluid chamber for expanding the working fluid sucked from the suction port by changing the volume;
A discharge port for discharging the working fluid expanded in the working fluid chamber;
Leading to the working fluid chambers respectively, the volume type in which and a first Lee emissions jection port and a second injection port for injection of working fluid into the working fluid chamber at a different timing of the expansion process of the working fluid in the working fluid chamber An expansion mechanism comprising an expander;
A compression mechanism for compressing the working fluid;
A rotating shaft connecting the expansion mechanism and the compression mechanism;
A main refrigerant circuit in which the compression mechanism, a radiator, the expansion mechanism, and an evaporator are sequentially connected in an annular shape;
A first injection passage for branching the working fluid between the radiator and the expansion mechanism in the main refrigerant circuit and supplying the working fluid to the first injection port via a first valve whose opening degree is adjustable. When,
A second injection passage for branching the working fluid between the first valve and the first injection port and supplying the working fluid to the second injection port via a second valve whose opening degree is adjustable; ,
A passage for branching the working fluid between the second valve and the second injection port and supplying the working fluid between the expansion mechanism and the evaporator via a third valve whose opening degree is adjustable When,
A refrigeration cycle apparatus comprising: The refrigeration cycle apparatus according to claim 1,
A refrigeration cycle apparatus comprising a check valve that prevents backflow of the working fluid from each injection port. The refrigeration cycle apparatus according to claim 1 or 2 ,
The refrigeration cycle apparatus , wherein the first valve , the second valve, and the third valve are electromagnetic valves whose opening degrees are adjustable. In the refrigerating cycle device according to any one of claims 1 to 3 ,
The refrigeration cycle apparatus, wherein the refrigerant is carbon dioxide.

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