JP5595245B2 - Refrigeration equipment - Google Patents

Description

  TECHNICAL FIELD The present invention relates to a refrigeration apparatus that can be used for a home / business refrigeration refrigerator, an ultra-low temperature freezer, a refrigerated showcase cooling system, and the like. In particular, the present invention relates to a refrigeration apparatus having a plurality of refrigeration cycle apparatuses (refrigerant circulation circuits).

  Conventionally, for example, a refrigeration cycle apparatus (hereinafter referred to as a high temperature side cycle) on the high temperature side (high stage side, primary side) and a refrigeration cycle apparatus (hereinafter referred to as a low temperature side cycle) on the low temperature side (low stage side, secondary side). And a refrigeration apparatus configured in multiple stages (here, it is assumed that it is a two-stage dual refrigeration apparatus). In such a refrigeration apparatus, for example, the heat to be condensed by the condensation of the refrigerant in the low temperature side cycle and the evaporation heat from the evaporation of the refrigerant in the high temperature side cycle are heat-exchanged, and the cooling target etc. Refrigeration operation (cooling operation) is performed by exchanging heat with. Thereby, in the evaporator of a low temperature side cycle, the low-temperature heat | fever evaporating heat | fever minus tens of degrees can be obtained efficiently.

  In such a binary refrigeration system, if the operation is continued at a low temperature at which the evaporation temperature in the low-temperature cycle evaporator (low-temperature evaporator) is negative (below zero), moisture in the air freezes and low-temperature evaporation occurs. The capacity of the refrigeration apparatus (refrigeration capacity) is reduced because frost is formed on the container and the heat exchange with the object to be cooled is prevented. Therefore, for example, defrosting (defrosting, defrosting) that melts the frost of the low-temperature side evaporator by supplying a gaseous refrigerant (hereinafter referred to as hot gas) discharged from the compressor to the evaporator at predetermined time intervals, for example. ) Driving.

  At this time, for example, the four-way valve of the low-temperature side cycle is switched, and hot gas is supplied to the evaporator through a circulation path (reverse cycle) opposite to the normal refrigerant circulation path (forward cycle). Two-way refrigeration apparatuses that perform the defrosting operation have been proposed. Furthermore, an improved example of a binary refrigeration apparatus in which an intermediate cooler that functions as an evaporator during defrosting operation is additionally connected to a low-temperature cycle has been proposed (see, for example, Patent Document 1).

Japanese Utility Model Publication No. 1-144770 (page 201, FIGS. 1 and 2)

  In the conventional binary refrigeration apparatus, when the defrosting operation by the reverse cycle is performed, there are the following problems. For example, if the frost remains in the evaporator during the defrosting operation, the amount of heat of the hot gas is taken away by the melting of the frost, so the condensation temperature during the defrosting operation is about 10 ° C, which is slightly higher than 0 ° C. is there. However, when the frost is reduced, the evaporator blower is stopped, so the hot gas cannot be dissipated, the condensation temperature rises rapidly, and the refrigerant pressure in the low-temperature cycle suddenly rises. End up. Depending on the conditions, an abnormal increase in pressure in the low temperature side cycle may be detected and the operation stopped abnormally before the defrosting operation ends. In particular, in the case of a refrigerant having a high operating pressure and a relatively low critical temperature, for example, a refrigerant such as carbon dioxide (critical temperature is 31.1 ° C.), if the frost disappears during the defrosting operation, the critical temperature is quickly increased. It will exceed. For this reason, the refrigerant pressure rises abnormally, reaches the design pressure of the low-temperature cycle, and may cause an abnormal stop, a safety valve, etc.

  In addition, at the end of the defrosting operation, liquid refrigerant (liquid refrigerant) is accumulated by condensation in the evaporator of the low temperature side cycle. When the normal cooling operation by the normal cycle is resumed after the defrosting operation is completed in this state, a lot of liquid refrigerant may flow into the compressor, which may damage the compressor.

  The present invention has been made to solve the above-described problems, and suppresses an abnormal increase in the refrigerant pressure during the defrosting operation, and reliably and reliably without stopping the defrosting operation abnormally. A high refrigeration apparatus capable of performing defrosting operation in a short time is obtained.

A refrigerating apparatus according to the present invention is a high-temperature side cycle device that forms a high-temperature side circulation circuit that circulates a high-temperature side refrigerant by connecting a high-temperature side compressor, a high-temperature side condenser, a high-temperature side expansion device, and a high-temperature side evaporator by piping And connecting a low-temperature side compressor, an intermediate cooler, a low-temperature side condenser, a first low-temperature side expansion device, and a low-temperature side evaporator to form a low-temperature side circulation circuit for circulating the low-temperature side refrigerant. A flow path switching device for switching a refrigerant flow in the circulation circuit, a low temperature side cycle device having a second low temperature side throttle device between the intermediate cooler and the low temperature side condenser, a high temperature side evaporator and a low temperature In the defrosting operation of the cascade condenser that is configured by the side condenser and performs heat exchange between the high temperature side refrigerant and the low temperature side refrigerant, and the low temperature side evaporator that switches the refrigerant flow by the flow path switching device, Side evaporator and cold side condensation Condensing the low temperature-side refrigerant by the, to reduce the pressure of the low-temperature-side refrigerant in the second low-temperature-side throttle device, in which a control means for performing control so as to evaporate the low-temperature-side refrigerant in the intermediate cooler.

  Since the refrigeration apparatus of the present invention has the second low-temperature side expansion device between the intermediate cooler and the low-temperature side condenser, the defrosting system performs defrosting by supplying hot gas to the low-temperature side evaporator. During operation, not only the low temperature evaporator but also the low temperature condenser can function as a condenser. For this reason, even if the frost attached to the low-temperature side evaporator is reduced or eliminated, even if the condensing and liquefying function of the low-temperature side refrigerant by the low-temperature side evaporator is reduced, it can be condensed and liquefied in the low-temperature side condenser, An increase in the pressure of the low-temperature side refrigerant can be suppressed. Thereby, it is possible to obtain a refrigeration apparatus that can reliably perform a highly reliable defrosting operation without abnormally stopping the defrosting operation. In addition, when the defrosting operation is completed, the condensed and liquefied refrigerant flows into the low temperature side condenser, so that when the cooling operation is resumed, the condensed and liquefied refrigerant may suddenly return to the low temperature side compressor. The cooling operation can be resumed without damaging the low temperature side compressor.

It is a figure showing the structure of the binary refrigeration apparatus in Embodiment 1 of this invention. FIG. 3 is a Mollier diagram showing the cooling operation of the low temperature side cycle in the first embodiment. FIG. 3 is a diagram showing an operation control flowchart in the first embodiment. FIG. 3 is a Mollier diagram showing a defrosting operation of a low temperature side cycle in the first embodiment. FIG. 10 is a diagram showing an operation control flowchart in the second embodiment. FIG. 10 is a diagram showing an operation control flowchart in the third embodiment. It is a figure showing the structure of the binary refrigeration apparatus in Embodiment 4 of this invention. It is a figure showing the structure of the binary refrigeration apparatus in Embodiment 5 of this invention. FIG. 10 is a diagram showing an operation control flowchart in the fifth embodiment. It is a figure showing the structure of the binary refrigeration apparatus in Embodiment 6 of this invention.

  Next, embodiments of the present invention will be described with reference to the drawings.

Embodiment 1 FIG.
1 is a diagram showing a configuration of a binary refrigeration apparatus in Embodiment 1 of the present invention. As shown in FIG. 1, the binary refrigeration apparatus in the present embodiment includes a high temperature side cycle 10 and a low temperature side cycle 20, and configures a refrigerant circulation circuit that circulates refrigerant independently of each other. In order to make the two refrigerant circulation circuits into a multi-stage configuration, a cascade condenser (refrigerant) in which the high-temperature side evaporator 14 and the low-temperature side condenser 22 are coupled so as to be able to exchange heat between the refrigerants passing therethrough. An intermediate heat exchanger) 30 is provided. Moreover, it has the control means 40 which performs operation control of the whole binary refrigeration apparatus. Here, the levels of temperature and pressure described below are not particularly determined in relation to absolute values, but are relatively determined in the state and operation of the system, apparatus, etc. To do.

  In FIG. 1, a high temperature side cycle 10 includes a high temperature side compressor 11, a high temperature side condenser 12, a high temperature side expansion device 13, and a high temperature side evaporator 14 connected in series by a refrigerant pipe, Hereinafter, the high-temperature side circulation circuit is configured. On the other hand, the low temperature side cycle 20 includes a low temperature side compressor 21, a low temperature side four-way valve 25, a low temperature side intercooler (auxiliary condenser) 26, a second low temperature side expansion device 27, and a low temperature side condenser 22. The first low-temperature side expansion device 23 and the low-temperature side evaporator 24 are connected in series by a refrigerant pipe to constitute a refrigerant circulation circuit (hereinafter referred to as a low-temperature side circulation circuit).

  In the binary refrigeration apparatus having such a configuration, for example, R410A, R32, R404A, HFO-1234yf, propane, isobutane, carbon dioxide, ammonia and the like are circulated through the high-temperature side circulation circuit (hereinafter referred to as high-temperature side refrigerant). Used. Further, carbon dioxide, nitrogen, air, or the like is used as a refrigerant circulating through the high temperature side circulation circuit (hereinafter referred to as a low temperature side refrigerant). Here, an example in which R410A is used as the high temperature side refrigerant and carbon dioxide is used as the low temperature side refrigerant will be described.

  Each component apparatus of a binary refrigeration apparatus is demonstrated in detail. The high temperature side compressor 11 of the high temperature side cycle 10 sucks the high temperature side refrigerant, compresses it, and discharges it in a high temperature / high pressure state. Here, for example, it may be configured by a compressor of a type that can control the number of revolutions by an inverter circuit or the like and adjust the discharge amount of the high-temperature side refrigerant. The high temperature side condenser 12 performs heat exchange between air, water and the like supplied from, for example, a blower, a pump, or the like (not shown) and the high temperature side refrigerant to condense and liquefy the high temperature side refrigerant.

  The high temperature side expansion device 13 such as a pressure reducing valve or an expansion valve expands the high temperature side refrigerant by reducing the pressure. For example, it is optimally configured by a flow rate control means such as an electronic expansion valve, but it may also be configured by a refrigerant flow rate control means such as a capillary tube or a temperature-sensitive expansion valve. The high temperature side evaporator 14 evaporates the high temperature side refrigerant by heat exchange. For example, here, it is assumed that the heat transfer tube or the like through which the high-temperature side refrigerant passes in the cascade capacitor 30 serves as the high-temperature side evaporator 14 and performs heat exchange with the low-temperature side refrigerant.

  On the other hand, the low temperature side compressor 21 of the low temperature side cycle 20 sucks the low temperature side refrigerant, compresses the refrigerant, and discharges it in a high temperature / high pressure state. The low temperature side compressor 21 may be configured by a compressor of a type that has an inverter circuit or the like and can adjust the discharge amount of the low temperature side refrigerant.

  The low temperature side intercooler 26 functions as a gas cooler or a condenser, and performs heat exchange between air, water and the like supplied from a blower, a pump, or the like (not shown) and a low temperature side refrigerant to condense at a low temperature side. In the vessel 22, the low temperature side refrigerant is assisted to condense. Here, a blower or the like that supplies air or the like to the high temperature side condenser 12 may be used in common. The low temperature side condenser 22 condenses and liquefies the low temperature side refrigerant by heat exchange. For example, here, it is assumed that the heat transfer tube or the like through which the low-temperature side refrigerant passes in the cascade condenser 30 serves as the low-temperature side condenser 22 and performs heat exchange with the high-temperature side refrigerant.

  The first low temperature side expansion device 23 such as a pressure reducing valve or an expansion valve decompresses and expands the low temperature side refrigerant. For example, it is optimal to configure with flow rate control means such as an electronic expansion valve, but it may be configured with refrigerant flow rate control means such as capillaries. Further, the second low-temperature side expansion device 27 also decompresses and expands the low-temperature side refrigerant. Here, the low-temperature side refrigerant is depressurized, particularly in the defrosting operation. Here, it is assumed that the first low temperature side throttle device 23 and the second low temperature side throttle device 27 are constituted by flow rate control means for adjusting the opening degree based on an instruction from the control means 40. For example, in the case where the first low temperature side throttle device 23 and the second low temperature side throttle device 27 are refrigerant flow rate adjusting means that cannot adjust the opening, in order to minimize the throttle function and reduce pressure loss, for example, A bypass pipe (not shown) may be provided in parallel with the first low temperature side expansion device 23 and the second low temperature side expansion device 27. And when a refrigerant | coolant flow volume adjustment means is not required, you may comprise so that it can switch so that a refrigerant | coolant may be flowed to bypass piping.

  The low temperature side evaporator 24 performs heat exchange between air, brine, and the like supplied from, for example, a blower, a pump, or the like (not shown) and the low temperature side refrigerant to evaporate the low temperature side refrigerant. The object to be cooled or the like is directly or indirectly cooled by heat exchange with the low-temperature side refrigerant. Here, the blower or the like that supplies air or the like to the low-temperature side evaporator 24 is different from the blower or the like that supplies air or the like to the high-temperature side condenser 12 or the low-temperature side intercooler 26. The low temperature side four-way valve 25 serving as the flow path switching device switches the flow of the low temperature side refrigerant in the low temperature side circulation circuit. Here, the flow of the low-temperature side refrigerant in the normal cooling operation (forward cycle, forward direction) and the flow of the low-temperature side refrigerant in the defrosting operation (reverse cycle, reverse direction) are switched. In FIG. 1, the forward cycle is indicated by a solid line arrow, and the reverse cycle is indicated by a broken line arrow.

  The cascade condenser 30 is a refrigerant heat exchanger that has the functions of the high-temperature side evaporator 14 and the low-temperature side condenser 22 described above and enables heat exchange between the high-temperature side refrigerant and the low-temperature side refrigerant. For example, it is composed of a plate heat exchanger, a double pipe heat exchanger or the like. By making the high temperature side circulation circuit and the low temperature side circulation circuit into a multistage configuration via the cascade capacitor 30 and performing heat exchange between the refrigerants, independent refrigerant circulation circuits can be linked.

  Moreover, the control means 40 monitors the state of the high temperature side cycle 10 and the low temperature side cycle 20, and controls the cooling operation and the defrosting operation in the dual refrigeration apparatus. For example, operations of the high temperature side compressor 11, the high temperature side expansion device 13, the low temperature side compressor 21, the low temperature side four-way valve 25, the first low temperature side expansion device 23, the second low temperature side expansion device 27, and the like are controlled. Here, the control means 40 of this Embodiment has a timer and can time-measure. Further, here, the control means 40 will be described as controlling the operation of the equipment of the high temperature side cycle 10 and the low temperature side cycle 20, but for example, two units for controlling the equipment of the high temperature side cycle 10 and the low temperature side cycle 20 respectively. You may make it comprise with a control means.

  The evaporator temperature sensor 51 is a temperature detection unit that detects, for example, the temperature at which hot gas condenses and flows out in the low temperature side evaporator 24 and sends it to the control unit 40 as a signal. The discharge-side pressure sensor 52 is a pressure detection unit that detects the pressure of the low-temperature side refrigerant on the refrigerant discharge side (high-pressure side) of the low-temperature side compressor 21 and sends it to the control unit 40 as a signal.

In the binary refrigeration apparatus of the present embodiment, a second low temperature side expansion device 27 is provided between the low temperature side condenser 22 and the low temperature side intercooler 26. During the defrosting operation, the low temperature side evaporator 24 and the low temperature side condenser 22 are functioned as a condenser, and the low temperature side intercooler 26 is functioned as an evaporator. Thereby, even if the frost attached to the low-temperature side evaporator 24 is reduced or eliminated, the low-temperature side condenser 22 causes the low-temperature side refrigerant 22 to condense and liquefy even if the low-temperature side refrigerant condensing and liquefying function is reduced. Therefore, it is possible to prevent a sudden increase in pressure of the low-temperature side refrigerant such as CO ₂ and to efficiently defrost the low-temperature side evaporator 24 in a short time.

  Next, operation | movement of each component apparatus at the time of the cooling operation of a binary refrigeration apparatus is demonstrated based on the flow of the refrigerant | coolant which circulates through each refrigerant | coolant circulation circuit. First, the operation | movement at the time of the cooling operation of the high temperature side cycle 10 is demonstrated. The high temperature side compressor 11 sucks the high temperature side refrigerant, compresses it, and discharges it in a high temperature / high pressure state. The discharged refrigerant flows into the high temperature side condenser 12. The high temperature side condenser 12 performs heat exchange between air, water, and the like supplied from a blower, a pump, or the like (not shown) and the high temperature side refrigerant to condense and liquefy the high temperature side refrigerant. The condensed high-temperature side refrigerant passes through the high-temperature side expansion device 13. The high temperature side expansion device 13 depressurizes the condensed liquid refrigerant passing therethrough. The decompressed refrigerant flows into the high temperature side evaporator 14 (cascade capacitor 30). The high temperature side evaporator 14 evaporates and gasifies the high temperature side refrigerant by heat exchange with the low temperature side refrigerant. The high temperature side compressor 11 sucks the high temperature side refrigerant that has been vaporized into gas. Here, when the high temperature side expansion device 13 is an electronic expansion valve, for example, the control means 40 has a superheat degree (4 to 10 K) that requires the high temperature side refrigerant flowing out from the high temperature side evaporator 14 (high temperature side refrigerant). In the case of R410A), the high temperature side expansion device 13 is caused to adjust the opening degree.

  FIG. 2 is a Mollier diagram (PH diagram) showing a state of the low-temperature side refrigerant during the cooling operation. In FIG. 2, the vertical axis represents absolute pressure (MPaabs) and the horizontal axis represents specific enthalpy (KJ / kg). In FIG. 2, a portion surrounded by a B curve (a line formed by a saturated liquid line and a saturated vapor line) indicates that the low-temperature side refrigerant is in a gas-liquid two-phase state. Further, the portion on the left side of the saturated liquid line indicates that the low-temperature side refrigerant is in a liquid state, and the portion on the right side of the saturated vapor line indicates that the low-temperature side refrigerant is in a gas state.

  Further, in FIG. 2, the vertex H of the B curve is called a critical point, and there is no phase change of liquid and vapor in a portion above the critical point. A line represented by a substantially trapezoidal shape in FIG. 2 represents a change in refrigerant state or the like in an operation (process) performed by each device in the cooling operation of the low temperature side cycle 20. The low temperature side cycle 20 is closed because it constitutes a low temperature side circulation circuit. Details will be described later.

  Next, based on FIG. 1 and FIG. 2, the operation | movement at the time of the cooling operation of the low temperature side cycle 20 is demonstrated. The low temperature side compressor 21 sucks the low temperature side refrigerant, compresses the refrigerant, discharges it in a high temperature / high pressure state (compression process from point C to point D in FIG. 2). The discharged refrigerant flows into the low temperature side intercooler 26 through the low temperature side four-way valve 25. At this time, the low temperature side four-way valve 25 is switched so that the low temperature side refrigerant is in a positive cycle.

  The low temperature side intercooler 26 performs heat exchange between air, water, and the like supplied from a blower, a pump, or the like (not shown) and the refrigerant, and the low temperature side condenser 22 condenses and liquefies the low temperature side refrigerant. To assist. Here, the low temperature side intercooler 26 does not necessarily require the low temperature side refrigerant to be condensed and liquefied, but at least the heat (sensible heat) is taken from the low temperature side refrigerant so that the low temperature side refrigerant is kept at a constant temperature. (The condensation process from point D to point E in FIG. 2). Thereby, it becomes possible to improve cooling operation efficiency as the whole apparatus.

  The refrigerant that has flowed out of the low temperature side intercooler 26 passes through the second low temperature side expansion device 27 and flows into the low temperature side condenser 22 (cascade capacitor 30). Here, when the second low-temperature side expansion device 27 is an electronic expansion valve, the opening degree is fully opened so that the expansion function is not activated. Moreover, when bypass piping is provided in parallel, it is made to let bypass piping pass. Therefore, the second low temperature side expansion device 27 does not function during the cooling operation.

  The low temperature side condenser 22 condenses and liquefies the low temperature side refrigerant by heat exchange with the high temperature side refrigerant (condensation step from point E to point F in FIG. 2). The condensed low-temperature side refrigerant passes through the first low-temperature side expansion device 23. The first low temperature side expansion device 23 depressurizes the condensed low temperature side refrigerant (expansion step from point F to point G in FIG. 2). The decompressed low-temperature side refrigerant flows into the low-temperature side evaporator 24. The low temperature side evaporator 24 performs heat exchange between the object to be cooled and the low temperature side refrigerant, and evaporates the low temperature side refrigerant. And the low temperature side refrigerant | coolant which flowed out the low temperature side evaporator 24 is suck | inhaled by the low temperature side compressor 21 via the low temperature side four-way valve 25 (evaporation process from G point to C point in FIG. 2). The object to be cooled is cooled directly or indirectly.

  Here, the temperature of the low-temperature-side refrigerant of each device in the cooling operation under a certain operating condition is shown as an example. For example, the condensation temperature in the high temperature side condenser 12 is + 45 ° C., and the evaporation temperature in the high temperature side evaporator 14 is −10 ° C. The condensation temperature in the low temperature side condenser 22 is −5 ° C., and the evaporation temperature in the low temperature side evaporator 24 is −40 ° C. Further, the temperature of the low-temperature side refrigerant at the point C in FIG. 2 (the suction temperature of the low-temperature side compressor 21) is 0 ° C. The temperature of the low-temperature side refrigerant at point D (discharge side temperature of the low-temperature side compressor 21) is 120 ° C., and the temperature of the low-temperature side refrigerant at point E (temperature of the low-temperature side refrigerant that has passed through the low-temperature side intercooler 26) is 32 ° C.

  FIG. 3 is a diagram showing a flowchart of operation control of the binary refrigeration apparatus performed by the control means 40. As shown in FIG. 3, the control means 40 makes the high temperature side cycle 10 and the low temperature side cycle 20 perform a cooling operation (S1). And the control means 40 starts the time measurement by a timer.

  In the cooling operation, for example, as described above, the switching of the low temperature side four-way valve 25 is controlled so that the flow of the low temperature side refrigerant becomes a positive cycle. Further, the first low-temperature side expansion device 23 causes the refrigerant to be depressurized. On the other hand, the second low-temperature side expansion device 27 is fully opened to control the depressurization. And, for example, the operating state of the high temperature side cycle 10 and the low temperature side cycle 20 is monitored by means of detection means (not shown) such as the refrigerant pipe of the high temperature side cycle 10 and the low temperature side cycle 20, the temperature, pressure, etc. provided in the equipment, The cooling operation performed by the dual refrigeration apparatus is controlled (S2).

  If it is determined that a predetermined time has elapsed since the start of the cooling operation (S3), the control means 40 causes the high temperature side cycle 10 and the low temperature side cycle 20 to start the defrosting operation (S4). The predetermined time until the start of the defrosting operation is not particularly limited. For example, it sets based on the frost formation state of the low temperature side evaporator 24 assumed.

  Next, operation | movement of each component apparatus at the time of the defrost operation of a binary refrigeration apparatus is demonstrated based on the flow of the refrigerant | coolant which circulates through each refrigerant | coolant circulation circuit. Here, the operation in the defrosting operation of the high temperature side cycle 10 is the same as the operation in the cooling operation described above. However, in the defrosting operation, it is not always necessary to operate the high temperature side cycle 10, and control to stop the operation as necessary may be performed according to the cooling load in the high temperature side evaporator 14. Further, the evaporating temperature setting in the high temperature side evaporator 14 is not necessarily set to the same temperature as in the cooling operation.

  FIG. 4 is a Mollier diagram (PH diagram) showing the state of the low-temperature side refrigerant during the defrosting operation. 4, as in FIG. 2, the vertical axis represents absolute pressure (MPaabs) and the horizontal axis represents specific enthalpy (KJ / kg). The A line represented by the trapezoidal shape of FIG. 4 represents the change of the refrigerant | coolant state in the operation | movement (process) which each apparatus performs in the defrost operation of the low temperature side cycle 20 similarly to the A line of FIG. Details will be described later.

  Next, based on FIG. 1 and FIG. 4, the operation | movement at the time of the defrost operation of the low temperature side cycle 20 is demonstrated. The low temperature side compressor 21 sucks the low temperature side refrigerant, compresses the refrigerant, and discharges it in a high temperature / high pressure state (compression process from point C to point D in FIG. 4). The discharged refrigerant flows into the low temperature side evaporator 24 through the low temperature side four way valve 25. At this time, the control means 40 controls switching of the low temperature side four-way valve 25 so that the flow of the low temperature side refrigerant is in a reverse cycle. Moreover, control which stops the air blower etc. (not shown) which sends air etc. to the low temperature side evaporator 24 is performed.

  The low temperature side evaporator 24 heat-exchanges between frost and a low temperature side refrigerant | coolant, cools a low temperature side refrigerant | coolant to a fixed temperature, and condenses and liquefies (condensing process from D point to F point in FIG. 4). On the other hand, the phase of frost is changed to water and dripped from the low temperature side evaporator 24. The dripped water is collected by, for example, a drain pan (not shown) serving as a water tray, and discharged from the refrigerator (a space to be cooled), for example, to the outside.

  The low-temperature side refrigerant that has flowed out of the low-temperature side evaporator 24 passes through the first low-temperature side expansion device 23 and flows into the low-temperature side condenser 22. For example, when the first low temperature side expansion device 23 is an electronic expansion valve, the opening degree is fully opened so that the expansion function is not activated. Moreover, when bypass piping is provided in parallel, it is made to let bypass piping pass. Therefore, the first low-temperature side expansion device 23 does not function during the defrosting operation.

  Here, while the low temperature side refrigerant is condensed and liquefied by heat exchange with frost in the low temperature side evaporator 24, the low temperature side condenser 22 (cascade capacitor 30) does not need to condense and liquefy the low temperature side refrigerant. For this reason, the operation on the high temperature side cycle 10 side may be stopped. The low temperature side refrigerant that has flowed out of the low temperature side condenser 22 passes through the second low temperature side expansion device 27.

  The second low temperature side expansion device 27 depressurizes the condensed low temperature side refrigerant (expansion step from point F to point G in FIG. 4). The decompressed low-temperature side refrigerant flows into the low-temperature side intercooler 26. The low temperature side intercooler 26 performs heat exchange between air, water, and the like supplied from a blower, a pump, or the like (not shown) and the high temperature side refrigerant, and evaporates the low temperature side refrigerant. And the low temperature side refrigerant | coolant which flowed out the low temperature side intercooler 26 is suck | inhaled by the high temperature side compressor 11 via the low temperature side four-way valve 25 (evaporation process of G point from FIG. 4). Here, when the second low temperature side expansion device 27 is, for example, an electronic expansion valve, the control means 40 has a superheat degree (4 to 10 K) that requires the low temperature side refrigerant flowing out from the low temperature side intercooler 26. In addition, the second low temperature side expansion device 27 is caused to adjust the opening degree.

  As described above, during the defrosting operation, the operation is performed as described above while the low temperature side evaporator 24 has frost. As the defrosting operation proceeds and the frost in the low temperature side evaporator 24 decreases, the low temperature side evaporator 24 reduces the amount of heat exchanged between the frost and the low temperature side refrigerant. For this reason, the low temperature side refrigerant | coolant which the low temperature side evaporator 24 condenses and liquefies decreases. On the other hand, since the gaseous refrigerant (gas refrigerant) increases, the pressure of the low temperature side refrigerant rises. At this time, since the reduction of frost in the low temperature side evaporator 24 proceeds rapidly, the pressure also increases rapidly.

  The state of the refrigerant outlet of the low temperature evaporator 24 at this time is a state at point E on the Mollier diagram of FIG. For example, if the low temperature side evaporator 24 has sufficient frost, the point E coincides with the point F. When the frost decreases, the point E moves from the point F to the direction of the point D, and when the frost disappears and there is no heat exchange with the low-temperature side refrigerant, the point E coincides with the point D. Become.

  Therefore, the control means 40 performs control to suppress an increase in the pressure of the low-temperature side refrigerant (high-pressure side) even if the frost in the low-temperature side evaporator 24 decreases or disappears. For this reason, the high temperature side cycle 10 is operated, and in the cascade condenser 30, the high temperature side refrigerant passing through the high temperature side evaporator 14 and the low temperature side refrigerant passing through the low temperature side condenser 22 are subjected to heat exchange. And the gas refrigerant which could not be condensed and liquefied in the low temperature side evaporator 24 is condensed and liquefied. Accordingly, even if the frost is reduced or completely eliminated and the low temperature side evaporator 24 cannot sufficiently condense the low temperature side refrigerant, it is possible to prevent a rapid increase in the pressure of the low temperature side refrigerant.

  As shown in FIG. 3, when the defrosting operation is started, the control unit 40 stops a blower, a pump (not shown), and the like that send air, brine, and the like to the low temperature side evaporator 24. Further, the switching of the low temperature side four-way valve 25 is controlled so that the flow of the low temperature side refrigerant is in the reverse cycle. Then, the refrigerant is depressurized in the second low-temperature side expansion device 27, and the first low-temperature side expansion device 23 is fully opened to control the depressurization (S4). For example, when time management of the defrosting operation is performed, the control means 40 starts timing related to the defrosting operation.

  For example, when the control means 40 determines that the temperature detected by the evaporator temperature sensor 51 (temperature of the low-temperature side evaporator 24) has reached a predetermined temperature (S5), and determines that the defrosting operation is to be terminated, A blower, a pump (not shown), etc. are driven, and air, brine, etc. are sent into the low temperature side evaporator 24 (S6). Further, returning to S1, in order to perform the cooling operation, switching of the low temperature side four-way valve 25 is controlled so that the flow of the low temperature side refrigerant becomes a positive cycle. Further, the first low-temperature side expansion device 23 is controlled to depressurize the low-temperature side refrigerant, and the second low-temperature side expansion device 27 is fully opened to control the depressurization. And, for example, the operating state of the high temperature side cycle 10 and the low temperature side cycle 20 is monitored by means of detection means (not shown) such as the refrigerant pipe of the high temperature side cycle 10 and the low temperature side cycle 20, the temperature, pressure, etc. provided in the equipment, Controls the cooling operation performed by the dual refrigeration system. Here, in S5, the end determination of the defrosting operation is performed based on the temperature detected by the evaporator temperature sensor 51. However, the end determination may be performed based on the defrosting operation time or the like (hereinafter the same).

  For example, when the frost is reduced or disappeared during the defrosting operation, the outlet of the low temperature side evaporator 24 approaches the point D in FIG. 4, so that the condensed and liquefied refrigerant does not remain in the low temperature side evaporator 24. The condensed and liquefied refrigerant remains in the low temperature side condenser 22 upstream of the first low temperature side expansion device 23 in the positive cycle. From the above, when the reverse cycle is changed to the forward cycle, the cooling operation can be smoothly restarted without causing liquid return from the low temperature side evaporator 24 to the low temperature side compressor 21.

  Here, the temperature of the low-temperature-side refrigerant of each device in the cooling operation under a certain operating condition is shown as an example. For example, in the initial stage of the defrosting operation in which the low temperature side evaporator 24 is frosted, the high temperature side cycle 10 is stopped. The condensation temperature in the low temperature side evaporator 24 is + 12 ° C., and the evaporation temperature in the low temperature side intercooler 26 is −10 ° C. Moreover, the temperature of the low temperature side refrigerant | coolant in C point in FIG. 4 is 10 degreeC, and the temperature of the low temperature side refrigerant | coolant in D point is 80 degreeC.

  In the latter half of the defrosting operation in which the frost attached to the low temperature side evaporator 24 is reduced and the high temperature side cycle 10 is operated, for example, the condensation temperature in the high temperature side condenser 12 is + 45 ° C., and the evaporation temperature in the high temperature side evaporator 14. Is 0 ° C. The condensation temperature in the low temperature side condenser 22 is + 12 ° C., and the evaporation temperature in the low temperature side intercooler 26 is −10 ° C. Further, the temperature of the low-temperature side refrigerant at point C in FIG. 4 is 10 ° C., and the temperature of the low-temperature side refrigerant at point D is 80 ° C.

  As described above, the binary refrigeration apparatus of the first embodiment is configured to have the second low temperature side expansion device 27 between the low temperature side intercooler 26 and the low temperature side condenser 22, so that the defrosting operation is performed. Sometimes not only the low temperature evaporator 24 but also the low temperature condenser 22 can function as a condenser. For this reason, even if the frost attached to the low-temperature side evaporator 24 is reduced or eliminated, the low-temperature side condenser 22 causes the low-temperature side condenser 22 to condense and liquefy the liquefaction function of the low-temperature side refrigerant. It is possible to suppress an abnormal pressure increase of the low-temperature side refrigerant. Thereby, it is possible to obtain a refrigeration apparatus that can perform a reliable and reliable defrosting operation in a short time without failing to stop the defrosting operation abnormally. When the defrosting operation is completed, the low-temperature side refrigerant that has been condensed and liquefied is accumulated in the low-temperature side condenser 22 that is upstream from the first low-temperature side expansion device 23 in the cooling operation. For this reason, when the cooling operation is resumed, the condensed and liquefied low-temperature side refrigerant does not suddenly return (liquid back) to the low-temperature side compressor, and the low-temperature side compressor 21 is protected without being damaged. Cooling operation can be resumed while measuring.

  Further, since it can be condensed and liquefied in the low-temperature side condenser 22, even if a refrigerant having a relatively low critical temperature (31.1 ° C.) such as carbon dioxide is used as the low-temperature side refrigerant, it becomes critical during defrosting operation. A reliable defrosting operation can be performed more efficiently and in a shorter time without exceeding the temperature. For this reason, it can contribute to energy saving.

Embodiment 2. FIG.
FIG. 5 is a diagram showing a flowchart of operation control of the dual refrigeration apparatus according to Embodiment 2 of the present invention. In the first embodiment described above, when the defrosting operation is started, the refrigerant is decompressed in the second low temperature side expansion device 27 and the first low temperature side expansion device 23 is fully opened.

  In the present embodiment, at the initial stage of the defrosting operation in which the low temperature side evaporator 24 has frost, the refrigerant is decompressed in the first low temperature side expansion device 23 in the same manner as in the cooling operation. The low temperature side expansion device 27 is fully opened. Then, when the frost attached to the low-temperature side evaporator 24 is reduced and the high-temperature side cycle 10 is operated, the refrigerant is decompressed in the second low-temperature side expansion device 27, and the first low-temperature side expansion device 23. Is fully opened. In the case of the reverse cycle, the first low-temperature side expansion device 23 located near the low-temperature side evaporator 24 performs a pressure reducing operation, thereby improving the efficiency of heat exchange between the frost and the low-temperature side refrigerant in the low-temperature side evaporator 24. The time for defrosting operation can be shortened.

  In FIG. 5, for S11 to S14, basically the same processing as the processing of S1 to 4 described in the first embodiment is performed. Here, even when the defrosting operation is started in S14, as described above, the opening degrees of the first low temperature side expansion device 23 and the second low temperature side expansion device 27 are not changed. The first low-temperature side expansion device 23 is controlled to depressurize the low-temperature side refrigerant, and the second low-temperature side expansion device 27 is fully opened to control the depressurization.

  Then, it is determined whether or not the detected pressure of the discharge side pressure sensor 52 (the high pressure side pressure of the low temperature side cycle 20) is equal to or higher than a predetermined pressure (S15). If it is determined that the pressure is not higher than the predetermined pressure, the process returns to S14.

  On the other hand, if it is determined that the discharge pressure of the low temperature side compressor 21 has become equal to or higher than the predetermined pressure, the second low temperature side expansion device 27 depressurizes the refrigerant, and the first low temperature side expansion device 23 is fully opened. Thus, control is performed so as not to reduce pressure (S16). Then, the high temperature side cycle 10 is operated, and in the cascade capacitor 30, heat exchange is performed between the high temperature side refrigerant passing through the high temperature side evaporator 14 and the low temperature side refrigerant passing through the low temperature side condenser 22. Thereby, even when the frost attached to the low temperature side evaporator 24 decreases or disappears, a rapid increase in the pressure of the low temperature side refrigerant can be suppressed and a stable defrosting operation can be performed. About the process of S17 and S18, the process similar to S5 and S6 in the flowchart of FIG. 3 demonstrated in Embodiment 1 is performed.

  As described above, according to the binary refrigeration apparatus of the second embodiment, when the discharge pressure of the low temperature side compressor 21 (pressure on the high pressure side of the low temperature side cycle 20) becomes equal to or higher than a predetermined pressure during the defrosting operation. In addition, the second low temperature side expansion device 27 is configured to depressurize the refrigerant, and the first low temperature side expansion device 23 is fully opened to control the depressurization. In the initial stage, the first low-temperature side expansion device 23 located near the low-temperature side evaporator 24 performs a pressure reducing operation, thereby increasing the efficiency of heat exchange between the frost and the low-temperature side refrigerant in the low-temperature side evaporator 24, The defrosting operation time can be shortened. Further, similarly to the refrigeration apparatus of the first embodiment, an abnormal increase in the pressure of the low-temperature side refrigerant having a low critical temperature or the like is suppressed, and the defrosting operation is reliably stopped without stopping abnormally. Driving can be performed in a short time. Further, the cooling operation can be restarted without damaging the low temperature side compressor 21.

Embodiment 3 FIG.
FIG. 6 is a diagram showing a flowchart of operation control of the dual refrigeration apparatus according to Embodiment 3 of the present invention. In Embodiment 2 described above, when it is determined that the discharge pressure of the low temperature side compressor 21 has become equal to or higher than a predetermined pressure, the high temperature side cycle 10 is operated. The refrigerant was decompressed in the second low-temperature side expansion device 27, and the first low-temperature side expansion device 23 was fully opened to prevent pressure reduction.

  Here, when the defrosting operation is performed based on the high pressure side pressure of the low temperature side cycle 20, the high pressure side pressure may rise suddenly depending on conditions. Therefore, in the present embodiment, the control means 40 measures the time, and when a predetermined time elapses after the start of the defrosting operation (even before the high-pressure side pressure reaches the predetermined pressure), the high-temperature side cycle 10 To work. Further, the refrigerant is decompressed in the second low temperature side expansion device 27, and the first low temperature side expansion device 23 is fully opened to prevent the depressurization.

  In S21 to S24 in FIG. 6, the same processing as S11 to S14 in FIG. 5 is performed. In the present embodiment, it is determined whether a predetermined time has elapsed after the start of the defrosting operation (S25). If it is determined that the predetermined time has passed, the refrigerant is decompressed in the second low-temperature side expansion device 27, and the first low-temperature side expansion device 23 is fully opened to control the depressurization (S26). ). About the process of S27, S28, the process similar to S17, S18 in the flowchart of FIG. 5 demonstrated in Embodiment 2 is performed.

  As described above, according to the binary refrigeration apparatus of the third embodiment, when a predetermined time has elapsed after the defrosting operation is started, the second low temperature side expansion device 27 decompresses the refrigerant, Since the low temperature side expansion device 23 is fully opened and controlled so as not to reduce the pressure, the first low temperature side expansion device is located near the low temperature side evaporator 24 in the initial stage of the defrosting operation. By performing the pressure reducing operation, the heat exchange efficiency between the frost and the low-temperature side refrigerant in the low-temperature side evaporator 24 can be increased, and the defrosting operation time can be shortened. Further, similarly to the refrigeration apparatus of the first embodiment, an abnormal increase in the pressure of the low-temperature side refrigerant having a low critical temperature or the like is suppressed, and the defrosting operation is reliably stopped without stopping abnormally. Driving can be performed in a short time. Further, the cooling operation can be restarted without damaging the low temperature side compressor 21.

Embodiment 4 FIG.
FIG. 7 is a diagram showing a configuration of a binary refrigeration apparatus in Embodiment 4 of the present invention. In FIG. 7, devices and the like having the same reference numerals as those in FIG. 1 perform the same operations and the like as described in the first embodiment. In FIG. 7, an intermediate cooler 28 having a heat storage agent (hereinafter referred to as an intermediate cooler 28 with a heat storage agent) is provided as a substitute for the low temperature side intermediate cooler 26. The intercooler 28 with a heat storage agent can perform heat absorption / dissipation by heat exchange between the heat storage agent and the low-temperature side refrigerant, for example, instead of air supplied from a blower or the like (not shown). In the cooling operation, the amount of heat is stored by absorbing heat from the low-temperature side refrigerant, and assistance related to condensation of the low-temperature side refrigerant is performed. In the defrosting operation, the amount of heat is supplied (dissipated) to the low-temperature side refrigerant to evaporate the low-temperature side refrigerant. Here, for example, water or the like can be used as the heat storage agent.

  In the above-described embodiment, the low temperature side intercooler 26 exchanges heat between air supplied from a blower or the like (not shown) and the low temperature side refrigerant. In such a case, for example, when the temperature of the air is low, the heat exchange efficiency may be deteriorated, which may be affected by the operating environment. Therefore, in the present embodiment, by using the intercooler 28 with a heat storage agent, it is possible to stably cool the low-temperature side refrigerant (including condensation liquefaction) in the cooling operation and evaporate gasification in the defrosting operation. Is.

  Next, operation | movement of each component apparatus at the time of the cooling operation of a binary refrigeration apparatus is demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG. On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. The low temperature side compressor 21 sucks the low temperature side refrigerant, compresses the refrigerant, discharges it in a high temperature / high pressure state (compression process from point C to point D in FIG. 2). The discharged refrigerant flows into the intercooler 28 with a heat storage agent via the low temperature side four-way valve 25. At this time, the low temperature side four-way valve 25 is switched so that the low temperature side refrigerant is in a positive cycle.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent (for example, water, etc.) and refrigerant inside, and assists the low temperature side condenser 22 to condense and liquefy the low temperature side refrigerant. Here, in the intercooler 28 with a heat storage agent, the low temperature side refrigerant is not necessarily condensed and liquefied, but at least the heat (sensible heat) is taken from the low temperature side refrigerant so that the low temperature side refrigerant is kept constant. It is made to cool to temperature (condensing process from D point to E point in FIG. 2). Thereby, it becomes possible to improve cooling operation efficiency as the whole apparatus.

  On the other hand, the heat storage agent of the intercooler 28 with a heat storage agent removes heat from the low-temperature side refrigerant, thereby increasing the temperature and storing a predetermined amount of heat. The low temperature side cycle 20 of the binary refrigeration apparatus can perform a cooling operation under relatively stable high pressure conditions even in an environment where the outside air temperature is low such as in winter. For this reason, it is suitable for storing the thermal energy of the low-temperature side refrigerant. The operations of the low temperature side condenser 22, the first low temperature side expansion device 23, and the low temperature side evaporator 24 are the same as those described in the first embodiment.

  As described above, in the binary refrigeration apparatus, when the operation in which the evaporation temperature of the low temperature side evaporator 24 is negative (below zero) is continued, the low temperature side evaporator 24 is frosted and the refrigerating capacity is reduced. Therefore, the defrosting operation is performed every predetermined time, and the low temperature side evaporator 24 is defrosted.

  Next, the operation | movement of each component apparatus at the time of the defrosting operation | movement of a binary refrigeration apparatus is demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG. On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. Here, the low-temperature side refrigerant discharges the low-temperature side compressor 21, passes through the low-temperature side four-way valve 25, the low-temperature side evaporator 24, the first low-temperature side expansion device 23, and the low-temperature side condenser 22 and passes through the second low-temperature side refrigerant. The operation of each device up to the side diaphragm device 27 is the same as in the first embodiment.

  The second low temperature side expansion device 27 depressurizes the condensed low temperature side refrigerant (expansion step from point F to point G in FIG. 4). The decompressed low-temperature side refrigerant flows into the intercooler 28 with a heat storage agent.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent and the low-temperature side refrigerant contained therein, and evaporates and gasifies the low-temperature side refrigerant. And the low temperature side refrigerant | coolant which flowed out the intercooler 28 with a thermal storage agent passes along the low temperature side four-way valve 25, and is suck | inhaled by the high temperature side compressor 11 (evaporation process from G point to C point in FIG. 4).

  At this time, since the predetermined amount of heat stored in the heat storage agent during the cooling operation is radiated to the low-temperature side refrigerant and the low-temperature side refrigerant is evaporated, the predetermined amount of heat can be stably supplied even in low outside air conditions such as in winter. It can be supplied to the low temperature side refrigerant. For this reason, it is possible to operate at a higher evaporation temperature, and to efficiently increase the refrigerant circulation rate. As a result, reliable and reliable defrosting operation can be performed more efficiently and in a shorter time without abnormally stopping the defrosting operation, and it can contribute to energy saving. Here, when the second low temperature side expansion device 27 is, for example, an electronic expansion valve, the control means 40 has a superheat degree (4 to 10 K) that requires the low temperature side refrigerant flowing out from the intercooler 28 with a heat storage agent. In this way, the second low temperature side expansion device 27 is caused to adjust the opening degree.

  As described above, according to the binary refrigeration apparatus of the fourth embodiment, since the intermediate cooler is the intermediate cooler 28 with a heat storage agent, for example, without being affected by the operating environment such as outside air, Cooling (including condensation liquefaction) of the low-temperature side refrigerant in the cooling operation and evaporative gasification in the defrosting operation can be performed stably. Further, similarly to the refrigeration apparatus of the first embodiment, an abnormal increase in the pressure of the low-temperature side refrigerant having a low critical temperature or the like is suppressed, and the defrosting operation is reliably stopped without stopping abnormally. Driving can be performed in a short time. Further, the cooling operation can be restarted without damaging the low temperature side compressor 21.

Embodiment 5 FIG.
FIG. 8 is a diagram showing the configuration of the binary refrigeration apparatus in Embodiment 5 of the present invention. In FIG. 8, the same reference numerals as those in FIG. 1, FIG. 7, etc. perform the same operations as those described in the first embodiment. In the binary refrigeration apparatus of the present embodiment, as shown in FIG. 8, both the low temperature side intercooler 26 described in the first embodiment and the intermediate cooler 28 with a heat storage agent described in the fourth embodiment are used. Provided and connected in series in the low temperature side circulation circuit.

  Further, the binary refrigeration apparatus of the present embodiment has an open / close valve 29. A bypass pipe is provided in parallel with the intermediate cooler 28 with a heat storage agent, and by opening and closing the on-off valve 29, the low-temperature side refrigerant is passed through the intermediate cooler 28 with a heat storage agent, or the low-temperature side refrigerant is also passed through the bypass pipe. Can be selected. Although not specifically shown in FIG. 8, for example, it is selected whether or not the low-temperature side refrigerant is allowed to pass through the intercooler 28 with a heat storage agent, and an on-off valve or the like that can switch the flow path is provided as an intercooler with a heat storage agent. You may make it provide in the 28th flow path.

  Next, operation | movement of each component apparatus etc. at the time of the cooling operation of the binary refrigeration apparatus in this Embodiment are demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG.

  On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. The low temperature side compressor 21 sucks the low temperature side refrigerant, compresses the refrigerant, discharges it in a high temperature / high pressure state (compression process from point C to point D in FIG. 2). The discharged refrigerant flows into the intermediate cooler 28 with a heat storage agent via the low temperature side four-way valve 25 and the low temperature side intermediate cooler 26. At this time, the low temperature side four-way valve 25 is switched so that the low temperature side refrigerant is in a positive cycle. Further, the on-off valve 29 is closed so that the discharged refrigerant flows into the intercooler 28 with a heat storage agent so that the low temperature side refrigerant does not pass through the bypass pipe. And the air blower etc. which supply air etc. to the low temperature side intercooler 26 are stopped.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent (for example, water, etc.) and refrigerant inside, and assists the low temperature side condenser 22 to condense and liquefy the low temperature side refrigerant. Here, in the intercooler 28 with a heat storage agent, the low temperature side refrigerant is not necessarily condensed and liquefied, but at least the heat (sensible heat) is taken from the low temperature side refrigerant so that the low temperature side refrigerant is kept constant. It is made to cool to temperature (condensing process from D point to E point in FIG. 2). Thereby, it becomes possible to improve cooling operation efficiency as the whole apparatus.

  Here, the heat storage agent of the intercooler 28 with the heat storage agent takes heat from the low-temperature side refrigerant so that the temperature rises and a predetermined amount of heat is stored. The low temperature side cycle 20 of the binary refrigeration apparatus can perform a cooling operation under relatively stable high pressure conditions even in an environment where the outside air temperature is low such as in winter. For this reason, it is suitable for storing the thermal energy of the low-temperature side refrigerant.

  For example, when it is determined that a predetermined amount of time has elapsed from the start of the cooling operation and a predetermined amount of heat is stored in the heat storage agent of the intercooler 28 with a heat storage agent, the control means 40 opens the on-off valve 29 and the bypass pipe is also cooled to a low temperature. Let the side refrigerant pass. Further, the air blower or the like is driven to supply air or the like to the low temperature side intercooler 26. Thereby, the intercooler 28 with a heat storage agent and the low-temperature side intercooler 26 assist the condensation of the low-temperature side refrigerant.

  FIG. 9 is a view showing a flowchart of operation control of the dual refrigeration apparatus performed by the control means 40 according to the fifth embodiment. About the process of S31, S32, the process similar to the process of S1, S2 of FIG. 3 demonstrated in Embodiment 1 is performed.

  And it is judged whether the calorie | heat amount in the heat storage agent of the intercooler 28 with a heat storage agent is less than predetermined | prescribed heat amount (S33). If it is determined that the amount of heat is less than the predetermined amount of heat, the control means 40 closes the on-off valve 29 and stops the blower that supplies air or the like to the low temperature side intercooler 26 (S34). On the other hand, if it is determined that the amount of heat is not less than the predetermined amount of heat (is greater than or equal to the predetermined amount of heat), the on-off valve is opened and the blower or the like is driven to supply air or the like to the low temperature side intercooler 26 (S35). . Here, how to determine whether the heat quantity is less than a predetermined heat quantity is not particularly limited. For example, the determination may be made based on the cooling operation time. Moreover, the temperature detection means for detecting the temperature of the heat storage agent may be provided, and the amount of heat of the heat storage agent may be determined based on the temperature detected by the temperature detection means. The operations of the low temperature side condenser 22, the first low temperature side expansion device 23, and the low temperature side evaporator 24 are the same as those described in the first embodiment.

  As described above, in the binary refrigeration apparatus, when the operation in which the evaporation temperature of the low temperature side evaporator 24 is negative (below zero) is continued, the low temperature side evaporator 24 is frosted and the refrigerating capacity is reduced. Therefore, as shown in the flowchart of FIG. 9, the defrosting operation is performed every predetermined time, and the low temperature side evaporator 24 is defrosted (S36).

  Next, the operation | movement of each component apparatus at the time of the defrosting operation | movement of a binary refrigeration apparatus is demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG. On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. Here, the low-temperature side refrigerant discharges the low-temperature side compressor 21, passes through the low-temperature side four-way valve 25, the low-temperature side evaporator 24, the first low-temperature side expansion device 23, and the low-temperature side condenser 22 and passes through the second low-temperature side refrigerant. The operation of each device up to the side diaphragm device 27 is the same as in the first embodiment. Here, the on-off valve 29 is closed.

  The second low temperature side expansion device 27 depressurizes the condensed low temperature side refrigerant (expansion step from point F to point G in FIG. 4). The decompressed low-temperature side refrigerant flows into the intercooler 28 with a heat storage agent because the on-off valve 29 is closed.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent and the low-temperature side refrigerant contained therein, and evaporates and gasifies the low-temperature side refrigerant. And the low temperature side refrigerant | coolant which flowed out the intercooler 28 with a thermal storage agent passes along the low temperature side four-way valve 25, and is suck | inhaled by the high temperature side compressor 11 (evaporation process from G point to C point in FIG. 4).

  At this time, since the predetermined amount of heat stored in the heat storage agent during the cooling operation is radiated to the low-temperature side refrigerant and the low-temperature side refrigerant is evaporated, the predetermined amount of heat can be stably supplied even in low outside air conditions such as in winter. It can be supplied to the low temperature side refrigerant. For this reason, it is possible to operate at a higher evaporation temperature, and to efficiently increase the refrigerant circulation rate. As a result, reliable and reliable defrosting operation can be performed more efficiently and in a shorter time without abnormally stopping the defrosting operation, and it can contribute to energy saving.

  In the flowchart shown in FIG. 9, the processing of S37 to S41 is basically the same as the processing of S14 to S18 of FIG. 5 described in the second embodiment. Here, in S37, the on-off valve 29 is closed as described above so that the low-temperature side refrigerant flows into the intercooler 28 with a heat storage agent. In S38, the opening degree of the first low temperature side expansion device 23 and the second low temperature side expansion device 27 is changed after a predetermined time has elapsed since the start of the defrosting operation, as in S25 of the third embodiment. You may make it do.

  As described above, according to the binary refrigeration apparatus of the fifth embodiment, the low temperature side intercooler 26 and the intercooler 28 with a heat storage agent are connected in series by piping. Without being affected by the environment, it is possible to stably cool the low-temperature side refrigerant (including condensate liquefaction) in the cooling operation and evaporate gasification in the defrosting operation. Further, by providing the low temperature side intercooler 26 and the intercooler 28 with the heat storage agent, the heat storage agent in the intercooler 28 with the heat storage agent can be optimally designed to the minimum necessary. The space can be saved as a whole. As in the refrigeration apparatus of the first embodiment, it is possible to suppress an abnormal increase in the pressure of the low-temperature side refrigerant having a low critical temperature or the like, and to reliably and reliably perform the defrosting without stopping the defrosting operation abnormally. Driving can be performed in a short time. Further, the cooling operation can be restarted without damaging the low temperature side compressor 21.

Embodiment 6 FIG.
FIG. 10 is a diagram showing the configuration of the binary refrigeration apparatus in Embodiment 6 of the present invention. 10, devices described with the same reference numerals as those in FIGS. 1 and 8 perform the operations described in the above embodiments. In the binary refrigeration apparatus of the present embodiment, the low temperature side intercooler 26 and the intercooler 28 with a heat storage agent are connected in parallel. Further, the open / close valve 29 is provided in series with the low temperature side condenser 22 on the low temperature side intermediate cooler 26 side of the low temperature side condenser 22 (the refrigerant downstream side in the cooling operation). Here, the on-off valve 29 is provided on the low temperature side intercooler 26 side. However, for example, an on-off valve may be provided on the intermediate cooler 28 side with a heat storage agent to switch the flow path.

  Next, operation | movement of each component apparatus etc. at the time of the cooling operation of the binary refrigeration apparatus in this Embodiment are demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG.

  On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. The low temperature side compressor 21 sucks the low temperature side refrigerant, compresses the refrigerant, discharges it in a high temperature / high pressure state (compression process from point C to point D in FIG. 2). The discharged refrigerant flows into the intermediate cooler 28 with a heat storage agent via the low temperature side four-way valve 25 and the low temperature side intermediate cooler 26. At this time, the low temperature side four-way valve 25 is switched so that the low temperature side refrigerant is in a positive cycle. In addition, the on-off valve is closed so that the discharged refrigerant flows into the intercooler 28 with a heat storage agent so that the low-temperature side refrigerant does not pass through the bypass pipe. And the air blower etc. which supply air etc. to the low temperature side intercooler 26 are stopped.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent (for example, water, etc.) and refrigerant inside, and assists the low temperature side condenser 22 to condense and liquefy the low temperature side refrigerant. Here, in the intercooler 28 with a heat storage agent, the low temperature side refrigerant is not necessarily condensed and liquefied, but at least the heat (sensible heat) is taken from the low temperature side refrigerant so that the low temperature side refrigerant is kept constant. It is made to cool to temperature (condensing process from D point to E point in FIG. 2). Thereby, it becomes possible to improve cooling operation efficiency as the whole apparatus.

  Here, the heat storage agent of the intercooler 28 with the heat storage agent takes heat from the low-temperature side refrigerant so that the temperature rises and a predetermined amount of heat is stored. The low temperature side cycle 20 of the binary refrigeration apparatus can perform a cooling operation under relatively stable high pressure conditions even in an environment where the outside air temperature is low such as in winter. For this reason, it is suitable for storing the thermal energy of the low-temperature side refrigerant.

  For example, when it is determined that a predetermined amount of time has elapsed from the start of the cooling operation and a predetermined amount of heat has been stored in the heat storage agent of the intercooler 28 with a heat storage agent, the control means 40 opens the on-off valve 29 and opens the bypass pipe to the low temperature side. Allow the refrigerant to pass through. Further, the air blower or the like is driven to supply air or the like to the low temperature side intercooler 26. Thereby, instead of the intercooler 28 with a heat storage agent, the low temperature side intercooler 26 assists to condense and liquefy the low temperature side refrigerant. Control in the cooling operation of the binary refrigeration apparatus performed by the control means 40 is the same as S31 to S35 in FIG.

  Next, the operation | movement of each component apparatus at the time of the defrosting operation | movement of a binary refrigeration apparatus is demonstrated. About the operation | movement at the time of cooling operation of the high temperature side cycle 10, it is the same as the operation | movement demonstrated in Embodiment 1. FIG. On the other hand, the operation of the low temperature side cycle 20 will be described with reference to FIGS. Here, the low-temperature side refrigerant discharges the low-temperature side compressor 21, passes through the low-temperature side four-way valve 25, the low-temperature side evaporator 24, the first low-temperature side expansion device 23, and the low-temperature side condenser 22 and passes through the second low-temperature side refrigerant. The operation of each device up to the side diaphragm device 27 is the same as in the first embodiment. Here, the on-off valve 29 is closed.

  The second low temperature side expansion device 27 depressurizes the condensed low temperature side refrigerant (expansion step from point F to point G in FIG. 4). The decompressed low-temperature side refrigerant flows into the intercooler 28 with a heat storage agent because the on-off valve 29 is closed.

  The intercooler 28 with a heat storage agent exchanges heat between the heat storage agent and the low-temperature side refrigerant contained therein, and evaporates and gasifies the low-temperature side refrigerant. And the low temperature side refrigerant | coolant which flowed out the intercooler 28 with a thermal storage agent passes along the low temperature side four-way valve 25, and is suck | inhaled by the high temperature side compressor 11 (evaporation process from G point to C point in FIG. 4).

  At this time, since the predetermined amount of heat stored in the heat storage agent during the cooling operation is radiated to the low-temperature side refrigerant and the low-temperature side refrigerant is evaporated, the predetermined amount of heat can be stably supplied even in low outside air conditions such as in winter. It can be supplied to the low temperature side refrigerant. For this reason, it is possible to operate at a higher evaporation temperature, and to efficiently increase the refrigerant circulation rate. As a result, reliable and reliable defrosting operation can be performed more efficiently and in a shorter time without abnormally stopping the defrosting operation, and it can contribute to energy saving. Control in the defrosting operation of the dual refrigeration apparatus performed by the control means 40 is the same as S36 to S41 in FIG.

  As described above, according to the binary refrigeration apparatus of the sixth embodiment, the low-temperature side intercooler 26 and the intercooler 28 with a heat storage agent are connected in parallel to each other. Without being affected by the environment, it is possible to stably cool the low-temperature side refrigerant (including condensate liquefaction) in the cooling operation and evaporate gasification in the defrosting operation. Further, by providing the low temperature side intercooler 26 and the intercooler 28 with the heat storage agent, the heat storage agent in the intercooler 28 with the heat storage agent can be optimally designed to the minimum necessary. The space can be saved as a whole. As in the refrigeration apparatus of the first embodiment, it is possible to suppress an abnormal increase in the pressure of the low-temperature side refrigerant having a low critical temperature or the like, and to reliably and reliably perform the defrosting without stopping the defrosting operation abnormally. Driving can be performed in a short time. Further, the cooling operation can be restarted without damaging the low temperature side compressor 21.

  Although the above-described embodiment has been described with respect to a binary refrigeration apparatus, it can also be applied to a multi-stage refrigeration apparatus having a multi-stage configuration. Further, the present invention can be applied not only to a binary refrigeration apparatus but also to a refrigeration apparatus that performs cooling or the like using carbon dioxide as a refrigerant.

  DESCRIPTION OF SYMBOLS 10 High temperature side cycle, 11 High temperature side compressor, 12 High temperature side condenser, 13 High temperature side expansion device, 14 High temperature side evaporator, 20 Low temperature side cycle, 21 Low temperature side compressor, 22 Low temperature side condenser, 23 1st Low temperature side throttle device, 24 Low temperature side evaporator, 25 Low temperature side four-way valve, 26 Low temperature side intercooler, 27 Second low temperature side throttle device, 28 Intermediate cooler with heat storage agent, 29 On-off valve, 30 Cascade condenser, 40 Control means, 51 evaporator temperature sensor, 52 discharge side pressure sensor.

Claims (7)

A high-temperature side cycle device that forms a high-temperature-side circulation circuit that circulates the high-temperature-side refrigerant by pipe-connecting the high-temperature side compressor, the high-temperature side condenser, the high-temperature side expansion device, and the high-temperature side evaporator;
The low temperature side compressor, the intercooler, the low temperature side condenser, the first low temperature side expansion device, and the low temperature side evaporator are connected to form a low temperature side circulation circuit for circulating the low temperature side refrigerant. A flow path switching device for switching the flow of refrigerant in the circuit, and a low temperature side cycle device further having a second low temperature side expansion device between the intermediate cooler and the low temperature side condenser;
A cascade capacitor configured by the high temperature side evaporator and the low temperature side condenser, and performing heat exchange between the high temperature side refrigerant and the low temperature side refrigerant ,
In the defrosting operation of the low-temperature evaporator performed by switching the refrigerant flow by the flow path switching device, the low-temperature refrigerant is condensed by the low-temperature evaporator and the low-temperature condenser, and the second low-temperature refrigerant is condensed. A refrigeration apparatus comprising: control means for controlling the decompression of the low temperature side refrigerant in the side expansion device so that the low temperature side refrigerant is evaporated in the intermediate cooler . The control means includes
In the defrosting operation, when the discharge pressure of the low temperature side compressor in the low temperature side cycle device is determined to be equal to or higher than a predetermined pressure, the first low temperature side expansion device is opened, and the second low temperature side expansion device is the low-temperature-side refrigerant by decompression so as to condense the low-temperature-side refrigerant in the low-temperature side condenser refrigeration system of claim 1, wherein the performing control for operating the high-temperature side cycle apparatus. The control means includes
When it is determined that the treatment time has elapsed from the start of the defrosting operation, the first low-temperature side expansion device is opened, the low-temperature side refrigerant is decompressed by the second low-temperature side expansion device, and the low-temperature side condenser the so as to condense the low temperature side refrigerant, the refrigeration apparatus of claim 1, wherein the performing control for operating the high-temperature side cycle apparatus. The intermediate cooler, the refrigerating apparatus according to any one of claims 1 to 3, characterized in that it has a heat storage agent to the low-temperature-side refrigerant and the heat exchanger. 2. The intermediate cooler is constituted by connecting an intermediate cooler having a heat storage agent and an intermediate cooler not having a heat storage agent by pipe connection in series to the high-temperature side circulation circuit. The refrigeration apparatus according to any one of to 3 . 2. The intermediate cooler is configured by connecting an intermediate cooler having a heat storage agent and an intermediate cooler not having a heat storage agent in parallel to the high temperature side circulation circuit. The refrigeration apparatus according to any one of to 3 . The refrigeration apparatus according to any one of claims 1 to 6 , wherein carbon dioxide is used as the low temperature side refrigerant.

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