Abstract: A liquid temperature control apparatus including a heat medium circulation apparatus equipped with a cooling unit having a compressor, a condenser, an expansion valve, and a plurality of cooling heat exchangers, and equipped with a heating unit configured to allow a portion of a heat medium flowing out from the compressor toward the condenser to be branched and return the portion of the heat medium to flow into the condenser on the downstream side of the compressor via a heating heat exchanger and a heating amount adjustment valve; and a liquid flow apparatus. A first liquid flow path of the liquid flow apparatus is connected to the first cooling heat exchanger and to the heating heat exchanger. A second liquid flow path is connected to the second cooling heat exchanger. Moreover, an electric heater for heating the liquid allowed to flow is provided in the second liquid flow path.

Abstract: Provided are a three-way valve for flow rate control and a temperature control device using the three-way valve for flow rate control. The three-way valve for flow rate control is capable of controlling a mixture ratio between two kinds of fluids with higher accuracy, as compared to a three-way valve including an inflow port which allows inflow of a high-temperature heat-medium circulating liquid, an inflow port which allows inflow of a low-temperature heat-medium circulating liquid, an outflow port which allows outflow of a constant-temperature heat-medium circulating liquid, and a control valve configured to control the flow rate ratio between the high-temperature heat-medium circulating liquid and the low-temperature heat-medium circulating liquid.

Abstract: The present invention is a hydrogen cooling apparatus comprising: a air-cooled condenser disposed on a part of a first coolant passage so as to enable cooling of a first coolant by driving an air-cooling fan; a first heat exchanger enabling cooling of a second coolant by the first coolant, between another part of the first coolant passage and a part of a second coolant passage; and a second heat exchanger enabling cooling of hydrogen by the second coolant, between another part of the second coolant passage and a part of a hydrogen passage. A driving rotational speed of the air-cooling fan is inverter controlled in such a manner that a pressure of the first coolant from the air-cooled condenser to the first heat exchanger is maintained between 1.5 MPa and 1.7 MPa.

Abstract: A temperature control system includes first and second temperature control devices. In the first temperature control device, a refrigeration circuit of a refrigeration device, which is positioned downstream of an expansion valve and upstream of an evaporator, and a brine circulation path of a brine circulation device, which is positioned on a heating unit, constitutes a refrigeration capacity adjustment mechanism, and cooling is performed by the evaporator of the refrigeration circuit. In the second temperature control device, a refrigeration device includes an injection circuit that bypasses a condensed refrigerant upstream of a compressor, and a hot gas circuit that bypasses a compressed high-temperature refrigerant upstream of a compressor. A part of the brine circulation path of the brine circulation device and an evaporator of the refrigeration device constitute a heating capacity adjustment heat exchanger, and heating or cooling is performed by a load unit of the brine circulation path.

Abstract: Provided are a three-way valve for flow rate control and a temperature control device using the three-way valve for flow rate control. The three-way valve for flow rate control is capable of controlling a mixture ratio between two kinds of fluids with higher accuracy, as compared to a three-way valve including an inflow port which allows inflow of a high-temperature heat-medium circulating liquid, an inflow port which allows inflow of a low-temperature heat-medium circulating liquid, an outflow port which allows outflow of a constant-temperature heat-medium circulating liquid, and a control valve configured to control the flow rate ratio between the high-temperature heat-medium circulating liquid and the low-temperature heat-medium circulating liquid.

Abstract: An air conditioner includes: a duct including an upstream flow path unit having an inlet through which air is taken in, and a downstream flow path unit provided with an outlet through which the air is discharged; a cooling unit positioned in the upstream flow path unit of the duct and cools the air; and a heating unit that is positioned in the downstream flow path unit of the duct and heats the air. The upstream flow path unit has a partition plate that partitions an inside space thereof into a main-flow flow path and a sub-flow flow path. The cooing unit is positioned in the main-flow flow path. The upstream flow path unit is provided with a flowrate adjusting member that covers at least a part of the sub-flow flow path so as to adjust an opening area of the sub-flow flow path.

Abstract: An air conditioner includes: a cooling unit having a compressor operated at a variable operating frequency to adjust a revolving speed thereof, a condenser, an expansion valve and a cooling coil; and a heating unit for causing the heating medium flowing from the compressor toward the condenser to diverge, and to return to flow into the condenser, through a heating coil and a thermal dose adjusting valve disposed on the downstream side thereof; so as to control a temperature of air by the cooling and heating coils. When an opening manipulated variable of the thermal dose adjusting valve exceeds a first threshold value over a period of time, an operating frequency of the compressor is decreased, and when the opening manipulated variable of the thermal dose adjusting valve falls below a smaller, second threshold value, over the said period of time, the operating frequency of the compressor is increased.

Abstract: A liquid temperature control apparatus including a heat medium circulation apparatus equipped with a cooling unit having a compressor, a condenser, an expansion valve, and a plurality of cooling heat exchangers, and equipped with a heating unit configured to allow a portion of a heat medium flowing out from the compressor toward the condenser to be branched and return the portion of the heat medium to flow into the condenser on the downstream side of the compressor via a heating heat exchanger and a heating amount adjustment valve; and a liquid flow apparatus. A first liquid flow path of the liquid flow apparatus is connected to the first cooling heat exchanger and to the heating heat exchanger. A second liquid flow path is connected to the second cooling heat exchanger. Moreover, an electric heater for heating the liquid allowed to flow is provided in the second liquid flow path.

Abstract: An environmental testing apparatus includes a chamber, a cooling unit including a cooling apparatus of a brine that cools the inside of the chamber, a heating unit and a control apparatus. The cooling apparatus includes: a high temperature side cooling circuit including a high temperature side compressor, condenser, high temperature side expansion valve and cascade condenser connected in this order to circulate a high temperature side heating medium; and a low temperature side cooling circuit including a low temperature side compressor, cascade condenser, low temperature side expansion valve and evaporator connected in this order to circulate a low temperature side heating medium. The low temperature side heating medium is cooled by the high temperature side heating medium in the cascade condenser, while the brine is cooled by the low temperature side heating medium in the evaporator. The control apparatus controls a temperature inside the chamber to between ?67.5° C. and 127.5° C.

Abstract: In the present chiller apparatus, a refrigerant flow path is branchably attached to a lower electrode serving as a large sample table, which copes with a case where the surface area of a sample is large in a configuration in which a plasma treatment device connected to a refrigerant cycle equipped with a heating device is applied. A control device transmits a heating adjustment control signal generated based on a result of a PID arithmetic operation including proportion, integration, and differentiation on a lower electrode refrigerant pipe refrigerant detection temperature detected from a temperature sensor provided in the vicinity of a refrigerant flow path of a heat insulating portion relative to the lower electrode of a lower electrode refrigerant pipe connected to be linked to the refrigerant cycle to a heating device and performs feedback control such that the lower electrode refrigerant pipe refrigerant detection temperature becomes a setting temperature.

Abstract: A temperature control apparatus is provided, which is capable of, even when it is necessary to perform control by means of valves in a plurality of channels, promptly controlling a temperature of an area to be temperature-controlled promptly to a desired temperature, while avoiding complication and enlargement of the apparatus as a whole. Passage and blockage of a heating medium passing through a first supply channel to a mixing channel, a temperature of the heating medium being controlled by a first temperature regulating unit at a predetermined temperature, and passage and blockage of a heating medium passing through a second supply channel to the mixing channel, a temperature of the heating medium being controlled by a second temperature regulating unit, are controlled by a valve unit. The valve unit includes a first spool valve and a second spool valve, which are coupled through a heat insulating layer.

Abstract: Chiller apparatus performs temperature-control operation without placing excessive load on an electric compressor even when temperature difference between set and work temperatures are small; little temperature difference between refrigerant intake side and refrigerant discharge side of an evaporator in freezing-cycle, at time of temperature-control setting with small temperature difference between set and work temperatures; PCB2 performs PID operation on refrigerant detection temperature by sensor near the side of refrigerant inflow of a heating apparatus in a refrigerant-cycle; a PCB1 performs serial communication of a drive control signal for an inverter generated based on a result, and controls the compressor rotational speed according to work temperature within range.

Abstract: A cooled-hydrogen supply station includes: a first coolant passage through which a first coolant circulates; a water-cooled refrigerator unit disposed on a part of the first coolant passage to cool the first coolant; a second coolant passage through which a second coolant flows; a first heat exchanger for cooling the second coolant by the first coolant, between another part of the first coolant passage and a part of the second coolant passage; a hydrogen storage unit; a hydrogen passage for transporting hydrogen stored in the hydrogen storage unit; and a second heat exchanger for cooling the hydrogen by the second coolant, between another part of the second coolant passage and a part of the hydrogen passage. The hydrogen is cooled down to a temperature of ?43° C. to ?20° C. by the second heat exchanger, and a hydrogen cooling power for cooling hydrogen to ?40° C. is between 13.5 kW and 16.5 kW.

Abstract: An air conditioning method that reduces the amount of cooling energy and the amount of dehumidification energy to approximately a limiting amount, and also reduces the amount of humidifying energy to approximately a limiting amount. If an absolute humidity of the process air is calculated by use of measurements of changes in work conditions and variations in atmospheric pressure, the required amount of air to be cooled and dehumidified flowing downstream through the main-stream duct and the required amount of humidification can be determined. Therefore, by outputting a signal indicative of the required amount of cooled-dehumidified air to actuate a controller of flow-rate regulating means, and outputting a signal indicative of the required amount of humidification to actuate a controller of humidifying means, the amount of air to be cooled and dehumidified can be reduced to the required amount of cooled-dehumidified air close to the limiting amount.

Abstract: Chiller apparatus performs temperature-control operation without placing excessive load on an electric compressor even when temperature difference between set and work temperatures are small; little temperature difference between refrigerant intake side and refrigerant discharge side of an evaporator in freezing-cycle, at time of temperature-control setting with small temperature difference between set and work temperatures; PCB2 performs PID operation on refrigerant detection temperature by sensor near the side of refrigerant inflow of a heating apparatus in a refrigerant-cycle; a PCB1 performs serial communication of a drive control signal for an inverter generated based on a result, and controls the compressor rotational speed according to work temperature within range.

Abstract: A cooled-hydrogen supply station includes: a first coolant passage through which a first coolant circulates; a water-cooled refrigerator unit disposed on a part of the first coolant passage to cool the first coolant; a second coolant passage through which a second coolant flows; a first heat exchanger for cooling the second coolant by the first coolant, between another part of the first coolant passage and a part of the second coolant passage; a hydrogen storage unit; a hydrogen passage for transporting hydrogen stored in the hydrogen storage unit; and a second heat exchanger for cooling the hydrogen by the second coolant, between another part of the second coolant passage and a part of the hydrogen passage. The hydrogen is cooled down to a temperature of ?43° C. to ?20° C. by the second heat exchanger, and a hydrogen cooling power for cooling hydrogen to ?40° C. is between 13.5 kW and 16.5 kW.

Abstract: An air conditioning method that reduces the amount of cooling energy and the amount of dehumidification energy to approximately a limiting amount, and also reduces the amount of humidifying energy to approximately a limiting amount. If an absolute humidity of the process air is calculated by use of measurements of changes in work conditions and variations in atmospheric pressure, the required amount of air to be cooled and dehumidified flowing downstream through the main-stream duct and the required amount of humidification can be determined. Therefore, by outputting a signal indicative of the required amount of cooled-dehumidified air to actuate a controller of flow-rate regulating means, and outputting a signal indicative of the required amount of humidification to actuate a controller of humidifying means, the amount of air to be cooled and dehumidified can be reduced to the required amount of cooled-dehumidified air close to the limiting amount.