JP4712910B1 - Precision air conditioner - Google Patents

Precision air conditioner Download PDF

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JP4712910B1
JP4712910B1 JP2010291585A JP2010291585A JP4712910B1 JP 4712910 B1 JP4712910 B1 JP 4712910B1 JP 2010291585 A JP2010291585 A JP 2010291585A JP 2010291585 A JP2010291585 A JP 2010291585A JP 4712910 B1 JP4712910 B1 JP 4712910B1
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evaporator
air
condenser
pressure
temperature
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JP2012137271A (en
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克昌 藤井
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Asahi Kogyosha Co Ltd
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Asahi Kogyosha Co Ltd
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Priority to JP2010291585A priority Critical patent/JP4712910B1/en
Priority to CN201180002373.7A priority patent/CN102803858B/en
Priority to KR1020117028332A priority patent/KR101272088B1/en
Priority to PCT/JP2011/050173 priority patent/WO2012090511A1/en
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Priority to TW100126994A priority patent/TWI431230B/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F1/00Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
    • F24F1/02Self-contained room units for air-conditioning, i.e. with all apparatus for treatment installed in a common casing
    • F24F1/022Self-contained room units for air-conditioning, i.e. with all apparatus for treatment installed in a common casing comprising a compressor cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • F24F11/84Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers using valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/72Control systems characterised by their outputs; Constructional details thereof for controlling the supply of treated air, e.g. its pressure
    • F24F11/74Control systems characterised by their outputs; Constructional details thereof for controlling the supply of treated air, e.g. its pressure for controlling air flow rate or air velocity
    • F24F11/77Control systems characterised by their outputs; Constructional details thereof for controlling the supply of treated air, e.g. its pressure for controlling air flow rate or air velocity by controlling the speed of ventilators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F5/00Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
    • F24F5/0007Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/30Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2110/00Control inputs relating to air properties
    • F24F2110/10Temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2140/00Control inputs relating to system states
    • F24F2140/30Condensation of water from cooled air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/16Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by purification, e.g. by filtering; by sterilisation; by ozonisation
    • F24F3/167Clean rooms, i.e. enclosed spaces in which a uniform flow of filtered air is distributed

Abstract

【課題】冷凍サイクルの負荷を一定に保ちつつ制御対象の空調負荷に対応して排熱量を制御できる精密空調機を提供する。
【解決手段】クリーンルーム10に設置されたチャンバ12内の空気を導入し、これを設定温度にしてチャンバ12に循環する精密空調機において、圧縮機29の吐出側から吸込側にかけて、凝縮器31、膨張弁35、蒸発器26が順次接続されると共に、圧縮機29の吐出側のホットガスを蒸発器26に流すホットガスバイパス回路40を有する冷凍サイクル25と、冷凍サイクル25の蒸発器26が収容され、チャンバ12からの空気を導入し、蒸発器26で設定温度に空調してチャンバ12に循環する熱回収部28と、クリーンルーム10内に設けられると共に冷凍サイクル25の凝縮器31が収容され、かつその凝縮器31をクリーンルーム10内の空気で空冷する能力可変ファン32を備えた放熱部33とを備えたものである。
【選択図】図1
A precision air conditioner capable of controlling the amount of exhaust heat corresponding to the air conditioning load to be controlled while keeping the load of the refrigeration cycle constant.
In a precision air conditioner that introduces air in a chamber 12 installed in a clean room 10 and circulates the air in the chamber 12 at a set temperature, a condenser 31, from the discharge side to the suction side of a compressor 29, The expansion valve 35 and the evaporator 26 are sequentially connected, and the refrigeration cycle 25 having a hot gas bypass circuit 40 for flowing hot gas on the discharge side of the compressor 29 to the evaporator 26 and the evaporator 26 of the refrigeration cycle 25 are accommodated. A heat recovery unit 28 that introduces air from the chamber 12, air-conditions to a set temperature by the evaporator 26 and circulates to the chamber 12, and a condenser 31 of the refrigeration cycle 25 that is provided in the clean room 10 is accommodated, And the heat dissipation part 33 provided with the capability variable fan 32 which air-cools the condenser 31 with the air in the clean room 10 is provided.
[Selection] Figure 1

Description

本発明は、クリーンルーム内に設置された露光装置などを収容する空調対象であるチャンバに精密温調された空気を供給循環する精密空調機に関するものである。   The present invention relates to a precision air conditioner that supplies and circulates precisely temperature-controlled air to a chamber that is an air conditioning target that houses an exposure apparatus or the like installed in a clean room.

液晶ガラス基板の露光装置の周辺環境は、温度変化によりガラス基板が熱膨張するため、空調温度を精密(精度±0.01〜±0.1℃)にコントロールする必要がある。   In the surrounding environment of the exposure apparatus for the liquid crystal glass substrate, since the glass substrate thermally expands due to temperature change, it is necessary to accurately control the air conditioning temperature (accuracy ± 0.01 to ± 0.1 ° C.).

このような露光装置などは、クリーンルーム内に隔壁などで形成したチャンバ内に設置されおり、クリーンルーム用の空調機とは別の精密空調機をクリーンルームの床下に設置し、その精密空調機から空調対象であるチャンバに、精密温度制御された空調空気を供給循環するようにしている。   Such exposure equipment is installed in a chamber formed of partition walls in a clean room, and a precision air conditioner that is different from the clean room air conditioner is installed under the floor of the clean room. Is supplied and circulated to the chamber.

この精密空調機は、冷凍サイクルで構成され、チャンバからの空気を蒸発器で設定温度より低い温度(例えば17℃)に冷却され、これを再熱電気ヒータで設定温度(例えば23℃)に加熱し、空調空気としてチャンバに供給循環するようにしている。   This precision air conditioner is composed of a refrigeration cycle, and the air from the chamber is cooled to a temperature lower than a set temperature (for example, 17 ° C.) by an evaporator and heated to a set temperature (for example, 23 ° C.) by a reheat electric heater. The air is supplied and circulated to the chamber as conditioned air.

ここで、冷凍サイクルの蒸発器である吸熱部は、チャンバ内を空調するためにクリーンルーム内に設置されるが、放熱部となる凝縮器は、圧縮機と共に室外機としてクリーンルーム外に設置し、放熱部と室外機を冷媒配管で接続して空冷型空調機とされる。または放熱部となる凝縮器を水冷式としてクリーンルームの床下に設置する場合には、クリーンルーム外に冷却水供給装置を設置し、放熱部と冷却水供給装置とを水冷配管で接続した水冷式空調機とされるなど、種々のタイプが提案されている(特許文献1)。   Here, the heat absorption part, which is the evaporator of the refrigeration cycle, is installed in the clean room in order to air-condition the inside of the chamber, but the condenser as the heat radiation part is installed outside the clean room as an outdoor unit together with the compressor, and dissipates heat. The unit and the outdoor unit are connected by a refrigerant pipe to form an air-cooled air conditioner. Or, when installing a condenser that becomes a heat radiating unit under the floor of a clean room as a water-cooled type, a cooling water supply device is installed outside the clean room, and the heat radiating unit and the cooling water supply device are connected by water-cooled piping Various types have been proposed (Patent Document 1).

しかし、蒸発器で設定温度より低い温度に冷却した空調空気を再熱電気ヒータで、設定温度に加熱する精密温度制御は、電気ヒータのランニングコストが嵩む問題がある。   However, the precise temperature control in which the conditioned air cooled to a temperature lower than the set temperature by the evaporator is heated to the set temperature by the reheat electric heater has a problem that the running cost of the electric heater increases.

そこで、特許文献2に提案されるように冷凍サイクルのホットガスを利用し、これを蒸発器に流して蒸発温度を制御するホットガスバイパスに加えて、蒸発器の空気吹出側に別途再熱用凝縮器を設置してこの再熱用凝縮器にホットガスを流し、蒸発器で冷却された空気を、その再熱用凝縮器で加熱し、その後再熱電気ヒータで精密温度制御することが提案されている。   Therefore, as proposed in Patent Document 2, the hot gas of the refrigeration cycle is used, and this is supplied to the evaporator and added to the hot gas bypass for controlling the evaporation temperature. Proposed to install a condenser and to flow hot gas through the reheating condenser, to heat the air cooled by the evaporator with the reheating condenser and then to control the temperature precisely with the reheating electric heater. Has been.

この特許文献2では、蒸発器にホットガスを流して蒸発温度を制御し、再熱用凝縮器で空調空気を温度制御するため、再熱電気ヒータのランニングコストをある程度低減することができるが、ホットガスバイパスで、冷凍サイクルの凝縮温度や蒸発温度を、応答性よくしかも精密に制御することは、不可能であり、再熱電気ヒータの設置は不可欠である。   In Patent Document 2, the running temperature of the reheat electric heater can be reduced to some extent because the hot gas is flowed through the evaporator to control the evaporation temperature and the temperature of the conditioned air is controlled by the reheat condenser. It is impossible to precisely control the condensation temperature and evaporation temperature of the refrigeration cycle with hot gas bypass, and installation of a reheat electric heater is indispensable.

一方、特許文献3では、蒸発器の吹出側に再熱用凝縮器を設置し、ホットガスを、空気圧で作動する三方比例制御弁にて、ホットガスのバイパス量を制御することで、再熱用凝縮器で応答性のよい温度制御が実現でき、これにより再熱電気ヒータを不要とすることが提案されている。   On the other hand, in Patent Document 3, a reheat condenser is installed on the outlet side of the evaporator, and the hot gas is reheated by controlling the bypass amount of the hot gas with a three-way proportional control valve that operates pneumatically. It has been proposed that temperature control with good responsiveness can be realized with a condenser for use, thereby eliminating the need for a reheat electric heater.

この特許文献3は、チャンバからの空気を、蒸発器で設定温度より、5℃低い温度に冷却したのち再熱用凝縮器で設定温度に加熱するものであり、再熱電気ヒータが不要なため、ランニングコストを抑えることが可能となる。   In Patent Document 3, the air from the chamber is cooled to a temperature lower by 5 ° C. than the set temperature by the evaporator and then heated to the set temperature by the condenser for reheating, and a reheat electric heater is unnecessary. The running cost can be reduced.

特開2000−283500号公報JP 2000-283500 A 特開2009−216332号公報JP 2009-216332 A 特許第3283245号公報Japanese Patent No. 3283245

しかしながら、特許文献1〜3では、排熱回収用の凝縮器に冷却水を用いており、冷却水供給装置をクリーンルーム外に別途設置すると共に冷水配管で、冷却水供給装置と凝縮器側の放熱部とを接続する作業を必要とする。   However, in Patent Documents 1 to 3, cooling water is used for the condenser for exhaust heat recovery, and the cooling water supply device is separately installed outside the clean room and the cooling water pipe is used to radiate heat between the cooling water supply device and the condenser side. Work to connect the parts.

特に、最近のクリーンルームは大型化が進んでおり、露光装置などのプロセス機器が設置されるクリーンゾーンの高さは10m近くで、また床下のレターンチャンバの高さも5〜6m程度と高くなっており、しかもその延べ床面積も数万m2となっており、クリーンゾーン内には多数のプロセス機器を覆うチャンバが個々に設置されることになる。この各チャンバの熱を放熱する放熱部は、レターンチャンバに個々に設置され、他方クリーンルーム外には冷却水供給装置が設置されるため、この冷水供給装置と各放熱部とを接続する冷水配管は必然的に長くなると共に、接続には高所作業も必要とすると共に、冷水配管の保温や水漏れ対策など多大な労力を必要とする。 In particular, recent clean rooms are becoming larger in size, the height of the clean zone where process equipment such as exposure equipment is installed is close to 10 m, and the height of the return chamber under the floor is as high as 5 to 6 m. Moreover, the total floor area is tens of thousands m 2, and chambers covering a large number of process devices are individually installed in the clean zone. The heat dissipating parts that dissipate the heat of each chamber are individually installed in the return chamber, while the cooling water supply device is installed outside the clean room. Inevitably, the connection requires work at a high place for connection, and also requires a great deal of labor such as keeping the cold water piping and measures against water leakage.

また、特許文献1〜3では、冷凍サイクルの負荷は、最大空調負荷に対応した能力に設定され、圧縮機の冷媒吐出圧は一定として運転されるため、蒸発器で吸熱した冷媒熱の排熱は、凝縮器に流す冷却水の循環量を制御し、吸熱量と排熱量のマッチングを図っている。しかし、冷却水で凝縮器を冷却する水冷式は、空調負荷が大きい場合には、凝縮器での放熱量を適正に制御できるものの、空調負荷が少ない場合には、凝縮器側に供給する冷却水流量が極端に少なくなり、冷却水流量の制御範囲以下となり安定運転が困難になる可能性がある。   Moreover, in patent documents 1-3, since the load of a refrigerating cycle is set to the capacity | capacitance corresponding to the largest air-conditioning load, and the refrigerant | coolant discharge pressure of a compressor is drive | operated as fixed, the exhaust heat of the refrigerant | coolant heat absorbed by the evaporator Controls the circulating amount of cooling water that flows to the condenser to match the amount of heat absorbed and the amount of exhaust heat. However, the water-cooled type, which cools the condenser with cooling water, can properly control the heat dissipation in the condenser when the air-conditioning load is large, but the cooling supplied to the condenser side when the air-conditioning load is small. There is a possibility that the water flow rate becomes extremely small and becomes less than the control range of the cooling water flow rate, which makes stable operation difficult.

すなわち、制御対象であるチャンバの温度制御は、吸込空気と吹出温度の温度差は±2℃以下と空調負荷が小さいケースが多い。他方、凝縮器へ供給する冷却水温度は18℃程度の冷却水が用いられ、冷媒の凝縮温度(70℃前後)に対して冷却水温度が低いため、空調負荷が小さくなるほど、冷却水量の制御は困難となり、冷凍サイクルを安定して運転し、しかも空調負荷に合わせて、凝縮器側の排熱量を調整することは困難となる。   That is, in the temperature control of the chamber to be controlled, there are many cases where the temperature difference between the intake air and the blowing temperature is ± 2 ° C. or less and the air conditioning load is small. On the other hand, the cooling water temperature supplied to the condenser is about 18 ° C., and the cooling water temperature is lower than the refrigerant condensing temperature (around 70 ° C.). It becomes difficult to operate the refrigeration cycle stably and to adjust the amount of exhaust heat on the condenser side according to the air conditioning load.

そこで、本発明の目的は、上記課題を解決し、冷凍サイクルの負荷を一定に保ちつつ制御対象のチャンバの空調負荷に対応して排熱量を制御できる精密空調機を提供することにある。   Accordingly, an object of the present invention is to provide a precision air conditioner that can solve the above-mentioned problems and can control the amount of exhaust heat corresponding to the air conditioning load of the chamber to be controlled while keeping the load of the refrigeration cycle constant.

上記目的を達成するために本発明は、クリーンルームに設置された空調対象であるチャンバ内の空気を導入し、これを設定温度にして前記チャンバに循環するための精密空調機において、
圧縮機の吐出側から吸込側にかけて、凝縮器、膨張弁、蒸発器が順次接続されると共に、前記圧縮機の吐出側のホットガスを前記蒸発器に流すホットガスバイパス回路を有する冷凍サイクルと、
前記冷凍サイクルの蒸発器が収容され、前記チャンバからの空気を導入し、前記蒸発器で設定温度に空調して前記チャンバに循環する熱回収部と、
前記クリーンルーム内に設けられると共に前記冷凍サイクルの凝縮器が収容され、かつその凝縮器をクリーンルーム内の空気で空冷して前記凝縮器の凝縮圧力を一定に保持する能力可変ファンを備えた放熱部と、
を備えた精密空調機である。
In order to achieve the above object, the present invention provides a precision air conditioner for introducing air in a chamber to be air-conditioned installed in a clean room and circulating the air into the chamber at a set temperature.
A condenser, an expansion valve, and an evaporator are sequentially connected from the discharge side of the compressor to the suction side, and a refrigeration cycle having a hot gas bypass circuit for flowing hot gas on the discharge side of the compressor to the evaporator;
A heat recovery unit that houses the evaporator of the refrigeration cycle, introduces air from the chamber, air-conditions to a set temperature with the evaporator and circulates to the chamber;
A heat dissipating unit provided with a variable capacity fan that is provided in the clean room and accommodates the condenser of the refrigeration cycle, and air-cools the condenser with air in the clean room to keep the condensation pressure of the condenser constant. ,
It is a precision air conditioner equipped with.

本発明において、前記冷凍サイクルと前記熱回収部と前記放熱部とが同一のケーシング内に収容されるものである。   In the present invention, the refrigeration cycle, the heat recovery unit, and the heat dissipation unit are accommodated in the same casing.

本発明において、前記ホットガスバイパス回路は比例制御弁を備え、前記熱回収部には、前記蒸発器で冷却された空調空気の温度を検出する温度センサが設けられ、その温度センサの検出値で、前記比例制御弁が制御され、これにより、蒸発器で冷却される空調空気が精密温度制御されるものである。   In the present invention, the hot gas bypass circuit includes a proportional control valve, and the heat recovery unit is provided with a temperature sensor for detecting the temperature of the conditioned air cooled by the evaporator, and the detected value of the temperature sensor is used. The proportional control valve is controlled, whereby the conditioned air cooled by the evaporator is precisely temperature controlled.

本発明において、前記蒸発器の冷媒出口と圧縮機の吸込側を結ぶ冷媒配管には、圧縮機の冷媒吸込圧力を一定に保持する吸込圧力調整弁が接続され、前記膨張弁が温度式膨張弁からなり、前記吸込圧力調整弁の上流側の配管には、前記温度式膨張弁の感温筒が設けられ、これにより前記蒸発器での冷媒蒸発圧力が一定に保持されるものである。   In this invention, the refrigerant | coolant piping which connects the refrigerant | coolant exit of the said evaporator and the suction side of a compressor is connected to the suction pressure adjustment valve which hold | maintains the refrigerant | coolant suction pressure of a compressor uniformly, and the said expansion valve is a temperature type expansion valve. And a temperature sensing cylinder of the temperature type expansion valve is provided in a pipe upstream of the suction pressure adjusting valve, whereby the refrigerant evaporation pressure in the evaporator is kept constant.

本発明において、前記凝縮器から前記温度式膨張弁に至る高圧側冷媒配管には高圧センサが設けられ、他方前記放熱部の能力可変ファンがインバータ装置で駆動され、前記高圧センサで検出される冷媒の凝縮圧力が一定となるようにインバータ装置で前記能力可変ファンの回転を制御し、これにより凝縮器での冷媒凝縮圧力が一定に保持されるものである。   In the present invention, a high pressure sensor is provided in a high pressure side refrigerant pipe from the condenser to the temperature type expansion valve, and on the other hand, a variable capacity fan of the heat radiating unit is driven by an inverter device, and the refrigerant detected by the high pressure sensor The rotation of the variable capacity fan is controlled by an inverter device so that the condensing pressure of the refrigerant becomes constant, whereby the refrigerant condensing pressure in the condenser is kept constant.

前記凝縮器と前記高圧センサ間の高圧側冷媒配管には、受液タンクが接続されるとよい。   A liquid receiving tank may be connected to the high-pressure side refrigerant pipe between the condenser and the high-pressure sensor.

前記熱回収部と前記放熱部を収容するケーシングは、前記クリーンルームのレターンチャンバに設けられるとよい。   The casing that houses the heat recovery unit and the heat dissipation unit may be provided in a return chamber of the clean room.

本発明によれば、空調対象のチャンバ内の空気を精密温度制御するに際して、チャンバの空気を空調する蒸発器にホットガスを流すことで、空調空気を精密温度制御し、蒸発器で熱回収した熱の相当分を、クリーンルーム内に設置した放熱部の凝縮器で空冷により排熱することで、安定した精密温度制御が可能となると共に、クリーンルーム外に室外機や冷水源を設置することが不要にできるという優れた効果を発揮するものである。   According to the present invention, when the temperature in the air to be air-conditioned is precisely controlled, the conditioned air is precisely temperature-controlled by flowing hot gas to the evaporator that air-conditions the chamber air, and heat is recovered by the evaporator. A large amount of heat is exhausted by air cooling with a condenser in the heat dissipation section installed in the clean room, enabling stable precise temperature control and eliminating the need for an outdoor unit or cold water source outside the clean room. It exhibits an excellent effect of being able to be made.

本発明の一実施の形態を示す全体図である。1 is an overall view showing an embodiment of the present invention. 図1に示した精密空調機の冷凍サイクルの詳細図である。It is detail drawing of the refrigerating cycle of the precision air conditioning machine shown in FIG. 図2における冷凍サイクルをモリエル線図上で示した説明図である。It is explanatory drawing which showed the refrigerating cycle in FIG. 2 on the Mollier diagram.

以下、本発明の好適な一実施の形態を添付図面に基づいて詳述する。   A preferred embodiment of the present invention will be described below in detail with reference to the accompanying drawings.

先ず図1により、クリーンルーム10と、クリーンルーム10内に設置される露光装置等のプロセス機器11を覆う、空調対象としてのチャンバ12を空調する精密空調機13とを説明する。   First, a clean room 10 and a precision air conditioner 13 that air-conditions a chamber 12 as an air-conditioning target that covers a process device 11 such as an exposure apparatus installed in the clean room 10 will be described with reference to FIG.

クリーンルーム10は、露光装置等のプロセス機器11が設置されると共にこれを覆うチャンバ12が設けられたクリーンゾーン16と、クリーンゾーン16の天井17の上方に形成され、クリーンゾーン16に清浄空気を給気する給気チャンバ18と、クリーンゾーン16の床19の下に形成されクリーンゾーン16からの空気を吸引するレターンチャンバ20で構成される。レターンチャンバ20と給気チャンバ18とは循環路21で連結され、その循環路21にクリーンルーム用空調機22が設けられ、給気チャンバ18内の天井17には、クリーンゾーン16に清浄空気を吹き出す、HEPAとファンを有するファンフィルタユニット23が複数設けられる。レターンチャンバ20からの空気は、循環路21を介して空調機22に導入され、空調機22で設定温度に空調され、その空調空気が給気チャンバ18からファンフィルタユニット23内の高性能フィルタを通して清浄化されてクリーンゾーン16にダウンフローで吹き出される。   The clean room 10 is formed above a clean zone 16 in which a process device 11 such as an exposure apparatus is installed and a chamber 12 covering the process device 11 is provided, and a ceiling 17 of the clean zone 16, and supplies clean air to the clean zone 16. An air supply chamber 18 to be aired and a return chamber 20 which is formed under the floor 19 of the clean zone 16 and sucks air from the clean zone 16 are configured. The return chamber 20 and the air supply chamber 18 are connected by a circulation path 21, a clean room air conditioner 22 is provided in the circulation path 21, and clean air is blown out to the clean zone 16 on the ceiling 17 in the air supply chamber 18. A plurality of fan filter units 23 having HEPA and fans are provided. The air from the return chamber 20 is introduced into the air conditioner 22 through the circulation path 21 and air-conditioned to the set temperature by the air conditioner 22, and the air-conditioned air passes from the air supply chamber 18 through the high performance filter in the fan filter unit 23. It is cleaned and blown out to the clean zone 16 in a down flow.

クリーンゾーン16には、床19上にプロセス機器11を覆うチャンバ12が設置され、チャンバ12内を精密空調機13で空調することで、プロセス機器11及びプロセス機器11の周囲環境を精密温度制御するようになっている。   In the clean zone 16, a chamber 12 that covers the process equipment 11 is installed on the floor 19, and the inside of the chamber 12 is air-conditioned by the precision air conditioner 13, thereby precisely controlling the temperature of the process equipment 11 and the environment surrounding the process equipment 11. It is like that.

本発明においては、この精密空調機13を、クリーンルーム10内、特にレターンチャンバ20内に設置したものである。すなわち精密空調機13は、チャンバ12内の空気を還気(RA)として導入し、これを精密空調して給気SAとしてチャンバ12に供給循環する蒸発器26及び循環ファン27を備えた熱回収部28と、圧縮機29等を備えた機器部30と、凝縮器31及び空冷用の能力可変ファン32を備えた放熱部33とで構成する。ここで放熱部33は少なくともクリーンルーム10、特にレターンチャンバ20に設けられるものである。また、図示のように、熱回収部28と圧縮機29等を備えた機器部30と、放熱部33とは、一つのケーシング14内に収容して精密空調機13とする。この精密空調機13は、クリーンルーム10内のクリーンゾーン16やレターンチャンバ20に設けるが、特に、レターンチャンバ20に設けるとよい。   In the present invention, the precision air conditioner 13 is installed in the clean room 10, particularly in the return chamber 20. In other words, the precision air conditioner 13 introduces the air in the chamber 12 as return air (RA), performs precision air conditioning on the air, and supplies and circulates the air to the chamber 12 as a supply air SA. The unit 28 includes a device unit 30 including a compressor 29 and the like, and a heat radiating unit 33 including a condenser 31 and a variable capacity fan 32 for air cooling. Here, the heat radiating section 33 is provided at least in the clean room 10, particularly in the return chamber 20. Further, as shown in the figure, the equipment unit 30 including the heat recovery unit 28, the compressor 29, and the like, and the heat radiating unit 33 are housed in one casing 14 to form the precision air conditioner 13. The precision air conditioner 13 is provided in the clean zone 16 and the return chamber 20 in the clean room 10, and particularly preferably provided in the return chamber 20.

次に図2により、精密空調機13を構成する冷凍サイクル25を説明する。   Next, the refrigeration cycle 25 constituting the precision air conditioner 13 will be described with reference to FIG.

冷凍サイクル25は、圧縮機29の吐出側から吸込側にかけて、放熱部33の凝縮器31、受液タンク34、膨張弁としての温度式膨張弁35、熱回収部28の蒸発器26、アキュムレータ36が冷媒配管37で順次接続され、さらに、圧縮機29の吐出側から凝縮器31に至る高圧側冷媒配管37aから分岐し、ホットガスを蒸発器26に流すホットガスバイパス回路40が設けられて主に構成される。   The refrigeration cycle 25 includes, from the discharge side to the suction side of the compressor 29, the condenser 31 of the heat radiating unit 33, the liquid receiving tank 34, the temperature type expansion valve 35 as an expansion valve, the evaporator 26 of the heat recovery unit 28, and the accumulator 36. Are sequentially connected by a refrigerant pipe 37, and further, a hot gas bypass circuit 40 that branches from a high-pressure side refrigerant pipe 37a from the discharge side of the compressor 29 to the condenser 31 and flows hot gas to the evaporator 26 is provided. Configured.

この冷凍サイクル25を、さらに詳しく説明する。   This refrigeration cycle 25 will be described in more detail.

圧縮機29の吐出側の高圧側冷媒配管37aには、圧縮機29の過負荷を検出する圧力スイッチ41が設けられ、その高圧側冷媒配管37aが凝縮器31の入口側に接続される。凝縮器31の入口側の高圧側冷媒配管37aには凝縮圧力調整弁50が接続される。凝縮器31は、フィン&チューブで形成され、その凝縮器31に能力可変ファン32が設けられて放熱部33が形成される。凝縮器31の出口側の高圧側冷媒配管37aは、受液タンク34の上部に接続され、受液タンク34の底部に高圧側冷媒配管37bが接続される。この受液タンク34から温度式膨張弁35に至る高圧側冷媒配管37bには、高圧センサ42が接続され、さらに、その下流の高圧側冷媒配管37bには、水分量を検出するサイトグラス43、冷媒中の水分を除去するフィルタドライヤ44、止弁としてのバックレス弁45が接続される。   The high pressure side refrigerant pipe 37 a on the discharge side of the compressor 29 is provided with a pressure switch 41 that detects an overload of the compressor 29, and the high pressure side refrigerant pipe 37 a is connected to the inlet side of the condenser 31. A condensing pressure adjusting valve 50 is connected to the high-pressure side refrigerant pipe 37 a on the inlet side of the condenser 31. The condenser 31 is formed of fins and tubes, and the variable capacity fan 32 is provided in the condenser 31 to form a heat radiation portion 33. The high-pressure side refrigerant pipe 37 a on the outlet side of the condenser 31 is connected to the upper part of the liquid receiving tank 34, and the high-pressure side refrigerant pipe 37 b is connected to the bottom of the liquid receiving tank 34. A high-pressure sensor 42 is connected to the high-pressure side refrigerant pipe 37b extending from the liquid receiving tank 34 to the temperature type expansion valve 35. Further, a sight glass 43 for detecting the amount of water is connected to the high-pressure side refrigerant pipe 37b downstream thereof. A filter dryer 44 for removing moisture in the refrigerant and a backless valve 45 as a stop valve are connected.

温度式膨張弁35からの低圧側冷媒配管37cは、蒸発器26の入口側に接続される。蒸発器26は、フィン&チューブで形成され、その蒸発器26の出口側に循環ファン27が設けられて熱回収部28が形成される。   A low-pressure side refrigerant pipe 37 c from the temperature type expansion valve 35 is connected to the inlet side of the evaporator 26. The evaporator 26 is formed of fins and tubes, and a circulation fan 27 is provided on the outlet side of the evaporator 26 to form a heat recovery unit 28.

蒸発器26の出口側からアキュムレータ36に至る低圧側冷媒配管37cには、圧力計46、外均圧導入弁47、ストレーナ48、吸入圧力調整弁49が順次接続される。   A pressure gauge 46, an external pressure equalizing introduction valve 47, a strainer 48, and a suction pressure adjusting valve 49 are sequentially connected to a low-pressure side refrigerant pipe 37c extending from the outlet side of the evaporator 26 to the accumulator 36.

温度式膨張弁35は、ダイアフラム弁からなり、詳細は図示しないが、一方ダイアフラム室がキャピラリ管51を介して感温筒52が接続され、他方のダイアフラム室が外均管53に接続されて構成される。感温筒52は、蒸発器26の出口側の低圧側冷媒配管37cに沿って設けられ、外均管53は、外均圧導入弁47に接続される。温度式膨張弁35は、感温筒52からキャピラリ管51を介してダイアフラムの一方に作用する圧力(蒸発器26の蒸発温度に基づく圧力)と、外均管53からダイアフラムの他方に作用する圧力(蒸発器26の蒸発圧力)との差圧で、弁開度(減圧度)が制御される。   The temperature type expansion valve 35 is formed of a diaphragm valve. Although not shown in detail, the temperature chamber 52 is connected to the temperature sensing cylinder 52 via the capillary tube 51 and the other diaphragm chamber is connected to the outer equalizing tube 53. Is done. The temperature sensing cylinder 52 is provided along the low-pressure side refrigerant pipe 37 c on the outlet side of the evaporator 26, and the outer equalization pipe 53 is connected to the outer equalization introduction valve 47. The temperature type expansion valve 35 has a pressure (pressure based on the evaporation temperature of the evaporator 26) acting on one of the diaphragms from the temperature sensing cylinder 52 through the capillary tube 51, and a pressure acting on the other of the diaphragms from the outer equalizing tube 53. The valve opening degree (decompression degree) is controlled by a differential pressure with respect to (evaporation pressure of the evaporator 26).

なお、図示の例では、外均式の温度式膨張弁35の例で説明したが、内均式の温度式膨張弁を用いても、或いは電動式膨張弁を用いるようにしてもよい。   In the illustrated example, the example of the outer-equalization type temperature expansion valve 35 has been described. However, an inner-equalization type temperature expansion valve may be used, or an electric expansion valve may be used.

吸入圧力調整弁49は、その下流側の冷媒圧力が入力され、その冷媒圧力が一定となるように圧縮機29の吸込圧が調整される。   The suction pressure adjusting valve 49 receives the downstream refrigerant pressure and adjusts the suction pressure of the compressor 29 so that the refrigerant pressure becomes constant.

ホットガスバイパス回路40は、圧縮機29の吐出側から凝縮器31に至る高圧側冷媒配管37aと蒸発器26の入口とを接続するバイパス配管54と、そのバイパス配管に接続した比例制御弁55とで構成される。また、比例制御弁55の上流側のバイパス配管54にストレーナ56が接続される。   The hot gas bypass circuit 40 includes a bypass pipe 54 connecting the high-pressure side refrigerant pipe 37a extending from the discharge side of the compressor 29 to the condenser 31 and the inlet of the evaporator 26, and a proportional control valve 55 connected to the bypass pipe. Consists of. A strainer 56 is connected to the bypass pipe 54 upstream of the proportional control valve 55.

熱回収部28には、蒸発器26で空調されて循環ファン27でチャンバ12に供給される給気SAの温度を検出する温度センサ58が設けられ、この温度センサ58の検出値で、ホットガスバイパス回路40の比例制御弁55が制御されるようになっている。   The heat recovery unit 28 is provided with a temperature sensor 58 that detects the temperature of the supply air SA that is air-conditioned by the evaporator 26 and is supplied to the chamber 12 by the circulation fan 27. The proportional control valve 55 of the bypass circuit 40 is controlled.

また、放熱部33の能力可変ファン32は、インバータ装置60で回転数可変に駆動され、そのインバータ装置60に高圧センサ42の検出値が入力され、高圧センサ42の検出値が一定となるようにインバータ装置60が能力可変ファン32の風量を制御するようになっている。   Further, the variable capacity fan 32 of the heat radiating unit 33 is driven by the inverter device 60 so that the number of rotations can be varied. The inverter device 60 controls the air volume of the variable capacity fan 32.

この図2の冷凍サイクル25においては、圧縮機29で圧縮された冷媒ガス(ホットガス)は、凝縮圧力調整弁50で圧力制御されて主に凝縮器31を通り、そこで能力可変ファン32の回転で送風されるレターンチャンバ20内の空気(23〜25℃程度)と熱交換して凝縮し、温度式膨張弁35で減圧されて蒸発器26に流れる。他方、圧縮機29からのホットガスの一部は、ホットガスバイパス回路40から比例制御弁55で流量制御されて、温度式膨張弁35で減圧された気液混相冷媒と共に蒸発器26に流れる。熱回収部28では、チャンバ12からの還気RAが導入され、これを蒸発器26で冷却して設定温度±0.01〜±0.1℃にし、精密温度制御した給気SAとしてチャンバ12に供給する。   In the refrigeration cycle 25 of FIG. 2, the refrigerant gas (hot gas) compressed by the compressor 29 is pressure-controlled by the condensing pressure adjusting valve 50 and mainly passes through the condenser 31, where the capacity variable fan 32 rotates. The heat is exchanged with the air in the return chamber 20 (about 23 to 25 ° C.) that is blown by the air to condense, and the pressure is reduced by the temperature expansion valve 35 and flows to the evaporator 26. On the other hand, a part of the hot gas from the compressor 29 flows from the hot gas bypass circuit 40 to the evaporator 26 together with the gas-liquid mixed phase refrigerant whose flow rate is controlled by the proportional control valve 55 and decompressed by the temperature type expansion valve 35. In the heat recovery unit 28, the return air RA from the chamber 12 is introduced, and this is cooled by the evaporator 26 to a set temperature ± 0.01 to ± 0.1 ° C., and the supply air SA with precise temperature control is used as the chamber 12. To supply.

蒸発器26で熱回収した冷媒は、蒸発冷媒として吸入圧力調整弁49で、圧縮機29の吸込圧力に調整され、アキュムレータ36を介して圧縮機29に吸い込まれて再度圧縮されてホットガスとされて循環される。   The refrigerant heat recovered by the evaporator 26 is adjusted to the suction pressure of the compressor 29 by the suction pressure adjusting valve 49 as the evaporated refrigerant, sucked into the compressor 29 via the accumulator 36 and compressed again to become hot gas. Circulated.

先ず本発明では、圧縮機29は、吸入圧力調整弁49で吸込圧力に調整され、かつスーパーヒート(飽和ガス線より5℃高い温度)とされた蒸発冷媒を所定の圧力に圧縮してホットガスとする。このホットガスは、放熱部33の凝縮器31とホットガスバイパス回路40を介して蒸発器26の双方に供給される。この際、凝縮器31の出口側の圧力を高圧センサ42が検出し、これに基づいてインバータ装置60が能力可変ファン32の送風量を制御すると共に、凝縮圧力調整弁50は凝縮器31に流入する圧力を調整する。これにより、凝縮器31での熱交換量(排熱量)が調整され、ホットガスバイパス量の変動にかかわらず、凝縮器31での凝縮圧力が一定に保たれる。この凝縮器31での凝縮はレターンチャンバ20内の空気(23℃〜25℃程度)と熱交換するため、凝縮冷媒温度と空気との温度差が小さく、放熱量が少ない場合でも能力可変ファン32の送風量で適正に放熱量を制御できる。   First, in the present invention, the compressor 29 compresses the evaporative refrigerant, which is adjusted to the suction pressure by the suction pressure adjusting valve 49 and is superheated (temperature higher by 5 ° C. than the saturated gas line), to a predetermined pressure to generate hot gas. And This hot gas is supplied to both the evaporator 26 via the condenser 31 of the heat radiating unit 33 and the hot gas bypass circuit 40. At this time, the pressure on the outlet side of the condenser 31 is detected by the high-pressure sensor 42, and based on this, the inverter device 60 controls the blowing amount of the capacity variable fan 32, and the condensing pressure adjusting valve 50 flows into the condenser 31. Adjust the pressure. Thereby, the heat exchange amount (exhaust heat amount) in the condenser 31 is adjusted, and the condensing pressure in the condenser 31 is kept constant regardless of fluctuations in the hot gas bypass amount. Since the condensation in the condenser 31 exchanges heat with the air in the return chamber 20 (about 23 ° C. to 25 ° C.), the variable temperature fan 32 has a small temperature difference between the condensed refrigerant temperature and the air, and the amount of heat radiation is small. The amount of heat release can be controlled appropriately by the amount of air flow.

次に、熱回収部28での給気SAの精密温度制御は、温度センサ58により比例制御弁55の開度を制御し、ホットガスバイパス回路40から蒸発器26に流入するホットガス量を制御することで行われる。   Next, in the precise temperature control of the supply air SA in the heat recovery unit 28, the opening degree of the proportional control valve 55 is controlled by the temperature sensor 58, and the amount of hot gas flowing into the evaporator 26 from the hot gas bypass circuit 40 is controlled. It is done by doing.

この温度センサ58は、図では熱回収部28の蒸発器26の出口側の給気SAの温度を検出する例を示しているが、蒸発器26の入口側の還気RAの温度を検出する温度センサを別途設け、その出入口の温度センサで比例制御弁55を制御するようにしてもよい。   Although the temperature sensor 58 shows an example of detecting the temperature of the supply air SA on the outlet side of the evaporator 26 of the heat recovery unit 28 in the figure, the temperature sensor 58 detects the temperature of the return air RA on the inlet side of the evaporator 26. A temperature sensor may be provided separately, and the proportional control valve 55 may be controlled by the temperature sensor at the entrance / exit.

他方、温度式膨張弁35は、ホットガスバイパス量に係わらず、減圧度を調整して蒸発器26の蒸発圧力を一定に保つものである。すなわち、蒸発器26の出口側温度が、感温筒52内に封入された冷媒の圧力に変換され、これがキャピラリ管51を介して温度式膨張弁35のダイアフラム室の一方に導入され、同時に蒸発器26で蒸発された冷媒の蒸発圧力を外均管53を介して温度式膨張弁35のダイアフラム室の他方に導入され、両ダイアフラム室の差圧で温度式膨張弁35の減圧度が調整される。   On the other hand, the temperature type expansion valve 35 adjusts the degree of pressure reduction to keep the evaporation pressure of the evaporator 26 constant regardless of the hot gas bypass amount. That is, the outlet side temperature of the evaporator 26 is converted into the pressure of the refrigerant sealed in the temperature sensing cylinder 52, and this is introduced into one of the diaphragm chambers of the temperature type expansion valve 35 via the capillary tube 51, and simultaneously evaporated. The evaporation pressure of the refrigerant evaporated in the vessel 26 is introduced to the other of the diaphragm chambers of the temperature type expansion valve 35 through the outer equalizing pipe 53, and the pressure reduction degree of the temperature type expansion valve 35 is adjusted by the differential pressure between the two diaphragm chambers. The

これにより、蒸発器26では、蒸発圧力が一定に保たれ、その蒸発器26での冷媒蒸発量、すなわち還気RAと冷媒の熱交換量が、ホットガス流入量で制御されるため、空調負荷に応じた精密温度制御が行なわれる。   Thereby, in the evaporator 26, the evaporation pressure is kept constant, and the refrigerant evaporation amount in the evaporator 26, that is, the heat exchange amount between the return air RA and the refrigerant is controlled by the hot gas inflow amount. Precise temperature control according to is performed.

この冷凍サイクル25おいては、熱回収部28の蒸発器26で回収した熱を、放熱部33の凝縮器31でレターンチャンバ20の空気に排熱するが、その排熱量は、クリーンルーム10の空調機13で処理する熱量に対して十分に小さいため、空調機13の空調で十分に処理することができる。したがって、従来のように排熱のための室外機や冷水供給装置をクリーンルーム10外に設置し、冷媒配管で接続する手間が不要となる。   In the refrigeration cycle 25, the heat recovered by the evaporator 26 of the heat recovery unit 28 is exhausted to the air of the return chamber 20 by the condenser 31 of the heat radiating unit 33. Since the amount of heat processed by the machine 13 is sufficiently small, it can be sufficiently processed by the air conditioning of the air conditioner 13. Therefore, it is not necessary to install an outdoor unit for exhaust heat or a cold water supply device outside the clean room 10 and connect with a refrigerant pipe as in the conventional case.

また、精密温度制御する際には、ホットガスバイパス回路40では、比例制御弁55で、そのホットガス流量を、レターンチャンバ20の空調負荷に合わせて制御して蒸発器26に流す。この際、高圧センサ42の検出値で凝縮器31が凝縮圧力を一定に制御し、同時に温度式膨張弁35が蒸発圧力を一定に制御し、その上で、吸入圧力調整弁49が圧縮機29の吸込圧力を調整することで冷凍サイクル25が安定して運転される。   Further, when the precise temperature control is performed, in the hot gas bypass circuit 40, the flow rate of the hot gas is controlled by the proportional control valve 55 according to the air conditioning load of the return chamber 20, and flows to the evaporator 26. At this time, the condenser 31 controls the condensing pressure to be constant based on the detection value of the high pressure sensor 42, and at the same time, the temperature type expansion valve 35 controls the evaporating pressure to be constant. The refrigeration cycle 25 is stably operated by adjusting the suction pressure.

また、比例制御弁55は、レターンチャンバ20の空調負荷変動に応じてホットガス量を制御し、蒸発器26で空調負荷に応じて、冷媒が熱回収する。その後、圧縮機29で圧縮したホットガスが放熱部33の凝縮器31に導入して放熱される。このように熱回収後に放熱するため、空調負荷が急激に変動する際には、冷凍サイクル25での熱回収量と放熱量のマッチングが悪くなりやすいが、冷凍サイクル25には、受液タンク34を設けているため、冷凍サイクル25は安定した運転が可能となる。   The proportional control valve 55 controls the amount of hot gas according to the air conditioning load fluctuation of the return chamber 20, and the refrigerant recovers heat by the evaporator 26 according to the air conditioning load. Thereafter, the hot gas compressed by the compressor 29 is introduced into the condenser 31 of the heat radiating section 33 and radiated. Since heat is radiated after heat recovery in this manner, when the air conditioning load fluctuates rapidly, the matching between the heat recovery amount and the heat dissipation amount in the refrigeration cycle 25 tends to deteriorate, but the refrigeration cycle 25 includes a liquid receiving tank 34. Therefore, the refrigeration cycle 25 can be stably operated.

次に、この冷凍サイクル25を図3のモリエル線図上で説明する。   Next, the refrigeration cycle 25 will be described on the Mollier diagram of FIG.

図3は、冷媒にR407Cを用いたときのモリエル線図上の冷凍サイクルを示し、横軸は比エンタルピー(kJ/kg)、縦軸は絶対圧力(MPa)、LgはR407Cの飽和ガス線、Llは飽和液線を示している。   FIG. 3 shows the refrigeration cycle on the Mollier diagram when R407C is used as the refrigerant, the horizontal axis is the specific enthalpy (kJ / kg), the vertical axis is the absolute pressure (MPa), Lg is the saturated gas line of R407C, Ll indicates a saturated liquid line.

先ず、圧縮機29の吸込冷媒は、吸入圧力調整弁49で点A(12℃、0.5MPa)で圧縮機29に導入される。この点Aは、飽和ガス線Lgより十分に高い(+5℃)ガス相側で、スーパーヒート状態にあり、その冷媒ガスが圧縮機29で点B(75℃、2.0MPa)に圧縮される。この点Bのホットガスは、凝縮器31側とホットガスバイパス回路40側に供給され、その分岐点で、点C(1.7MPa)に下がった圧力とされる。凝縮器31に導入されたホットガスは、放熱により、点Cの凝縮圧力を保ったまま飽和液線Llを通り、気液混相状態から過冷却液となる点D(31℃)まで冷却される。   First, the suction refrigerant of the compressor 29 is introduced into the compressor 29 at a point A (12 ° C., 0.5 MPa) by the suction pressure adjusting valve 49. This point A is in the superheat state on the gas phase side sufficiently higher than the saturated gas line Lg (+ 5 ° C.), and the refrigerant gas is compressed by the compressor 29 to point B (75 ° C., 2.0 MPa). . The hot gas at point B is supplied to the condenser 31 side and the hot gas bypass circuit 40 side, and at that branch point, the pressure is reduced to point C (1.7 MPa). The hot gas introduced into the condenser 31 passes through the saturated liquid line Ll while maintaining the condensation pressure at the point C, and is cooled to the point D (31 ° C.) that becomes the supercooled liquid from the gas-liquid mixed phase state by heat radiation. .

この点Dの過冷却度は、温度式膨張弁35で制御でき、温度式膨張弁35で点E(11℃、0.8MPa)まで減圧される。蒸発器26では、この点Eの圧力で蒸発圧力が維持される。他方点Cからのホットガスは、蒸発器26に導入されることで、点F(0.8MPa)まで圧力が下がって蒸発器26の蒸発圧力となる。蒸発器26には、点Fのホットガスと温度式膨張弁35で点Eまで減圧された冷媒とが流入し、その冷媒が、チャンバ12からの空気(還気RA)と熱交換する。これにより冷媒は、点Gの状態となって、蒸発器26の出口から吸入圧力調整弁49の入口側に流入し、その吸入圧力調整弁49で、点Gから点Aに減圧調整されて、圧縮機29に導入される。   The degree of supercooling at this point D can be controlled by the temperature type expansion valve 35, and the pressure is reduced to the point E (11 ° C., 0.8 MPa) by the temperature type expansion valve 35. In the evaporator 26, the evaporation pressure is maintained at the pressure at this point E. On the other hand, the hot gas from the point C is introduced into the evaporator 26, whereby the pressure is reduced to the point F (0.8 MPa) and becomes the evaporation pressure of the evaporator 26. The hot gas at point F and the refrigerant depressurized to point E by the temperature type expansion valve 35 flow into the evaporator 26, and the refrigerant exchanges heat with air from the chamber 12 (return air RA). As a result, the refrigerant enters the state of point G and flows from the outlet of the evaporator 26 to the inlet side of the suction pressure adjustment valve 49, and the suction pressure adjustment valve 49 reduces the pressure from point G to point A. It is introduced into the compressor 29.

このモリエル線図上の冷凍サイクルで点Cから点Dの熱量は、凝縮器31の放熱量であり、点Eから点Gの熱量は、蒸発器26での熱量変化であり、凝縮器31の放熱量は、圧縮機29の熱量分(点Gから点Fの熱量)と蒸発熱量分の合計熱量となる。   In this refrigeration cycle on the Mollier diagram, the amount of heat from point C to point D is the amount of heat released from the condenser 31, and the amount of heat from point E to point G is the change in the amount of heat at the evaporator 26, The amount of heat release is the total amount of heat corresponding to the amount of heat of the compressor 29 (the amount of heat from point G to point F) and the amount of heat of evaporation.

ここで、ホットガスバイパス量が0%の場合は蒸発器26の蒸発熱量は、点Eから点Gの熱量となり、空調負荷がなくホットガスバイパス量が100%のときは、圧縮機29の熱量分を凝縮器26で放熱することとなり、蒸発器26の入口の冷媒の比エンタルピーは、点Gから圧縮機29の熱量分を引いた点Hとなる。よって、ホットガスバイパス量0%〜100%に対して、蒸発器26の入口の冷媒の比エンタルピーは、点E〜点Hのいずれかの点H’となり、点H’〜点Gの熱量が空調負荷に応じた蒸発熱量、すなわち蒸発器26で空気(還気RA)と熱交換した熱量となる。   Here, when the hot gas bypass amount is 0%, the evaporation heat amount of the evaporator 26 is the heat amount from the point E to the point G, and when there is no air conditioning load and the hot gas bypass amount is 100%, the heat amount of the compressor 29. The heat is dissipated by the condenser 26, and the specific enthalpy of the refrigerant at the inlet of the evaporator 26 is a point H obtained by subtracting the amount of heat of the compressor 29 from the point G. Therefore, with respect to the hot gas bypass amount of 0% to 100%, the specific enthalpy of the refrigerant at the inlet of the evaporator 26 is any point H ′ from point E to point H, and the amount of heat from point H ′ to point G is The amount of heat of evaporation according to the air conditioning load, that is, the amount of heat exchanged with the air (return air RA) by the evaporator 26.

従ってチャンバ12の空調負荷状態に合わせて、ホットガスバイパス量0%〜100%の範囲で制御することで、図に示した点Eから点Hの間で、空調負荷にあわせた熱交換量を調整することができる。   Therefore, by controlling the hot gas bypass amount in the range of 0% to 100% in accordance with the air conditioning load state of the chamber 12, the heat exchange amount according to the air conditioning load between the points E and H shown in the figure can be obtained. Can be adjusted.

このホットガスバイパス回路40に流すホットガスバイパス量は、冷凍サイクル25の冷媒の循環量を100%としたとき、圧縮機での発生熱量を放熱できる量まで可能であり、最大で70%程度まで流しても冷凍サイクル25は安定して運転が可能である。従って、比例制御弁55での流量制御を適正に行うことで、設定温度(例えば23℃)に対して、±0.01℃〜±0.1℃に精密温度制御することができる。   The amount of hot gas bypass that flows to the hot gas bypass circuit 40 can be as much as the amount of heat generated in the compressor can be dissipated when the circulation amount of the refrigerant in the refrigeration cycle 25 is 100%. Even if it flows, the refrigeration cycle 25 can be operated stably. Accordingly, by appropriately performing the flow rate control with the proportional control valve 55, it is possible to precisely control the temperature to ± 0.01 ° C. to ± 0.1 ° C. with respect to the set temperature (for example, 23 ° C.).

以上本発明の実施の形態を説明したが、本発明は、上述の実施の形態に限定されず種々の変更が可能である。すなわち膨張弁として温度式膨張弁を例に説明したが、電動式膨張弁で行うようにしても、また図3では冷媒としてR407を用いたときの冷媒凝縮圧力、蒸発圧力、圧縮機吸込圧力の一例を示したが、空調負荷や処理風量に応じて、圧縮機の圧縮能力や凝縮圧力、蒸発圧力を変更してもよいことは勿論である。   Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made. That is, although the temperature type expansion valve has been described as an example of the expansion valve, the refrigerant condensation pressure, the evaporation pressure, and the compressor suction pressure when R407 is used as the refrigerant in FIG. Although an example has been shown, it is a matter of course that the compression capacity, the condensation pressure, and the evaporation pressure of the compressor may be changed according to the air conditioning load and the processing air volume.

10 クリーンルーム
12 チャンバ
14 ケーシング
25 冷凍サイクル
26 蒸発器
28 熱回収部
29 圧縮機
31 凝縮器
32 能力可変ファン
33 放熱部
40 ホットガスバイパス回路
DESCRIPTION OF SYMBOLS 10 Clean room 12 Chamber 14 Casing 25 Refrigerating cycle 26 Evaporator 28 Heat recovery part 29 Compressor 31 Condenser 32 Capability variable fan 33 Heat radiation part 40 Hot gas bypass circuit

Claims (7)

クリーンルームに設置された空調対象であるチャンバ内の空気を導入し、これを設定温度にして前記チャンバに循環するための精密空調機において、
圧縮機の吐出側から吸込側にかけて、凝縮器、膨張弁、蒸発器が順次接続されると共に、前記圧縮機の吐出側のホットガスを前記蒸発器に流すホットガスバイパス回路を有する冷凍サイクルと、
前記冷凍サイクルの蒸発器が収容され、前記チャンバからの空気を導入し、前記蒸発器で設定温度に空調して前記チャンバに循環する熱回収部と、
前記クリーンルーム内に設けられると共に前記冷凍サイクルの凝縮器が収容され、かつその凝縮器をクリーンルーム内の空気で空冷して前記凝縮器の凝縮圧力を一定に保持する能力可変ファンを備えた放熱部と、
を備えたことを特徴とする精密空調機。
In a precision air conditioner for introducing air in a chamber to be air-conditioned installed in a clean room and circulating it to the chamber with this set temperature,
A condenser, an expansion valve, and an evaporator are sequentially connected from the discharge side of the compressor to the suction side, and a refrigeration cycle having a hot gas bypass circuit for flowing hot gas on the discharge side of the compressor to the evaporator;
A heat recovery unit that houses the evaporator of the refrigeration cycle, introduces air from the chamber, air-conditions to a set temperature with the evaporator and circulates to the chamber;
A heat dissipating unit provided with a variable capacity fan that is provided in the clean room and accommodates the condenser of the refrigeration cycle, and air-cools the condenser with air in the clean room to keep the condensation pressure of the condenser constant. ,
A precision air conditioner characterized by comprising
前記冷凍サイクルと前記熱回収部と前記放熱部とが同一のケーシング内に収容される請求項1記載の精密空調機。   The precision air conditioner according to claim 1, wherein the refrigeration cycle, the heat recovery unit, and the heat dissipation unit are accommodated in the same casing. 前記ホットガスバイパス回路は、比例制御弁を備え、前記熱回収部には、前記蒸発器で冷却された空調空気の温度を検出する温度センサが設けられ、その温度センサの検出値で、前記比例制御弁が制御され、これにより、蒸発器で冷却される空調空気は精密温度制御される請求項1又は2記載の精密空調機。   The hot gas bypass circuit includes a proportional control valve, and the heat recovery unit is provided with a temperature sensor that detects the temperature of the conditioned air cooled by the evaporator, and the proportional value is determined by the detected value of the temperature sensor. The precision air conditioner according to claim 1 or 2, wherein the control valve is controlled, and thereby the conditioned air cooled by the evaporator is precisely temperature controlled. 前記蒸発器の冷媒出口と圧縮機の吸込側を結ぶ冷媒配管には、圧縮機の冷媒吸込圧力を一定に保持する吸込圧力調整弁が接続され、前記膨張弁が温度式膨張弁からなり、前記吸込圧力調整弁の上流側の配管には、前記温度式膨張弁の感温筒が設けられ、これにより前記蒸発器での冷媒蒸発圧力が一定に保持される請求項3記載の精密空調機。   The refrigerant pipe connecting the refrigerant outlet of the evaporator and the suction side of the compressor is connected to a suction pressure adjusting valve that keeps the refrigerant suction pressure of the compressor constant, and the expansion valve is a temperature type expansion valve, The precision air conditioner according to claim 3, wherein a temperature sensing cylinder of the temperature type expansion valve is provided in a pipe upstream of the suction pressure adjusting valve, whereby the refrigerant evaporation pressure in the evaporator is kept constant. 前記凝縮器から前記温度式膨張弁に至る高圧側冷媒配管には高圧センサが設けられ、他方前記放熱部の能力可変ファンがインバータ装置で駆動され、前記高圧センサで検出される冷媒の凝縮圧力が一定となるようにインバータ装置で前記能力可変ファンの回転を制御し、これにより凝縮器での冷媒凝縮圧力が一定に保持される請求項4記載の精密空調機。   A high-pressure sensor is provided on the high-pressure side refrigerant pipe from the condenser to the temperature type expansion valve, while the variable capacity fan of the heat radiating unit is driven by an inverter device, and the condensing pressure of the refrigerant detected by the high-pressure sensor is The precision air conditioner according to claim 4, wherein the rotation of the capacity variable fan is controlled by an inverter device so as to be constant, whereby the refrigerant condensing pressure in the condenser is kept constant. 前記凝縮器と前記高圧センサ間の高圧側冷媒配管には、受液タンクが接続される請求項5記載の精密空調機。   The precision air conditioner according to claim 5, wherein a liquid receiving tank is connected to a high-pressure side refrigerant pipe between the condenser and the high-pressure sensor. 前記熱回収部と前記放熱部を収容するケーシングは、前記クリーンルームのレターンチャンバに設けられる請求項2記載の精密空調機。   The precision air conditioner according to claim 2, wherein a casing that houses the heat recovery unit and the heat dissipation unit is provided in a return chamber of the clean room.
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