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JP3933264B2 - Dehumidification air conditioning system - Google Patents
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JP3933264B2 - Dehumidification air conditioning system - Google Patents

Dehumidification air conditioning system Download PDF

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Publication number
JP3933264B2
JP3933264B2 JP22751097A JP22751097A JP3933264B2 JP 3933264 B2 JP3933264 B2 JP 3933264B2 JP 22751097 A JP22751097 A JP 22751097A JP 22751097 A JP22751097 A JP 22751097A JP 3933264 B2 JP3933264 B2 JP 3933264B2
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Prior art keywords
air
heat
desiccant
condenser
dehumidifying
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JP22751097A
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Japanese (ja)
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JPH1163871A (en
Inventor
健作 前田
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Ebara Corp
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Ebara Corp
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    • 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
    • F24F3/14Air-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 humidification; by dehumidification
    • F24F3/1411Air-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 humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
    • F24F3/1423Air-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 humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1016Rotary wheel combined with another type of cooling principle, e.g. compression cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1032Desiccant wheel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1056Rotary wheel comprising a reheater
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1068Rotary wheel comprising one rotor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1084Rotary wheel comprising two flow rotor segments

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Central Air Conditioning (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、除湿空調システム、特に室内プール施設などのように高湿度の空間を除湿するための除湿空調システムに係り、ヒートポンプによる冷却除湿とデシカントによる吸着除湿を併せて行い、かつヒートポンプからの放熱によってデシカントの再生処理を連続的に行えるようにした空調システムに関する。
【0002】
【従来の技術】
図7は、室内プール施設の内部空間用の除湿装置として米国で普及している従来技術であり、これは、圧縮機260と凝縮器220と蒸発器240と膨張弁250を主な構成機器として蒸気圧縮式冷凍サイクルをなす冷媒経路Aと、蒸発器240で前記冷媒経路Aと熱交換し送風機101と顕熱交換器150を主な構成機器として室内空気を取り入れて冷却除湿して室内に戻す処理空気経路Bと、凝縮器220で前記冷媒経路Aと熱交換しプール水を取り入れて加熱してプールに戻す水経路Cとによって構成されている。
【0003】
これにより、プール室内の高湿度の空気を取り入れて処理空気とし、顕熱交換器150で除湿後の処理空気と熱交換して予冷却したのち蒸発器240で露点温度以下に冷却して除湿し、除湿後の処理空気を前記顕熱交換器150で除湿前の処理空気と熱交換してレヒート加熱して室内に供給するとともに、凝縮器220において処理空気の冷却によって生じる蒸気圧縮式冷凍サイクルの放熱でプール水を加熱してプールに戻すことによって、室内の除湿と、プール水の加熱を同時に行っていた。そして、除湿した処理空気は主に、ペリメータ部分の窓や壁が結露しないように窓や壁に沿って、スリットダクトから室内に還流させていた。
【0004】
【発明が解決しようとする課題】
上記のような従来の技術においては、処理空気の状態変化は図8の湿り空気線図に示すようになる。すなわち、平均的なプール室内の環境である気温28〜30℃、相対湿度80〜90%の高湿度の室内から取り入れた処理空気(状態K)は、顕熱交換器150で除湿後の処理空気(状態M)と熱交換して予冷却(状態L)されたのち蒸発器240で露点温度以下に冷却除湿され(状態M)、除湿後の処理空気は前記顕熱交換器150で除湿前の処理空気と熱交換しレヒート加熱されて(状態N)室内に供給されている。従って、室内空気(状態K)と給気(状態N)との間には、ヒートバランスから、冷凍サイクルによって蒸発器240で状態Lから状態Mに冷却されるエンタルピ落差ΔQに等しいエンタルピ落差が生じる。すなわちエンタルピ落差ΔQだけ室内空間は冷房される。従って、ペリメータ部分のスリットダクトからは室内気温よりも低い気温の空気が供給されることになり、この部分にプールから上がった人が入ると肌寒く感じる問題があった。
【0005】
また、給気(状態N)によってペリメータの窓や壁の結露を防止するためには、外気の気温が低下するほど給気の露点温度(T1)を下げる必要があり、そのためには蒸発器240の冷却能力ΔQを外気温が低下するほど増加させることが必要になる。従って、外気温が下がるほど、室内(状態K)と給気(状態N)のエンタルピ落差即ち冷房効果が大きくなってペリメータ部分の肌寒く感じる不快感がさらに増す欠点があった。さらに、厳冬季に外気温が特に低くて露点温度を0℃近くまで下げる必要がある場合には、冷凍サイクルの蒸発温度が氷点下まで下がって、蒸発器240の伝熱面に霜が付いて連続運転が不能になる欠点があった。
【0006】
この発明は、上記課題に鑑みてなされたもので、冷房が不適当な状況下では、高湿度の室内から取り入れた空気を、処理空気と再生空気とに分岐し、処理空気はヒートポンプで冷却除湿したのちデシカントでさらに吸着除湿を行って乾球温度を室温よりも上げ、露点温度をさらに低下させた後、室内に供給するとともに、冷房が適当な状況下では、デシカントの作用を弱めるか、停止させつつ、冷房効果と除湿効果を発生させることによって、年間を通じて快適な環境を提供することができ、かつペリメータゾーンの結露防止能力が高く、かつ省エネルギな除湿空調システムを提供することを目的とする。
【0007】
【課題を解決するための手段】
本発明は上記目的を達成するためになされたもので、処理空気中の水分を吸着し再生空気によって再生されるデシカントと、処理空気を低熱源、再生空気を高熱源として動作するヒートポンプとを備え、室内空気を取り入れて、処理空気と再生空気とに分岐し、処理空気をヒートポンプの低熱源によって冷却除湿したのちデシカントで吸着除湿して室内に供給するとともに、再生空気をヒートポンプの高熱源で加熱したのちデシカントを通過させてデシカントを再生することを特徴とする除湿空調システムである。
【0008】
このように、高湿度の室内から取り入れた空気を、処理空気と再生空気とに分岐し、処理空気はヒートポンプで冷却除湿したのちデシカントでさらに吸着除湿を行って乾球温度を室温よりも上げた後、室内に供給することによって冷房作用による不快感がなくなり、かつ除湿能力が高くなり、かつ再生空気をヒートポンプからの放熱を再利用して加熱してデシカントを再生することによって省エネルギ効果が得られる。
【0009】
また、デシカント再生後の再生空気を乾燥用の温風として特定の箇所に供給することを特徴とする除湿空調システムである。このように、デシカント再生後であっても相対湿度が高くなく、しかも乾球温度が高い再生空気を温風として特定の箇所に供給することによって、乾燥用途に有効に活用できる。
【0010】
また、デシカント再生後の再生空気を屋外に排気することを特徴とする除湿空調システムである。このように、絶対湿度が室内及び室外よりも高いデシカント再生後の再生空気を屋外に排気することによって、室内の除湿作用を高くすることができる。
【0011】
また、本発明は、処理空気中の水分を吸着し再生空気によって再生されるデシカントと、圧縮機と、処理空気と熱交換する蒸発器と、デシカント再生前の再生空気と熱交換する第1の凝縮器と、再生空気以外の熱媒体と熱交換する第2の凝縮器とを有するヒートポンプとを備え、室内空気を取り入れて、少なくともその一部を処理空気として蒸発器で冷却除湿したのちデシカントを通過させて室内に供給するとともに、ヒートポンプの圧縮機によって圧縮した冷媒の一部を前記第1の凝縮器に導いて再生空気を加熱するとともに、圧縮した冷媒の他の一部を前記第2の凝縮器に導いて再生空気以外の熱媒体を加熱することを特徴とする除湿空調システムである。
【0012】
また、本発明は、処理空気中の水分を吸着し再生空気によって再生されるデシカントと、圧縮機と、処理空気と熱交換する蒸発器と、デシカント再生前の再生空気と熱交換する第1の凝縮器と、再生空気以外の熱媒体と熱交換する第2の凝縮器とを有するヒートポンプとを備え、室内空気を取り入れて、少なくともその一部を処理空気として蒸発器で冷却除湿するとともに、ヒートポンプの圧縮機によって圧縮した冷媒を前記第1の凝縮器に導いて再生空気を加熱してデシカントを再生し、冷却除湿した処理空気をデシカントで除湿したのち室内に供給する第1の運転形態と、圧縮した冷媒を前記第2の凝縮器に導いて再生空気以外の熱媒体を加熱することによって再生空気を加熱せず、冷却除湿した処理空気をデシカントで除湿せずに室内に供給する第2の運転形態と、ヒートポンプの圧縮機によって圧縮した冷媒の一部を前記第1の凝縮器に導いて再生空気を加熱して冷却除湿した処理空気をデシカントで除湿したのち室内に供給するとともに、圧縮した冷媒の他の一部を前記第2の凝縮器にも導いて再生空気以外の熱媒体を加熱する第3の運転形態とを選択的に運転可能であることを特徴とする除湿空調システムである。
【0013】
また、前記第2の運転形態の際に、再生空気の送風機を停止することを特徴とする除湿空調システムである。このように、冷房運転の際には再生空気の送風機を停止することによって省エネルギな運転ができる。
【0014】
また、前記室内空気は室内プールの空間内の空気であり、前記第2の凝縮器で熱交換する再生空気以外の熱媒体はプール水であることを特徴とする除湿空調システムである。このように、ヒートポンプからの放熱をプール水などの加熱にも用いることによって、デシカントの除湿能力を調節して処理空気の吸着熱による温度上昇を変化させ、必要に応じて冷房効果を発生させることができ、夏期においても空調空間を快適に保つことができる。
【0015】
また、デシカントで除湿後の処理空気を建物のペリメータゾーンに供給することを特徴とする除湿空調システムである。このように、最も湿度が下がりかつ乾球温度が高くなった処理空気をペリメータゾーンに送ることで、ペリメータゾーンの結露防止と不快感を防止することができる。
【0016】
また、ヒートポンプとして蒸気圧縮式ヒートポンプを用いることを特徴とする除湿空調システムである。また、ヒートポンプとして吸収式ヒートポンプを用いてもよい。
【0017】
【発明の実施の形態】
以下、本発明に係る除湿空調システムの実施の形態を図面を参照して説明する。図1は、本発明の参考例に係る除湿空調システムの設置状況を示す図である。図1において、室内プール40を囲む空調空間1には、図2に基本構成を示すような内部にデシカントを有する除湿空調機10を設置し、該除湿空調機10は空気取り入れ口12から室内空気を取り入れるようになっている。取り入れられた室内空気は、この除湿空調機10の内部では、処理空気と再生空気に分岐し、処理空気をデシカントで除湿し、除湿を行った処理空気の出口はダクト50を介して、窓20,25に隣接するペリメータに設置されたスリットダクト30,35に接続している。一方、該除湿空調機10のデシカントの再生を行った再生空気の出口14は、乾燥用の温風として空調空間に局所的に吹き出すよう構成している。また、該除湿空調機10の内部で冷却除湿によって発生するドレンは経路16を介して、排水溝60に接続するよう構成している。
【0018】
図2は図1に示した除湿空調機10の基本構成を示す説明図である。図2において、除湿空調機10は蒸気圧縮式ヒートポンプ及び処理空気と再生空気の2種類の空気系統とから構成されている。このうち蒸気圧縮式ヒートポンプの部分は、圧縮機260、低熱源熱交換器(蒸発器)240、高熱源熱交換器(凝縮器)220、膨張弁250を構成機器として蒸気圧縮式冷凍サイクルを構成したものである。そして低熱源熱交換器(蒸発器)240において低圧の冷媒蒸気がデシカント102通過前の処理空気と熱交換関係をなし、かつ高熱源熱交換器(凝縮器)220において高圧の冷媒蒸気がデシカント通過前の再生空気と熱交換関係をなすよう構成したものである。
【0019】
また、空気系統は次のように構成されている。デシカントロータ102は、デシカントが、処理空気経路Aと再生空気経路Bの双方に跨がってアクチュエータ103の作用によって所定のサイクルで回転するよう構成されている。処理空気経路Aは、空調空間1と低熱源熱交換器(蒸発器)240と経路110を介して接続し、低熱源熱交換器(蒸発器)240の処理空気の出口は室内空気導入用の送風機101の吸い込み口と経路111を介して接続し、送風機102の吐出口はデシカントロータ102の水分吸着工程を行う第1の区画と経路112を介して接続し、デシカントロータ102の処理空気の出口は給気口(図1中の符号50で示す)となる処理空気出口と経路113を介して接続して形成する。
【0020】
一方、再生空気経路Bは、空調空間1と高熱源熱交換器(凝縮器)220とを経路120を介して接続し、再生空気の高熱源熱交換器(凝縮器)220の出口は室内空気導入用の送風機140の吸い込み口と経路121を介して接続し、送風機140の吐出口はデシカントロータ102の再生空気の再生工程を行う第2の区画と経路122を介して接続し、デシカントロータ102の再生空気の再生工程を行う第2の区画の再生空気の出口は室内空間の局所的吹き出し口(図1中の符号14で示す)と経路123を介して接続して再生空気の経路を形成する。なお図中、丸で囲ったアルファベットK〜Sは、図3と対応する空気の状態を示す記号である。
【0021】
上述のように構成された除湿空調機10の蒸気圧縮式冷凍サイクル部分のサイクルを次に説明する。冷媒は低熱源熱交換器(蒸発器)240で処理空気から蒸発潜熱を奪って蒸発し(状態a:約10℃、4.2kg/cm2)、経路206を経て圧縮機260に吸引され圧縮される。圧縮された冷媒(状態b:約80℃、19.3kg/cm2)は経路202を経て高熱源熱交換器(凝縮器)220に流入し冷媒の過熱蒸気の顕熱および凝縮潜熱をデシカント102に流入前の再生空気に放出して凝縮した(状態c:約65℃、19.3kg/cm2)のち経路203を経て膨張弁250に至りそこで減圧膨張した(状態d:約10℃、4.2kg/cm2)後、経路205を経て低熱源熱交換器(蒸発器)240に還流する。このように蒸気圧縮式冷凍サイクル部分のサイクルは、従来ルームエアコン等の空調分野で通常行われているものと技術上大きな差異はなく、作用温度と圧力のみが異なる。
【0022】
次に、前述のように構成されたヒートポンプを熱源とする除湿空調機10の動作を図3の湿り空気線図を参照して説明する。室内空気から導入され分岐された処理空気(状態K)は経路110を経て低熱源熱交換器(蒸発器)240に至り、ヒートポンプの作用により冷却除湿され乾球温度および絶対湿度が低下する(状態L)。冷却除湿された処理空気は送風機101に吸引され昇圧され、経路112 を経てデシカントロータ102の水分吸着工程を行う第1の区画 に送られ、デシカントロータ102の吸湿剤で空気中の水分を吸着されて更に絶対湿度が低下するとともに吸着熱によって空気は温度上昇する(状態M)。絶対湿度が下がり温度が上昇した空気は、経路113を経て給気として空調空間のペリメータに送られる。なお、低熱源熱交換器(蒸発器)で冷却除湿される際に処理空気から分離された結露水(ドレン)は、ドレンパン245に集められ、図1に示した経路16を経て、排水溝60に捨てられる。
【0023】
一方、デシカントロータ102の再生は次のように行われる。室内空気から導入され分岐された再生空気(状態K)は経路120を経て高熱源熱交換器(凝縮器)220に至り、ここで冷媒蒸気によって加熱されて温度上昇し(状態R)、経路121を経て送風機140 に吸引され昇圧され、経路122を経てデシカントロータ102の再生工程を行う第2の区画を通過してデシカントロータ102の水分を除去し再生作用を行い(状態S)、経路123を経て、室内空間1の局所的吹き出し口(図1中の符号14で示す)から室内に戻される。
【0024】
このようにして、処理空気の冷却除湿およびデシカントによる吸着除湿とデシカントの再生をくりかえし行うことによって、除湿運転を行うことができるが、この際、室内に供給される空気の状態は、従来技術と比べて大きく異なる。この点について以下に説明する。
【0025】
平均的なプール室内の環境である気温28〜30℃、相対湿度80〜90%の高湿度の室内から取り入れた処理空気(状態K)は、蒸発器240で露点温度(24〜28℃)以下に冷却除湿され(状態L)、乾球温度が低下し(15〜20℃)、絶対湿度が低下する(11〜15 g/kg)。この状態では処理空気の露点温度はヒートポンプの低熱源温度(蒸発温度)よりも高くなるが、さらにデシカントロータ102の除湿剤によって吸着除湿することにより、湿り空気線図では、ほぼ等エンタルピ線上を移動して乾球温度が上昇する(35〜40℃)とともに、絶対湿度も低下(3.5〜6g/kg)する。
【0026】
このようにして得られる処理空気は気温が室内よりも高く、また露点温度は蒸発温度より大幅に低くなり(0〜6℃)かつ露点と乾球温度との温度差が大きい。従って、このように除湿された空気を、図1に示すようなペリメータのスリットダクトから吹き出すことによって、外気温度が低くても、窓等の外壁部に結露を生じにくくなり、また、スリットダクトから吹き出す空気の噴流内にプールから上がった人が入っても、乾球温度が高いため肌寒く感じないで済む。また、厳冬季に外気温が特に低くて露点温度を0℃近くまで下げる必要がある場合でも、冷凍サイクルの蒸発温度を氷点下まで下げる必要がなく、従って蒸発器240の伝熱面に霜が付かず連続運転が可能になる。
【0027】
さらに、デシカント再生後の再生空気は、絶対湿度は上昇する(25〜30g/kg)ものの、乾球温度が高い(40〜45℃)ため、相対湿度が50%前後となり、乾燥用の温風としても利用できるので、プールから上がった人のためにスポット風として、局所的に供給してもよく、また室内からの除湿能力を高めたい場合には外部に排気し、代りに絶対湿度の低い外気を取り入れても差し支えない。また図4の設置形態のように、デシカントを出た再生空気をダクト14、給気口71を介して、乾燥用の部屋70に供給したのち、排気口72から外部に排気しても差し支えない。また、排気と取り入れる外気との間に顕熱熱交換器を用いても差し支えない。このように再生空気も乾燥用として利用することができる。
【0028】
次に、本実施の形態のエネルギ効率について説明する。本実施の形態では、図3において、冷却除湿して処理空気から取り出した熱量(ΔQ)は外部にそのまま捨てずに、ヒートポンプで昇温して再生空気の加熱に用いるため、熱の多重効用化が図れる。すなわち、ヒートポンプの駆動エネルギ(圧縮機入力)はまず冷却除湿効果を発生させ、その時取り出した熱とヒートポンプの駆動エネルギ(圧縮機入力)は熱エネルギとして再生空気の加熱に再度用いられて、デシカントによる吸着除湿効果を発生する。従って、ヒートポンプの駆動エネルギ(圧縮機入力)が少なくて済み、省エネルギ効果がある。本実施の形態ではヒートポンプとして蒸気圧縮式ヒートポンプを事例として示したが、吸収ヒートポンプを用いても同様の省エネルギ効果が得られる。
【0029】
図5は本発明に係る除湿空調システムの設置形態を示す図であり、図6は図5中に示した除湿空調機10の基本構成を示す説明図である。この実施の形態では、除湿空調機10は、圧縮機260と、処理空気と熱交換する蒸発器240と、デシカント再生前の再生空気と熱交換する第1の凝縮器220と、プール水と熱交換する第2の凝縮器230とを有するヒートポンプとを備えている。これにより、室内空気を取り入れて、少なくともその一部を処理空気として蒸発器240で冷却除湿したのちデシカントを通過させて室内に供給するとともに、ヒートポンプの圧縮機260によって圧縮した冷媒の一部を前記第1の凝縮器220に導いて再生空気を加熱するとともに、圧縮した冷媒の他の一部を前記第2の凝縮器230にも導いてプール水を加熱するようにしている。そして、図5に示すように、除湿空調機10の第2の凝縮器230には経路17,18を介してプール水が流動して冷媒と熱交換するようになっている。
【0030】
また、本実施の形態では、制御機器としてコントローラ301を設け、該コントローラ301は、室内空間の温度湿度の状態や外気温度を検出して、冷房または暖房の負荷状況を判断している。これにより、冷媒の流量調節用の3方弁270及びデシカントロータ102のアクチュエータ103及び各送風機101、140を制御して、参考例に係る実施の形態で示した、冷房効果がなく肌寒さを感じない運転形態のみでなく、状況に応じて、適度な冷房効果を発生させることができるようになっている。
【0031】
以下に、上記の実施の形態の除湿空調システムの作用について説明する。まず、第1の運転形態においては、冷媒の流量調節用の3方弁270の経路207側を閉じて、全ての冷媒を第1の凝縮器220に導くようにするが、この場合には、参考例に係る実施の形態と同じになるので、説明を省略する。
【0032】
次に、冷媒の流量調節用の3方弁270の経路202側を閉じて、全ての冷媒を第2の凝縮器20に導く第2の運転形態について説明する。この場合、第1の凝縮器220は作用せず、従って再生空気が加熱されないので、デシカントを再生することができないため、デシカントの除湿作用がなくなり、処理空気は吸着除湿されない。従って、図3の湿り空気線図の状態Mと状態Lが等しくなって、給気が室温よりも低くなり、図7に示した従来例と同様に冷房作用が得られる。このような第2の運転形態は、夏期など冷房することが適当な時期に用いる。なお、プール水の温度が上昇して好ましくない場合には、冷却水を用いて外部のクーリングタワーに第2の凝縮器20の熱を排出しても差し支えなく、また第2の凝縮器を空冷式として、外部に設置しても差し支えない。また、再生空気を流動させる必要がない場合には、省エネルギのためコントローラ301によって、送風機140およびデシカントロータ102のアクチュエータ103を停止させても差し支えない。
【0033】
次に、冷媒の流量調節用の3方弁270の経路202側および経路207側を両方開けて、第1の凝縮器220および第2の凝縮器20を共に作用させる第3の運転形態について説明する。この場合、第1の凝縮器220における再生空気への加熱作用が弱くなり、従ってデシカントの除湿能力が低下し、処理空気の吸着除湿作用が低下して図3における状態Mが状態Lに近づき、処理空気の出口の乾球温度が第1の運転形態よりも低くなる。従って、第1の運転形態と第2の運転形態の中間的な冷房効果を抑制した運転が可能である。従って、中間期にも、快適な室内環境が得られる。
【0034】
このように、暖房が必要な時期にはデシカントを作動させて乾球温度を室温よりも上げた後、室内に供給することによって冷房作用を防止しかつ省エネルギな運転形態ができるほか、冷房が必要な時期にはヒートポンプからの放熱をプール水の加熱に用いることによって、デシカントの除湿能力を停止して処理空気の吸着熱による温度上昇を止め、冷房効果を発生させる運転形態を採ることができ、またその中間的運転形態も採ることができるので、年間を通じて室内プール施設の空調空間を快適に保つことができる。
【0035】
【発明の効果】
以上説明したように、本発明によれば、冷房が不適当な状況下では、高湿度の室内から取り入れた空気を、処理空気と再生空気とに分岐し、処理空気はヒートポンプで冷却除湿したのちデシカントでさらに吸着除湿を行って乾球温度を室温よりも上げ、露点温度をさらに低下させた後、室内に供給するとともに、冷房が適当な状況下では、デシカントの作用を弱めるか、停止させつつ、冷房効果と除湿効果を発生させることによって、年間を通じて、快適で、かつペリメータゾーンの結露防止能力が高く、かつ省エネルギな除湿空調システムを提供することができる。
【図面の簡単な説明】
【図1】 本発明の参考例に係る除湿空調システムの基本構成を示す説明図である。
【図2】図1に示した除湿空調機の基本構成を示す説明図である。
【図3】ヒートポンプを熱源とする除湿空調機の動作を説明する湿り空気線図である。
【図4】図1に示す除湿空調システムの変形例を示す説明図である。
【図5】 本発明に係る除湿空調システムの実施の形態を示す説明図である。
【図6】図5に示した除湿空調機の基本構成を示す説明図である。
【図7】従来の除湿空調機を示す説明図である。
【図8】図7に示す除湿空調機の動作を説明する湿り空気線図である。
【符号の説明】
1 空調空間
10 除湿空調機
12 空気取り入れ口
30,35 スリットダクト
40 室内プール
101 送風機
102 デシカントロータ
220 高熱源熱交換器(凝縮器)
240 低熱源熱交換器(蒸発器)
250 膨張弁
260 圧縮機
A 処理空気経路
B 再生空気経路
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a dehumidification air-conditioning system, particularly a dehumidification air-conditioning system for dehumidifying a high-humidity space such as an indoor pool facility, etc., performing cooling dehumidification by a heat pump and adsorption dehumidification by a desiccant, and releasing heat from the heat pump. It is related with the air-conditioning system which enabled the reproduction | regeneration processing of a desiccant continuously by this.
[0002]
[Prior art]
FIG. 7 is a conventional technique that is widely used in the United States as a dehumidifying device for the interior space of an indoor pool facility. The refrigerant path A forming the vapor compression refrigeration cycle and the evaporator 240 exchange heat with the refrigerant path A, and the indoor air is taken in with the blower 101 and the sensible heat exchanger 150 as main components, cooled and dehumidified, and returned to the room. A processing air path B and a water path C that exchanges heat with the refrigerant path A by the condenser 220 to take in pool water and heat it to return to the pool.
[0003]
As a result, high-humidity air in the pool room is taken in as processing air, pre-cooled by heat exchange with the processing air after dehumidification in the sensible heat exchanger 150, and then cooled to the dew point temperature or lower in the evaporator 240 to dehumidify. In the vapor compression refrigeration cycle generated by cooling the processing air in the condenser 220, the processing air after dehumidification is heat-exchanged with the processing air before dehumidification by the sensible heat exchanger 150 and reheated and heated. Heating the pool water with heat dissipation and returning it to the pool simultaneously dehumidifies the room and heats the pool water. The dehumidified process air was mainly recirculated from the slit duct into the room along the windows and walls so that the windows and walls of the perimeter portion did not condense.
[0004]
[Problems to be solved by the invention]
In the conventional technique as described above, the state change of the processing air is as shown in the wet air diagram of FIG. That is, the processing air (state K) taken from a high-humidity room with an average pool room temperature of 28-30 ° C. and a relative humidity of 80-90% is treated air after dehumidification by the sensible heat exchanger 150. (State M) is pre-cooled (State L) and cooled and dehumidified below the dew point temperature by the evaporator 240 (State M). The treated air after dehumidification is dehumidified by the sensible heat exchanger 150 before being dehumidified. The heat is exchanged with the process air, reheated (state N), and supplied to the room. Therefore, an enthalpy drop equal to the enthalpy drop ΔQ that is cooled from the state L to the state M in the evaporator 240 by the refrigeration cycle occurs between the indoor air (state K) and the supply air (state N) due to the heat balance. . That is, the indoor space is cooled by the enthalpy drop ΔQ. Accordingly, air having a temperature lower than the room temperature is supplied from the slit duct of the perimeter portion, and there is a problem that it feels chilly when a person who goes up from the pool enters this portion.
[0005]
Further, in order to prevent dew condensation on the windows and walls of the perimeter due to the supply air (state N), it is necessary to lower the dew point temperature (T1) of the supply air as the outside air temperature decreases. It is necessary to increase the cooling capacity ΔQ as the outside air temperature decreases. Accordingly, there is a drawback that the enthalpy drop, that is, the cooling effect between the room (state K) and the air supply (state N) increases as the outside air temperature decreases, and the discomfort of the perimeter portion that feels chilly further increases. Further, when the outside air temperature is particularly low in the severe winter season and the dew point temperature needs to be lowered to near 0 ° C., the evaporation temperature of the refrigeration cycle is lowered below the freezing point, and the heat transfer surface of the evaporator 240 is continuously frosted. There was a fault that made driving impossible.
[0006]
The present invention has been made in view of the above-described problems. Under circumstances where cooling is inappropriate, air taken from a room with high humidity is branched into treated air and regenerated air, and the treated air is cooled and dehumidified by a heat pump. Then, after further dehumidification with a desiccant, the dry bulb temperature is raised above room temperature, the dew point temperature is further lowered, and then supplied to the room, and if the cooling is appropriate, the desiccant action is weakened or stopped. The purpose is to provide a dehumidifying air conditioning system that can provide a comfortable environment throughout the year by generating a cooling effect and a dehumidifying effect, and has a high dew condensation prevention capability in the perimeter zone and is energy saving. To do.
[0007]
[Means for Solving the Problems]
The present invention has been made in order to achieve the above object, a desiccant that is regenerated by adsorbing moisture in the processed air regenerating air, the process air low-temperature heat source, and a heat pump to operate the regeneration air as a high heat source It takes indoor air, branches it into treated air and regenerated air, cools and dehumidifies the treated air with a low heat source of the heat pump, adsorbs and dehumidifies with a desiccant, and supplies the regenerated air with a high heat source of the heat pump. A dehumidifying air-conditioning system which regenerates a desiccant by passing the desiccant after heating.
[0008]
In this way, air taken from a room with high humidity is branched into treated air and regenerated air. The treated air is cooled and dehumidified with a heat pump, and then adsorbed and dehumidified with a desiccant to raise the dry bulb temperature above room temperature. Later, by supplying it indoors, there is no discomfort due to the cooling action, the dehumidifying ability is increased, and the desiccant is regenerated by heating the regenerated air by reusing heat released from the heat pump, thereby obtaining an energy saving effect. It is done.
[0009]
Also, a dehumidifying air-conditioning system that is characterized in that the supply to the specific location of the regeneration air after the desiccant regeneration as hot air for drying. In this way, even after the desiccant regeneration, by supplying the regenerated air having a high relative humidity and a high dry bulb temperature as a warm air to a specific location, it can be effectively used for a drying application.
[0010]
Also, a dehumidifying air-conditioning system that is characterized in that exhausting the regeneration air after desiccant regeneration outdoors. In this way, the indoor dehumidifying action can be enhanced by exhausting the regenerated air after the regeneration with the desiccant whose absolute humidity is higher than that in the room and outdoors to the outside.
[0011]
The present invention also includes a desiccant that adsorbs moisture in the processing air and is regenerated by the regenerating air, a compressor, an evaporator that exchanges heat with the processing air, and a first that exchanges heat with the regenerating air before desiccant regeneration. A heat pump having a condenser and a second condenser for exchanging heat with a heat medium other than the regeneration air, taking in indoor air, cooling and dehumidifying at least part of it as treated air with an evaporator, and then desiccant A part of the refrigerant compressed by the compressor of the heat pump is led to the first condenser to heat the regeneration air and the other part of the compressed refrigerant is supplied to the second A dehumidifying air-conditioning system that heats a heat medium other than regenerated air by guiding it to a condenser.
[0012]
The present invention also includes a desiccant that adsorbs moisture in the processing air and is regenerated by the regenerating air, a compressor, an evaporator that exchanges heat with the processing air, and a first that exchanges heat with the regenerating air before desiccant regeneration. A heat pump having a condenser and a second condenser for exchanging heat with a heat medium other than the regeneration air, taking in indoor air, cooling and dehumidifying at least a part thereof as processing air with an evaporator, and a heat pump A first operation mode in which the refrigerant compressed by the compressor is guided to the first condenser to regenerate the desiccant by heating the regenerated air, and the cooled and dehumidified treated air is dehumidified by the desiccant and then supplied into the room; The compressed refrigerant is guided to the second condenser to heat the heat medium other than the regenerated air, so that the regenerated air is not heated, and the cooled and dehumidified treated air is not dehumidified by the desiccant Second operation mode to be supplied, and a part of the refrigerant compressed by the compressor of the heat pump is led to the first condenser, and the regenerated air is heated and cooled and dehumidified, and then dehumidified by the desiccant and supplied to the room both the you that, characterized by a third operating configuration in which another portion of the compressed refrigerant also led to the second condenser to heat the heat medium other than the regeneration air can be selectively operated It is a dehumidifying air conditioning system.
[0013]
Further, when the second operating mode, a dehumidifying air-conditioning system that is characterized in that to stop the blower regeneration air. In this way, energy-saving operation can be performed by stopping the blower of regenerated air during the cooling operation.
[0014]
Further, the indoor air is air in the space of an indoor pool, a heat medium other than the regeneration air exchanges heat with the second condenser are dehumidifying air-conditioning system that is characterized in that a pool water. In this way, heat dissipation from the heat pump is also used for heating pool water etc., thereby adjusting the dehumidifying capacity of the desiccant to change the temperature rise due to the heat of adsorption of the processing air and generating a cooling effect as necessary The air-conditioned space can be kept comfortable even in summer.
[0015]
Also, a dehumidifying air-conditioning system that is characterized in that supplying process air after dehumidification by a desiccant in building perimeter zone. In this way, by sending the processed air having the lowest humidity and the highest dry bulb temperature to the perimeter zone, it is possible to prevent dew condensation and discomfort in the perimeter zone.
[0016]
Also, a dehumidifying air-conditioning system that is characterized by using a vapor compression heat pump as a heat pump. An absorption heat pump may be used as the heat pump .
[0017]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of a dehumidifying air conditioning system according to the present invention will be described with reference to the drawings. Figure 1 is a diagram illustrating a particular installation of the dehumidifying air-conditioning system according to a reference example of the present invention. In FIG. 1, a dehumidifying air conditioner 10 having a desiccant is installed in the air-conditioned space 1 surrounding the indoor pool 40 as shown in FIG. 2, and the dehumidifying air conditioner 10 is connected to the indoor air through the air intake 12. Has come to be adopted. The taken-in indoor air is branched into treated air and regenerated air inside the dehumidifying air conditioner 10, the treated air is dehumidified with a desiccant, and the outlet of the treated air that has been dehumidified passes through the duct 50 through the window 20. , 25 are connected to slit ducts 30, 35 installed in the perimeter adjacent to each other. On the other hand, the outlet 14 of the regenerated air that has regenerated the desiccant of the dehumidifying air conditioner 10 is configured to blow out locally to the conditioned space as hot air for drying. Further, the drain generated by the cooling and dehumidification inside the dehumidifying air conditioner 10 is configured to be connected to the drainage groove 60 via the path 16.
[0018]
FIG. 2 is an explanatory diagram showing a basic configuration of the dehumidifying air conditioner 10 shown in FIG. In FIG. 2, the dehumidifying air conditioner 10 includes a vapor compression heat pump and two types of air systems, that is, processing air and regeneration air. Among these components, the vapor compression heat pump portion constitutes a vapor compression refrigeration cycle with the compressor 260, the low heat source heat exchanger (evaporator) 240, the high heat source heat exchanger (condenser) 220, and the expansion valve 250 as components. It is a thing. In the low heat source heat exchanger (evaporator) 240, the low pressure refrigerant vapor has a heat exchange relationship with the processing air before passing through the desiccant 102, and in the high heat source heat exchanger (condenser) 220, the high pressure refrigerant vapor passes through the desiccant. It is configured to have a heat exchange relationship with the previous regeneration air.
[0019]
The air system is configured as follows. The desiccant rotor 102 is configured such that the desiccant rotates in a predetermined cycle by the action of the actuator 103 across both the processing air path A and the regeneration air path B. The processing air path A is connected to the air-conditioned space 1 and the low heat source heat exchanger (evaporator) 240 via the path 110, and the processing air outlet of the low heat source heat exchanger (evaporator) 240 is for introducing indoor air. The suction port of the blower 101 is connected via a path 111, and the discharge port of the blower 102 is connected via a path 112 to the first section that performs the moisture adsorption process of the desiccant rotor 102, and the outlet of the processing air of the desiccant rotor 102 Is formed by being connected to a processing air outlet serving as an air supply port (indicated by reference numeral 50 in FIG. 1) via a path 113.
[0020]
On the other hand, the regeneration air path B connects the air-conditioned space 1 and the high heat source heat exchanger (condenser) 220 via the path 120, and the outlet of the high temperature heat source heat exchanger (condenser) 220 for the regeneration air is the room air. The suction port of the blower 140 for introduction is connected via the path 121, and the discharge port of the blower 140 is connected via the path 122 to the second section for performing the regeneration air regeneration process of the desiccant rotor 102, and the desiccant rotor 102 is connected. The regeneration air outlet of the second section for performing the regeneration air regeneration step is connected to a local outlet (indicated by reference numeral 14 in FIG. 1) of the indoor space via a path 123 to form a regeneration air path. To do. In the figure, alphabets K to S surrounded by circles are symbols indicating air states corresponding to FIG.
[0021]
Next, the cycle of the vapor compression refrigeration cycle portion of the dehumidifying air conditioner 10 configured as described above will be described. The refrigerant takes the latent heat of vaporization from the processing air in the low heat source heat exchanger (evaporator) 240 and evaporates (state a: about 10 ° C., 4.2 kg / cm 2 ), and is sucked and compressed by the compressor 260 via the path 206. Is done. The compressed refrigerant (state b: about 80 ° C., 19.3 kg / cm 2 ) flows into the high heat source heat exchanger (condenser) 220 via the path 202 and the sensible heat and latent heat of condensation of the refrigerant are desiccant 102. After being discharged into the regenerated air before flowing in and condensed (state c: about 65 ° C., 19.3 kg / cm 2 ), it reached the expansion valve 250 via the path 203 and expanded under reduced pressure (state d: about 10 ° C., 4 After 2 kg / cm 2 ), the refrigerant is refluxed to the low heat source heat exchanger (evaporator) 240 via the path 205. As described above, the cycle of the vapor compression refrigeration cycle portion is not technically different from that conventionally performed in the air conditioning field such as a room air conditioner, and only the working temperature and pressure are different.
[0022]
Next, the operation of the dehumidifying air conditioner 10 using the heat pump configured as described above as a heat source will be described with reference to the wet air diagram of FIG. The process air (state K) branched from the indoor air reaches the low heat source heat exchanger (evaporator) 240 via the path 110, is cooled and dehumidified by the action of the heat pump, and the dry bulb temperature and absolute humidity are reduced (state). L). The cooled and dehumidified process air is sucked into the blower 101 and pressurized, and is sent to the first section where the moisture adsorption process of the desiccant rotor 102 is performed via the path 112, and moisture in the air is adsorbed by the desiccant rotor 102. As the absolute humidity further decreases, the temperature of the air increases due to the heat of adsorption (state M). The air whose absolute humidity is decreased and whose temperature is increased is sent to the perimeter of the air-conditioned space as supply air via the path 113. Condensed water (drain) separated from the processing air when being cooled and dehumidified by the low heat source heat exchanger (evaporator) is collected in the drain pan 245 and passes through the path 16 shown in FIG. Thrown away.
[0023]
On the other hand, regeneration of the desiccant rotor 102 is performed as follows. The regenerative air introduced from the indoor air and branched (state K) reaches the high heat source heat exchanger (condenser) 220 via the path 120 where it is heated by the refrigerant vapor to rise in temperature (state R). Through the second section where the regeneration process of the desiccant rotor 102 is performed through the path 122 to remove the moisture of the desiccant rotor 102 and perform the regeneration action (state S). Then, it returns to the room from a local outlet (indicated by reference numeral 14 in FIG. 1) of the indoor space 1.
[0024]
In this way, the dehumidifying operation can be performed by repeatedly performing the cooling dehumidification of the processing air and the adsorption dehumidification by the desiccant and the regeneration of the desiccant. At this time, the state of the air supplied to the room is the same as that of the prior art. It is very different. This will be described below.
[0025]
Processed air (state K) taken from a room with a high humidity of an average pool room temperature of 28-30 ° C. and a relative humidity of 80-90% is dew point temperature (24-28 ° C.) or less in the evaporator 240. To dehumidify (state L), the dry bulb temperature decreases (15 to 20 ° C.), and the absolute humidity decreases (11 to 15 g / kg). In this state, the dew point temperature of the processing air is higher than the low heat source temperature (evaporation temperature) of the heat pump, but further moves on the isenthalpy line in the humid air diagram by adsorbing and dehumidifying with the desiccant rotor 102 dehumidifying agent. As the dry bulb temperature rises (35-40 ° C.), the absolute humidity also drops (3.5-6 g / kg).
[0026]
The treated air thus obtained has a higher temperature than indoors, the dew point temperature is significantly lower than the evaporation temperature (0 to 6 ° C.), and the temperature difference between the dew point and the dry bulb temperature is large. Therefore, by blowing out the air thus dehumidified from the slit duct of the perimeter as shown in FIG. 1, even if the outside air temperature is low, it becomes difficult for condensation to occur on the outer wall portion such as a window. Even if a person who goes up from the pool enters the jet of air that blows out, the dry bulb temperature is high and it doesn't feel chilly. Further, even when the outside air temperature is particularly low and the dew point temperature needs to be lowered to near 0 ° C. in the severe winter season, it is not necessary to lower the evaporation temperature of the refrigeration cycle below the freezing point, so that the heat transfer surface of the evaporator 240 is frosted. However, continuous operation is possible.
[0027]
Furthermore, the regeneration air after desiccant regeneration has an absolute humidity rise (25-30 g / kg), but the dry bulb temperature is high (40-45 ° C.), so the relative humidity is around 50%, and the warm air for drying. It can also be used as a spot wind for people who have risen from the pool, and if you want to increase the dehumidifying capacity from the room, exhaust it to the outside and instead have a low absolute humidity There is no problem in taking outside air. Further, as in the installation form of FIG. 4, the regeneration air that has exited the desiccant may be supplied to the drying room 70 through the duct 14 and the air supply port 71 and then exhausted to the outside from the exhaust port 72. . Further, a sensible heat exchanger may be used between the exhaust and the outside air taken in. Thus, the regeneration air can also be used for drying.
[0028]
Next, the energy efficiency of this embodiment will be described. In this embodiment, in FIG. 3, the heat quantity (ΔQ) extracted from the processing air by cooling and dehumidification is not thrown away to the outside, but is used for heating the regeneration air by raising the temperature with a heat pump. Can be planned. That is, the drive energy (compressor input) of the heat pump first generates a cooling and dehumidifying effect, and the heat extracted at that time and the drive energy (compressor input) of the heat pump are reused as heat energy for heating the regenerative air, and by the desiccant Adsorption dehumidification effect is generated. Therefore, the drive energy (compressor input) of the heat pump can be reduced, and there is an energy saving effect. In this embodiment, a vapor compression heat pump is shown as an example of the heat pump, but the same energy saving effect can be obtained even if an absorption heat pump is used.
[0029]
Figure 5 is a diagram showing an Installation form of dehumidifying air-conditioning system according to the present invention, FIG. 6 is an explanatory view showing a basic structure of a dehumidifying air conditioner 10 shown in FIG. In this embodiment, the dehumidifying air conditioner 10 includes a compressor 260, an evaporator 240 that exchanges heat with the processing air, a first condenser 220 that exchanges heat with the regenerated air before desiccant regeneration, pool water, and heat. And a heat pump having a second condenser 230 to be replaced. As a result, the indoor air is taken in, and at least a part of the refrigerant is cooled and dehumidified by the evaporator 240 and then supplied to the room through the desiccant, and a part of the refrigerant compressed by the compressor 260 of the heat pump is supplied to the room. The regeneration air is heated by being led to the first condenser 220, and the pool water is heated by guiding another part of the compressed refrigerant to the second condenser 230. As shown in FIG. 5, the pool water flows to the second condenser 230 of the dehumidifying air conditioner 10 via paths 17 and 18 so as to exchange heat with the refrigerant.
[0030]
Further, in the present embodiment, a controller 301 is provided as a control device, and the controller 301 detects the temperature / humidity state of the indoor space and the outside air temperature to determine the load condition of cooling or heating. As a result, the three-way valve 270 for adjusting the flow rate of the refrigerant, the actuator 103 of the desiccant rotor 102 and the fans 101 and 140 are controlled, and there is no cooling effect as shown in the embodiment according to the reference example , and the user feels chilly. It is possible to generate an appropriate cooling effect depending on the situation as well as no operation mode.
[0031]
Below, an effect | action of the dehumidification air conditioning system of said embodiment is demonstrated. First, in the first operation mode, the path 207 side of the three-way valve 270 for adjusting the flow rate of the refrigerant is closed so that all the refrigerant is guided to the first condenser 220. In this case, Since it becomes the same as embodiment which concerns on a reference example , description is abbreviate | omitted.
[0032]
Next, a second operation mode in which the route 202 side of the three-way valve 270 for adjusting the refrigerant flow rate is closed and all the refrigerant is guided to the second condenser 2 30 will be described. In this case, the first condenser 220 does not act, and therefore the regeneration air is not heated, so that the desiccant cannot be regenerated. Therefore, the desiccant dehumidification action is lost, and the processing air is not adsorbed and dehumidified. Accordingly, the state M and the state L in the wet air diagram of FIG. 3 become equal, the supply air becomes lower than room temperature, and the cooling action is obtained as in the conventional example shown in FIG. Such a second mode of operation is used when it is appropriate to cool, such as in summer. If the temperature of the pool water rises and it is not desirable, the cooling water can be used to discharge the heat of the second condenser 2 30 to the external cooling tower, and the second condenser can be It can be installed outside as an air-cooled type. When there is no need to flow the regenerated air, the controller 301 may stop the blower 140 and the actuator 103 of the desiccant rotor 102 by the controller 301 for energy saving.
[0033]
Next, a third operation mode in which the first condenser 220 and the second condenser 2 30 are operated together by opening both the path 202 side and the path 207 side of the three-way valve 270 for adjusting the refrigerant flow rate. Will be described. In this case, the heating action on the regenerated air in the first condenser 220 is weakened, so the desiccant dehumidifying ability is reduced, the adsorption dehumidifying action of the processing air is lowered, and the state M in FIG. The dry bulb temperature at the outlet of the processing air is lower than that in the first operation mode. Therefore, an operation that suppresses an intermediate cooling effect between the first operation mode and the second operation mode is possible. Therefore, a comfortable indoor environment can be obtained even in the intermediate period.
[0034]
In this way, when the heating is necessary, the desiccant is operated to raise the dry bulb temperature above room temperature, and then the air is supplied to the room to prevent the cooling action and to achieve an energy saving operation form. When necessary, heat dissipation from the heat pump can be used to heat the pool water, so that the desiccant's dehumidifying capacity is stopped, the temperature rise due to the adsorption heat of the processing air is stopped, and the cooling mode is generated. In addition, since the intermediate operation mode can be adopted, the air-conditioned space of the indoor pool facility can be kept comfortable throughout the year.
[0035]
【The invention's effect】
As described above, according to the present invention, under conditions where cooling is inappropriate, air taken from a room with high humidity is branched into treated air and regenerated air, and the treated air is cooled and dehumidified with a heat pump. After further adsorption dehumidification with a desiccant to raise the dry bulb temperature above room temperature and further lower the dew point temperature, it is supplied to the room and, under appropriate conditions of cooling, weakens or stops the action of the desiccant. By generating the cooling effect and the dehumidifying effect, it is possible to provide a dehumidifying air conditioning system that is comfortable throughout the year, has a high dew condensation prevention capability in the perimeter zone, and is energy saving.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a basic structure of a dehumidifying air-conditioning system according to a reference example of the present invention.
FIG. 2 is an explanatory diagram showing a basic configuration of the dehumidifying air conditioner shown in FIG.
FIG. 3 is a moist air diagram illustrating the operation of a dehumidifying air conditioner using a heat pump as a heat source.
4 is an explanatory view showing a modification of the dehumidifying air conditioning system shown in FIG. 1. FIG.
5 is an explanatory diagram showing a form of implementation of the dehumidifying air-conditioning system according to the present invention.
6 is an explanatory diagram showing a basic configuration of the dehumidifying air conditioner shown in FIG. 5. FIG.
FIG. 7 is an explanatory view showing a conventional dehumidifying air conditioner.
8 is a moist air diagram illustrating the operation of the dehumidifying air conditioner shown in FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Air-conditioned space 10 Dehumidification air conditioner 12 Air intake port 30, 35 Slit duct 40 Indoor pool 101 Blower 102 Desiccant rotor 220 High heat source heat exchanger (condenser)
240 Low heat source heat exchanger (evaporator)
250 Expansion valve 260 Compressor A Process air path B Regenerative air path

Claims (4)

処理空気中の水分を吸着し再生空気によって再生されるデシカントと、圧縮機と、処理空気と熱交換する蒸発器と、デシカント再生前の再生空気と熱交換する第1の凝縮器と、再生空気以外の熱媒体と熱交換する第2の凝縮器とを有するヒートポンプとを備え、
室内空気を取り入れて、少なくともその一部を処理空気として蒸発器で冷却除湿したのちデシカントを通過させて室内に供給するとともに、ヒートポンプの圧縮機によって圧縮した冷媒の一部を前記第1の凝縮器に導いて再生空気を加熱するとともに、圧縮した冷媒の他の一部を前記第2の凝縮器に導いて再生空気以外の熱媒体を加熱することを特徴とする除湿空調システム。
A desiccant that absorbs moisture in the processing air and is regenerated by the regenerating air, a compressor, an evaporator that exchanges heat with the processing air, a first condenser that exchanges heat with the regenerating air before the desiccant regeneration, and the regenerating air A heat pump having a second condenser that exchanges heat with a heat medium other than
After taking in indoor air and cooling and dehumidifying at least a part thereof as processing air with an evaporator, the desiccant is passed through and supplied to the room, and a part of the refrigerant compressed by the compressor of the heat pump is supplied to the first condenser. The dehumidifying air conditioning system is characterized in that the regenerative air is heated by heating the heat medium other than the regenerated air by guiding another part of the compressed refrigerant to the second condenser.
処理空気中の水分を吸着し再生空気によって再生されるデシカントと、圧縮機と、処理空気と熱交換する蒸発器と、デシカント再生前の再生空気と熱交換する第1の凝縮器と、再生空気以外の熱媒体と熱交換する第2の凝縮器とを有するヒートポンプとを備え、
室内空気を取り入れて、少なくともその一部を処理空気として蒸発器で冷却除湿するとともに、ヒートポンプの圧縮機によって圧縮した冷媒を前記第1の凝縮器に導いて再生空気を加熱してデシカントを再生し、冷却除湿した処理空気をデシカントで除湿したのち室内に供給する第1の運転形態と、
圧縮した冷媒を前記第2の凝縮器に導いて再生空気以外の熱媒体を加熱することによって再生空気を加熱せず、冷却除湿した処理空気をデシカントで除湿せずに室内に供給する第2の運転形態と、
ヒートポンプの圧縮機によって圧縮した冷媒の一部を前記第1の凝縮器に導いて再生空気を加熱して冷却除湿した処理空気をデシカントで除湿したのち室内に供給するとともに、圧縮した冷媒の他の一部を前記第2の凝縮器にも導いて再生空気以外の熱媒体を加熱する第3の運転形態とを選択的に運転可能であることを特徴とする除湿空調システム。
A desiccant that absorbs moisture in the processing air and is regenerated by the regenerating air, a compressor, an evaporator that exchanges heat with the processing air, a first condenser that exchanges heat with the regenerating air before the desiccant regeneration, and the regenerating air A heat pump having a second condenser that exchanges heat with a heat medium other than
The room air is taken in, and at least a part of the air is cooled and dehumidified with an evaporator, and the refrigerant compressed by a heat pump compressor is led to the first condenser to regenerate the desiccant by heating the regeneration air. A first operation mode of supplying the indoors after dehumidifying the dehumidified treated air with a desiccant;
The compressed refrigerant is guided to the second condenser to heat the heat medium other than the regenerated air, so that the regenerated air is not heated, and the cooled and dehumidified treated air is supplied to the room without being dehumidified by the desiccant. Driving mode,
Both If you feed the process air a part of the refrigerant compressed by the compressor of the heat pump moistened cooled dividing by heating regeneration air is guided to the first condenser chamber after dehumidified by the desiccant, compressed refrigerant A dehumidifying air-conditioning system capable of selectively operating a third operation mode in which another part is also led to the second condenser to heat a heat medium other than regenerated air.
前記第2の運転形態の際に、再生空気の送風機を停止することを特徴とする請求項に記載の除湿空調システム。The dehumidifying air-conditioning system according to claim 2 , wherein the blower for regenerated air is stopped during the second operation mode. 前記室内空気は室内プールの空間内の空気であり、前記第2の凝縮器で熱交換する再生空気以外の熱媒体はプール水であることを特徴とする請求項1ないしのいずれかに記載の除湿空調システム。The said indoor air is the air in the space of an indoor pool, and heat media other than the reproduction | regeneration air heat-exchanged by a said 2nd condenser are pool water in any one of Claim 1 thru | or 3 characterized by the above-mentioned. Dehumidification air conditioning system.
JP22751097A 1997-08-08 1997-08-08 Dehumidification air conditioning system Expired - Fee Related JP3933264B2 (en)

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JP2009115379A (en) * 2007-11-06 2009-05-28 Sasakura Engineering Co Ltd Water refrigerant refrigerating device and heating/cooling system comprising the same
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