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JP3752816B2 - Operation control method and operation control apparatus for variable capacity compressor - Google Patents
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JP3752816B2 - Operation control method and operation control apparatus for variable capacity compressor - Google Patents

Operation control method and operation control apparatus for variable capacity compressor Download PDF

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Publication number
JP3752816B2
JP3752816B2 JP02605098A JP2605098A JP3752816B2 JP 3752816 B2 JP3752816 B2 JP 3752816B2 JP 02605098 A JP02605098 A JP 02605098A JP 2605098 A JP2605098 A JP 2605098A JP 3752816 B2 JP3752816 B2 JP 3752816B2
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Japan
Prior art keywords
pressure
capacity
control valve
control
suction pressure
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JP02605098A
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Japanese (ja)
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JPH11223183A (en
Inventor
尚也 横町
芳之 中根
達也 小出
俊郎 藤井
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Toyota Industries Corp
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Toyota Industries Corp
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Priority to JP02605098A priority Critical patent/JP3752816B2/en
Priority to US09/243,715 priority patent/US6138468A/en
Priority to DE69925653T priority patent/DE69925653T2/en
Priority to EP99102296A priority patent/EP0935107B1/en
Publication of JPH11223183A publication Critical patent/JPH11223183A/en
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Description

【0001】
【発明の属する技術分野】
本発明は、冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられ、制御圧室の制御圧と吸入圧領域の吸入圧との差圧の変化に基づいて吐出容量を変える可変容量型圧縮機に動作制御方法及び装置に関するものである。
【0002】
【従来の技術】
回転軸の回転をピストンの往復動に変換する斜板の傾角を変えて吐出容量を変える可変容量型圧縮機では、斜板の傾角変更は斜板を収容する制御圧室内の圧力を変更することによって行われる。この種の可変容量型圧縮機では、ピストンによって区画される圧縮室内の圧力、即ち吸入圧と制御圧室の圧力とのピストンを介した差圧によって斜板の傾角が規定される。前記差圧が大きくなるほど斜板の傾角は小さくなり、ピストンのストロークが小さくなる。即ち、前記差圧が大きくなるほど吐出容量が少なくなる。
【0003】
フロンは冷凍回路における冷媒として一般的に用いられているが、特開平8−110104号公報には二酸化炭素(CO2 )を冷媒として用いた冷凍回路が開示されている。二酸化炭素の臨界温度は31°C程度であってフロンに比べて20°ほども低い。冷凍回路中の凝縮器におけるフロン冷媒に関する熱交換、即ちフロン冷媒の冷却は、フロンの臨界温度を越えない温度域で行われる。しかし、二酸化炭素冷媒の冷却は、外気温度が高くなる夏では二酸化炭素の臨界温度を越えた超臨界域で行われることが多くなる。
【0004】
フロン冷媒使用の冷凍回路では温度膨張弁が用いられている。圧縮機の回転数の上昇に伴い、冷凍回路を循環するフロン冷媒の流量が増え、蒸発器における熱交換が十分に行われない。そのため、蒸発器の出口側の過熱度が低下する。温度膨張弁は前記過熱度の低下に伴ってフロン冷媒の流量を減らす方向に動作する。このような温度膨張弁の流量調整動作により吸入圧力が低下し、可変容量型圧縮機における前記差圧が増大する。その結果、吐出容量が減少し、冷房能力が調整される。又、フロン冷媒を蒸発させる蒸発温度は吸入圧の低下によって下がる。従って、吸入圧の変動に対応した容量ダウン制御は、蒸発器の出口側におけるフロン冷媒の圧力あるいは温度を検出することによって行える。
【0005】
二酸化炭素冷媒使用の冷凍回路では、超臨界域で冷媒を冷却する場合があり、同じ温度でも熱負荷によって圧力が変わる。このため、圧力によって流量を制御する圧力膨張弁が用いられる。圧縮機の回転数の上昇に伴い、冷凍回路を循環する二酸化炭素冷媒の流量が増え、吐出圧が上昇する。圧力膨張弁は吐出圧上昇に伴って二酸化炭素冷媒の流量を増やす方向に動作する。このような圧力膨張弁の流量調整動作により吸入圧が即座に低下せず、可変容量型圧縮機における前記差圧が即座に増大しない。その結果、吐出容量が即座に減少せず、冷房能力が迅速に調整されない。又、二酸化炭素冷媒を蒸発させる蒸発温度も即座に低下しない。従って、蒸発器の出口側における二酸化炭素冷媒の圧力あるいは温度の検出に基づく吸入圧の変動に対応した容量ダウン制御は困難である。このような困難性は、可変容量型圧縮機に必要以上の仕事をさせることになり、可変容量型圧縮機における動力消費及び負荷が過剰となる。
【0006】
本発明は、冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられる可変容量型圧縮機における動力消費及び負荷を減らすことを目的とする。
【0007】
【課題を解決するための手段】
そのために本発明は、冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられ、制御圧室の制御圧と吸入圧領域の吸入圧との差圧の変化に基づいて吐出容量を変える可変容量型圧縮機を対象とし、請求項1の発明では、前記制御圧と吸入圧との差圧を第1の容量制御弁及び第2の容量制御弁によって制御し、前記第1の容量制御弁は吐出圧を一定に保つように動作する目標吐出圧設定用の電気式容量制御弁であり、外気温度及び熱負荷を検出し、検出された外気温度及び熱負荷に基づいて前記目標吐出圧を決定し、前記決定された目標吐出圧をもたらすように前記第1の容量制御弁に対する電流供給が制御される。この構成によると、可変容量型圧縮機の吐出容量は、第1の容量制御弁の容量調整状態を外部情報に基づいて決定された容量調整状態に対応する吐出容量に迅速に調整される。従って、可変容量型圧縮機が必要以上の仕事を行うことが抑制される。電気式容量制御弁によって保たれる吐出圧は容量調整状態を反映し、制御圧室の制御圧と吸入圧との差圧の増減は、第1の容量制御弁によって保たれる吐出圧の値の増減を反映する。即ち、吐出圧は吐出容量に略比例し、吐出容量が増大すると吐出圧も増大するから、電気式容量制御弁によって保たれる吐出圧の値を変更することによって吐出容量の調整が行われる。また、外気温度、熱負荷は可変容量型圧縮機の吐出容量を調整するための外部情報として適切である。
【0008】
請求項2の発明では、請求項1において、吐出圧領域から前記制御圧室への冷媒供給を第1の容量制御弁によって制御し、前記制御圧室から前記吸入圧領域への冷媒抜き出しを第2の容量制御弁によって制御し、第2の容量制御弁の容量調整状態を外気温度又は熱負荷を含む外部情報に基づいて決定するようにした。
【0013】
請求項の発明では、請求項1及び請求項のいずれか1項において、前記第2の容量制御弁は吸入圧を一定に保つように動作する目標吸入圧設定用の電気式容量制御弁とした。
【0014】
吸入圧が増大すると制御圧と吸入圧との差圧が減り、吐出容量が増える。第2の容量制御弁によって保たれる吸入圧は容量調整状態を反映し、制御圧室の制御圧と吸入圧との差圧の増減は、第2の容量制御弁によって保たれる吸入圧の値の増減を反映する。即ち、第2の容量制御弁によって保たれる吸入圧の値を変更することによって吐出容量の調整が行われる。
【0016】
請求項の発明では、請求項において、熱負荷を検出し、検出された熱負荷に基づいて前記目標吸入圧を決定し、前記決定された目標吸入圧をもたらすように前記第2の容量制御弁に対する電流供給を制御するようにした。
【0017】
請求項の発明では、前記制御圧と前記吸入圧との差圧を制御する第1の容量制御弁と、前記制御圧と前記吸入圧との差圧を制御する第2の容量制御弁と、少なくとも、前記第1の容量制御弁の容量調整状態を決定する容量調整状態制御手段と、外気温度を検出する外気温度検手段及び熱負荷を検出する熱負荷検出手段とを備え、前記容量調整状態制御手段は、前記外気温度検出手段によって検出された外気温度及び前記熱負荷検出手段によって検出された熱負荷に基づいて前記目標吐出圧を決定する目標吐出圧決定手段と、前記決定された目標吐出圧をもたらすように前記第1の容量制御弁に対する電流供給を制御する第1の電流供給制御手段とを備えた動作制御装置を構成した。この構成によると、目標吐出圧決定手段は、検出された外気温度及び熱負荷に基づいて目標吐出圧を決定する。第1の電気供給制御手段は決定された目標吐出圧をもたらすように第1の容量制御弁に対する電流供給を制御し、第1の容量制御弁が前記決定された目標吐出圧をもたらすように動作する。吐出圧は第1の容量制御弁に対する電流供給の制御によって迅速に制御される。従って、容量調整状態を反映する吐出圧は外部情報に基づいて迅速に調整され、可変容量型圧縮機が必要以上の仕事を行なうことが抑制される。
【0018】
請求項の発明では、請求項において、前記第1の容量制御弁は吐出圧領域から前記制御圧室への冷媒供給を制御し、前記第2の容量制御弁は前記制御圧室から前記吸入圧領域への冷媒抜き出しを制御するようにした。
【0022】
請求項の発明では、請求項及び請求項のいずれか1項において、熱負荷を検出する熱負荷検出手段を備え、前記容量調整状態制御手段は、前記熱負荷検出手段によって検出された熱負荷に基づいて前記目標吸入圧を決定する目標吸入圧決定手段と、前記決定された目標吸入圧をもたらすように前記第2の容量制御弁に対する電流供給を制御する第2の電流供給制御手段とを備えた動作制御装置を構成した。
【0023】
目標吸入圧決定手段は、検出された熱負荷に基づいて目標吸入圧を決定する。第2の電気供給制御手段は決定された目標吸入圧をもたらすように第2の容量制御弁に対する電流供給を制御し、第2の容量制御弁が前記決定された目標吸入圧をもたらすように動作する。吸入圧は第2の容量制御弁に対する電流供給の制御によって迅速に制御される。従って、容量調整状態を反映する吸入圧は外部情報に基づいて迅速に調整され、可変容量型圧縮機が必要以上の仕事を行なうことが抑制される。
【0024】
【発明の実施の形態】
以下、本発明を具体化した第1の実施の形態を図1〜図7に基づいて説明する。
【0025】
図1に示すように、シリンダブロック11の前後にはフロントハウジング12及びリヤハウジング13が接合固定されている。シリンダブロック11及びフロントハウジング12には回転軸14がラジアルベアリング15,16を介して回転可能に支持されている。回転軸14は、図示しない電磁クラッチを介して圧縮機搭載車両のエンジンから回転力を得る。フロントハウジング12内にて回転軸14には円板形状の回転支持体17が止着されており、回転支持体17の周縁部に形成された支持アーム171にはガイド孔172が形成されている。
【0026】
回転軸14には斜板18が回転軸14の軸方向へ傾動可能かつスライド可能に支持されている。図1及び図2に示すように、斜板18には連結片181が止着されていると共に、連結片181の先端部にはガイドピン19が取り付けられている。ガイドピン19はガイド孔172に係合しており、ガイド孔172はガイドピン19を介して斜板18の傾動を案内する。この案内作用及び回転軸14の支持作用により斜板18が回転軸14方向へ揺動可能かつ回転軸14と一体的に回転可能である。
【0027】
シリンダブロック11に貫設されたシリンダボア111内にはピストン20が収容されている。ピストン20は、シリンダボア111内に圧縮室112を区画する。ピストン20の首部201と斜板18との間には一対のシュー21が介在されている。制御圧室121内に収容された斜板18の回転運動はシュー21を介してピストン20の前後往復運動に変換され、ピストン20がシリンダボア111内を前後動する。
【0028】
図1及び図3に示すように、リヤハウジング13内には吸入圧領域となる吸入室131及び吐出圧領域となる吐出室132が区画形成されている。シリンダブロック11とリヤハウジング13との間には区画板22及び一対の弁形成板23,24が介在されており、区画板22には吸入ポート221及び吐出ポート222が設けられている。吸入ポート221は弁形成板23上の吸入弁231によって開閉され、吐出ポート222は弁形成板24上の吐出弁241によって開閉される。吐出弁241はリテーナ37によって開度規制される。吐出動作となるピストン20の往動により圧縮室112内の冷媒が吐出弁241を押し退けて吐出ポート222から吐出室132へ吐出される。吸入動作となるピストン20の復動により吸入室131内の冷媒が吸入弁231を押し退けて吸入ポート221から圧縮室112へ吸入される。
【0029】
吐出室132から外部冷媒回路38へ流出した冷媒は凝縮器39で冷却作用を受ける。凝縮器39で冷却作用を受けた冷媒は圧力膨張弁40を経由して蒸発器41に到る。圧力膨張弁40は吐出圧Pdの上昇に応じて通過断面積を増やすように動作する。蒸発器41で加熱された冷媒は吸入室131へ還流する。
【0030】
図6はモリエル線図である。曲線E1は飽和液線と飽和蒸気線とを表す。曲線E2は二酸化炭素冷媒の臨界温度曲線を表す。横軸はエンタルピー、縦軸は圧力を表す。直線D1は蒸発器41における蒸発行程、曲線D2は可変容量型圧縮機における圧縮行程、直線D3は凝縮器39における凝縮行程、直線D4は圧力膨張弁40における膨張行程を表す。図示の例では、曲線E3で表す外気温度Teが臨界温度曲線E2で表す臨界温度よりも高く、二酸化炭素冷媒の凝縮は超臨界域で行われる。
【0031】
ピストン20のストロークは制御圧室121内の制御圧Pcと圧縮室112内の圧力とのピストン20を介した差圧、即ち制御圧Pcと吸入圧Psとの差圧(Pc−Ps)に応じて変わり、吐出容量を左右する斜板18の傾角が変化する。差圧(Pc−Ps)が増加すると斜板18の傾角が小さくなり、吐出容量が減る。差圧(Pc−Ps)が減少すると斜板18の傾角が大きくなり、吐出容量が増える。リヤハウジング13内の電気式の第1の容量制御弁25は、吐出室132から制御圧室121への冷媒供給を制御する。リヤハウジング13内の電気式の第2の容量制御弁42は、制御圧室121から吸入室131への冷媒抜き出しを制御する。制御圧室121内の制御圧Pcは、第1の容量制御弁25の冷媒供給及び第2の容量制御弁42の冷媒抜き出しによって制御される。
【0032】
図4に示すように、第1の容量制御弁25は、ソレノイド26と弁機構27とからなる。ソレノイド26は、コイル261と、固定鉄芯262と、可動鉄芯263と、可動鉄芯263に止着された駆動ロッド264と、復帰ばね265とからなる。弁機構27は、ハウジング28と、ハウジング28内の弁室281に収容された弁体29と、弁体29を保持する保持ばね30とからなる。可動鉄芯263はコイル261への電流供給によって固定鉄芯262側に吸引付勢される。即ち、ソレノイド26の駆動力は駆動ロッド264を介して弁体29に伝達され、弁体29は弁孔282を閉じる方向へ付勢される。復帰ばね265は可動鉄芯263を固定鉄芯262から離間する方向へ付勢する。
【0033】
ハウジング28にはポート283が形成されている。弁室281はポート283及び通路31を介して制御圧室121に連通しており、弁孔282は通路32を介して吐出室132に連通している。図4に示すように弁体29が弁孔282を開いた位置にあるときには、吐出室132内の高圧冷媒は、通路32、弁孔282、弁室281、ポート283、通路31という冷媒供給通路を経由して制御圧室121へ送られる。
【0034】
ソレノイド26の駆動力Fdと保持ばね30のばね力F2との和は、弁体29に作用する吐出圧Pdの全圧力Pd1と復帰ばね265のばね力F1との和に対抗する。即ち、吐出圧Pdの全圧力Pd1が(Fd+F2−F1)を上回ると弁体29が弁孔282を開き、吐出室132の高圧冷媒が制御圧室121へ流入する。吐出圧Pdの全圧力Pd1が(Fd+F2−F1)を越えない場合には弁体29が弁孔282を閉じ、吐出室132の高圧冷媒が制御圧室121へ流入しない。即ち、吐出室132から制御圧室121への冷媒供給を制御する第1の容量制御弁25は、吐出圧Pdを一定に保つように動作する。
【0035】
第2の容量制御弁42は、ソレノイド43と弁機構44とからなる。ソレノイド43は、コイル431と、固定鉄芯432と、可動鉄芯433と、可動鉄芯433に止着された駆動ロッド434と、復帰ばね435とからなる。弁機構44は、ハウジング45と、駆動ロッド434に結合されてハウジング45内の弁室451に収容された弁体46と、弁室451内に収容されて駆動ロッド434に結合するベローズ48と、ベローズ48を伸張する方向へ受圧板481に作用するばね49とからなる。弁室451は弁孔453及び通路47を介して制御圧室121に連通しており、ポート452は通路50を介して吸入室131に連通している。図5に示すように弁体29が弁孔453を開いた位置にあるときには、制御圧室121内の冷媒は、通路47、弁孔453、弁室451、ポート452、通路50という冷媒抜き出し通路を経由して吸入室131へ流出する。
【0036】
吸入室131の吸入圧Psは通路50及びポート452を介して弁室451に波及しており、ばね49のばね力F4が受圧板481に作用する吸入圧Psの全圧力Ps1に対抗する。可動鉄芯433はコイル431への電流供給によって固定鉄芯432側に吸引付勢される。即ち、ソレノイド43の駆動力はばね49のばね力に対抗する。復帰ばね435は可動鉄芯433を固定鉄芯432から離間する方向へ付勢する。
【0037】
ソレノイド43の駆動力Fsと受圧板481に対する吸入圧Psの全圧力Ps1との和は、復帰ばね435のばね力F3とばね49のばね力F4との和に対抗する。全圧力Ps1が(F3+F4−F)を下回ると弁体46が弁孔453を閉じ、全圧力Ps1が(F3+F4−F)を越えると弁体46が弁孔453を開く。即ち、制御圧室121から吸入室131への冷媒抜き出しを制御する第2の容量制御弁42は、吸入圧Psを一定に保つように動作する。
【0038】
第1の容量制御弁25のソレノイド26及び第2の容量制御弁42のソレノイド43はコントローラ33の電流供給制御を受ける。コントローラ33は、目標吐出圧決定手段となる目標吐出圧決定部331と、目標吸入圧決定手段となる目標吸入圧決定部332と、第1の電流供給制御手段となる第1の電流供給制御部333と、第2の電流供給制御手段となる第2の電流供給制御部334とからなる。コントローラ33は図7のフローチャートで示す容量調整状態制御プログラムに基づいて第1の容量制御弁25及び第2の容量制御弁42の容量調整状態を制御する。目標吐出圧決定部331は、外気温度検出器34によって検出される外気温度Te、及び室内温度検出器35によって検出される室内温度Tsを所定の時間間隔でサンプリングしている。目標吸入圧決定部332は室内温度検出器35によって検出される室内温度Tsを所定の時間間隔でサンプリングしている。
【0039】
目標吐出圧決定部331は、外気温度検出器34によって検出された外気温度Te、室内温度検出器35によって検出された室内温度Ts、及び目標室内温度設定器36によって設定された目標室内温度Toに基づいて目標吐出圧Pdoを決定する。外気温度Teが高くなれば吐出容量を増やす必要がある。又、熱負荷が高いレベル域で増大すれば吐出容量を増やす必要がある。外気温度Te及び熱負荷と目標吐出圧Pdoとの関係は、前記のような必要性に基づいて予め決められており、目標吐出圧決定部331は外気温度情報、熱負荷情報及び前記関係に基づいて目標吐出圧Pdoを決定する。第1の電流供給制御部333は、目標吐出圧決定部331によって決定された目標吐出圧Pdoをもたらすように第1の容量制御弁25のソレノイド26に対する電流供給を制御する。
【0040】
目標吸入圧決定部332は、検出された室内温度Ts及び目標室内温度Toに基づいて目標吸入圧Psoを決定する。目標室内温度Toと室内温度Tsとの差は熱負荷を反映しており、目標吸入圧決定部332は熱負荷に基づいて目標吸入圧Psoを決定する。熱負荷が大きくなれば吸入圧Psを下げる必要がある。熱負荷と目標吸入圧Psoとの関係は、前記のような必要性に基づいて予め決められており、目標吸入圧決定部332は熱負荷情報及び前記関係に基づいて目標吸入圧Psoを決定する。第2の電流供給制御部334は、目標吸入圧決定部332によって決定された目標吸入圧Psoをもたらすように第2の容量制御弁42のソレノイド43に対する電流供給を制御する。
【0041】
第1の実施の形態では以下の効果が得られる。
(1-1)吐出容量は制御圧室121内の制御圧Pcと吸入圧Psとの差圧によって調整され、制御圧Pcと吸入圧Psとの差圧は第1の容量制御弁25に対する電流供給制御によって迅速に調整される。吐出容量は吐出圧Pdに略比例し、吐出圧Pdは吐出容量を反映する。即ち、目標吐出圧Pdoは第1の容量制御弁25の容量調整状態を規定する。目標吐出圧決定部331は外気温度Te及び熱負荷という外部情報に基づいて目標吐出圧Pdoを迅速に決定する。車両エンジンの回転数変動は回転軸14の回転数変動をもたらし、吐出圧Pdが変動しようとするが、吐出容量を反映する吐出圧Pdは外気温度Teという外部情報に基づいて決定された目標吐出圧Pdoという一定値に定圧制御される。従って、回転軸14の回転数変動に起因した吐出容量の変動は、コントローラ33及び第1の容量制御弁25による外気温度Teに応じた吐出圧の定圧制御によって抑制される。その結果、圧縮機の回転数変動のために可変容量型圧縮機が必要以上の仕事を行なうことが抑制され、可変容量型圧縮機における動力消費及び負荷が減らされる。
(1-2)制御圧Pcと吸入圧Psとの差圧は第2の容量制御弁42に対する電流供給制御によっても迅速に調整される。吸入圧Psは熱負荷を直接的に反映しており、熱負荷は室内温度を直接的に反映している。従って、室内温度の制御には吸入圧Psを制御するのがよい。目標吸入圧Psoは第2の容量制御弁42の容量調整状態を規定する。目標吸入圧決定部332は熱負荷という外部情報に基づいて目標吸入圧Psoを迅速に決定する。熱負荷の変動は吸入圧Psの変動をもたらすが、熱負荷を反映する吸入圧Psは熱負荷という外部情報に基づいて決定された目標吸入圧Psoに迅速に制御される。従って、熱負荷の変動のために可変容量型圧縮機が必要以上の仕事を行なうことが抑制される。
(1-3)熱負荷が高いレベル域にある場合にも、吐出圧Pdは熱負荷という外部情報に基づいて決定された目標吐出圧Pdoという一定値に定圧制御される。従って、高いレベル域での熱負荷の変動に対応した吐出容量の変動は、コントローラ33及び第1の容量制御弁25による熱負荷に応じた吐出圧の制御によって適正に調整され、可変容量型圧縮機が必要以上の仕事を行なうことが抑制される。
(1-4)室内温度の制御はきめ細かに行なえるのが望ましい。吸入圧Psを制御する第2の容量制御弁42は室内温度のきめ細かな制御に適しているが、圧縮機の大きな回転数変動に対する容量調整には不向きである。吐出圧Pdを制御する第1の容量制御弁25は圧縮機の大きな回転数変動に対する容量調整に好適であるが、室内温度のきめ細かな制御には不向きである。回転数変動に対する吐出圧制御、熱負荷変動に対する吸入圧制御を2つの容量制御弁25,42によって適正に分担して受け持つ構成は、可変容量型圧縮機における動力消費及び負荷を減らすと共に、良好な冷房制御の達成を可能にする。
(1-5)外気温度、熱負荷の変動は穏やかであるため、コントローラ33にはそれほどの高速処理機能は要求されない。従って、制御システムは安価に構築できる。
(1-6)熱負荷が高いときには吐出容量を増やす必要があり、熱負荷が低いときには吐出容量を減らす必要がある。従って、室内温度Ts及び目標室内温度Toに基づいて把握される熱負荷は、吐出容量を迅速に調整するための外部情報として適切である。
【0042】
次に、図8の第2の実施の形態を説明する。可変容量型圧縮機の内部構造は第1の実施の形態と同じであり、第1の実施の形態と同じ構成部には同じ符号が付してある。
【0043】
この実施の形態における第2の容量制御弁51では吸入室131の吸入圧Psが感圧室511に波及しており、感圧室511内の吸入圧Psがダイヤフラム512を介してばね52のばね力と対抗しており、ばね52のばね力はねじ53の螺合位置によって調整できる。ダイヤフラム512の変位は変位伝達ロッド513を介して弁体514に伝達される。第2の容量制御弁51も第1の実施の形態における第2の容量制御弁42と同様に目標吸入圧設定用の制御弁であるが、目標吸入圧はばね52のばね力設定によって行われる。第1の容量制御弁25の容量調整状態は、目標吐出圧決定部331及び第1の電流供給制御部333からなるコントローラ54によって第1の実施の形態の場合と同様に行われる。
【0044】
この実施の形態においても第1の実施の形態における(1-1)項、(1-3)項と同様の効果が得られる。
次に、図9の第3の実施の形態を説明する。可変容量型圧縮機の内部構造は第1の実施の形態と同じであり、第1の実施の形態と同じ構成部には同じ符号が付してある。
【0045】
第2の容量制御弁55のソレノイド56は、コイル561と、固定鉄芯562と、可動鉄芯563と、可動鉄芯563に止着された駆動ロッド564と、復帰ばね565とからなる。弁機構44は、ハウジング57と、ハウジング57内の弁室571に収容された弁体58と、弁体58を保持する保持ばね59と、ハウジング57内の感圧室572内に収容されて駆動ロッド564に結合するベローズ60と、ベローズ60を伸張する方向へ受圧板601に作用するばね61とからなる。吸入室131の吸入圧Psは通路50及びポート575を介して感圧室572に波及しており、ばね61のばね力F4が受圧板601に作用する吸入圧Psの全圧力Ps1に対抗する。可動鉄芯563はコイル561への電流供給によって固定鉄芯562側に吸引付勢される。即ち、ソレノイド56の駆動力はばね61のばね力に対抗する。復帰ばね565は可動鉄芯563を固定鉄芯562から離間する方向へ付勢する。弁孔573が開いたときには吐出室132の高圧冷媒が通路62,63を経由して制御圧室121へ送られる。吸入室131内の吸入圧Psは通路64を介して感圧室572に波及している。
【0046】
ソレノイド56の駆動力Foと受圧板601に対する吸入圧Psの全圧力Ps1との和は、復帰ばね565のばね力F5とばね61のばね力F6との和に対抗する。全圧力Ps1が(F5+F6−Fo)を下回ると弁体58が弁孔573を開き、全圧力Ps1が(F5+F6−Fo)を越えると弁体58が弁孔573を閉じる。即ち、容量制御弁55は、吐出室132から制御圧室121への冷媒供給を制御し、かつ吸入圧Psを一定に保つように動作する。
【0047】
制御圧室121から吸入室131への冷媒抜き出しは絞り通路66を介して行われる。
コントローラ65の目標吐出圧決定部651は、外気温度検出器34によって検出された外気温度Teに基づいて目標吐出圧Pdoを決定する。外気温度Teが高くなれば吐出容量を増やす必要がある。第1の電流供給制御部653は、目標吐出圧決定部651によって決定された目標吐出圧Pdoをもたらすように第1の容量制御弁25のソレノイド26に対する電流供給を制御する。
【0048】
目標吸入圧決定部652は、室内温度検出器35によって検出された室内温度Ts及び目標室内温度設定器36によって設定された目標室内温度Toに基づいて目標吸入圧Psoを決定する。第2の電流供給制御部654は、目標吸入圧決定部652によって決定された目標吸入圧Psoをもたらすように第2の容量制御弁55のソレノイド56に対する電流供給を制御する。
【0049】
この実施の形態では、第1の容量制御弁25、目標吐出圧決定部651及び第1の電流供給制御部653が回転数変動に対する吐出圧変動抑制制御を受持ち、第2の容量制御弁55、目標吸入圧決定部652及び第2の電流供給制御部654が熱負荷変動に対する吸入圧制御を受持つ。従って、この実施の形態においても第1の実施の形態における(1-4)項と同様の効果が得られる。
【0050】
本発明では、以下のような実施の形態も可能である
(1)第3の実施の形態において、第1の実施の形態の場合のように外気温度及び熱負荷から目標吐出圧を決定するようにすること。
)第1の容量制御弁を電磁開閉弁とし、目標吐出圧をもたらすように電磁開閉弁を開閉制御するようにすること。
)第2の容量制御弁を電磁開閉弁とし、目標吸入圧をもたらすように電磁開閉弁を開閉制御するようにすること。
【0051】
【発明の効果】
以上詳述したように本発明では、吐出圧領域から制御圧室への冷媒供給を制御する第1の容量制御弁の容量調整状態を外部情報に基づいて決定するようにしたので、冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられる可変容量型圧縮機における動力消費及び負荷を減らし得るという優れた効果を奏する。
【図面の簡単な説明】
【図1】本発明の第1の実施の形態を示す圧縮機全体の側断面図。
【図2】図1のA−A線断面図。
【図3】図1のB−B線断面図。
【図4】要部拡大側断面図。
【図5】要部拡大側断面図。
【図6】モリエル線図。
【図7】容量調整状態制御プログラムを表すフローチャート。
【図8】第2の実施の形態を示す要部拡大側断面図。
【図9】第3の実施の形態を示す要部拡大側断面図。
【符号の説明】
121…制御圧室、131…吸入圧領域となる吸入室、132…吐出圧領域となる吐出室、25…第1の容量制御弁、42,51…第2の容量制御弁、33,54,65…容量調整状態制御手段となるコントローラ、331,651…目標吐出圧決定手段となる目標吐出圧決定部、332,652…目標吸入圧決定手段となる目標吸入圧決定部、333,653…第1の電流供給制御手段となる第1の電流供給制御部、334,654…第2の電流供給制御手段となる第2の電流供給制御部、34…外気温度検出手段となる外気温度検出器、35…熱負荷検出手段を構成する室内温度検出器。
[0001]
BACKGROUND OF THE INVENTION
The present invention is used in a refrigeration circuit that performs heat exchange including the case where the refrigerant is cooled in a supercritical region that exceeds the critical temperature of the refrigerant, and the differential pressure between the control pressure in the control pressure chamber and the suction pressure in the suction pressure region. The present invention relates to an operation control method and apparatus for a variable displacement compressor that changes the discharge capacity based on the change in the pressure.
[0002]
[Prior art]
In variable displacement compressors that change the discharge capacity by changing the tilt angle of the swash plate that converts the rotation of the rotating shaft into the reciprocating motion of the piston, changing the tilt angle of the swash plate changes the pressure in the control pressure chamber that houses the swash plate Is done by. In this type of variable displacement compressor, the inclination angle of the swash plate is defined by the pressure in the compression chamber defined by the piston, that is, the pressure difference between the suction pressure and the control pressure chamber via the piston. As the differential pressure increases, the inclination angle of the swash plate decreases and the piston stroke decreases. That is, the discharge volume decreases as the differential pressure increases.
[0003]
Freon is generally used as a refrigerant in a refrigeration circuit, but Japanese Patent Application Laid-Open No. 8-110104 discloses carbon dioxide (CO2) As a refrigerant is disclosed. The critical temperature of carbon dioxide is about 31 ° C, which is about 20 ° lower than that of Freon. Heat exchange related to the chlorofluorocarbon refrigerant in the condenser in the refrigeration circuit, that is, cooling of the chlorofluorocarbon refrigerant is performed in a temperature range that does not exceed the critical temperature of the fluorocarbon. However, the cooling of the carbon dioxide refrigerant is often performed in a supercritical region exceeding the critical temperature of carbon dioxide in the summer when the outside air temperature becomes high.
[0004]
A temperature expansion valve is used in a refrigeration circuit using a fluorocarbon refrigerant. As the rotational speed of the compressor increases, the flow rate of the chlorofluorocarbon refrigerant circulating in the refrigeration circuit increases, and heat exchange in the evaporator is not sufficiently performed. For this reason, the degree of superheat on the outlet side of the evaporator is reduced. The temperature expansion valve operates to reduce the flow rate of the chlorofluorocarbon refrigerant as the degree of superheat decreases. By such a flow rate adjusting operation of the temperature expansion valve, the suction pressure is reduced, and the differential pressure in the variable capacity compressor is increased. As a result, the discharge capacity is reduced and the cooling capacity is adjusted. Further, the evaporation temperature for evaporating the chlorofluorocarbon refrigerant decreases as the suction pressure decreases. Therefore, the capacity reduction control corresponding to the fluctuation of the suction pressure can be performed by detecting the pressure or temperature of the chlorofluorocarbon refrigerant at the outlet side of the evaporator.
[0005]
In refrigeration circuit using carbon dioxide refrigerantIn some cases, the refrigerant is cooled in the supercritical region, and the pressure changes depending on the heat load even at the same temperature. Therefore, the pressure that controls the flow rate by pressureA force expansion valve is used. As the rotational speed of the compressor increases, the flow rate of the carbon dioxide refrigerant circulating in the refrigeration circuit increases, and the discharge pressure increases. The pressure expansion valve operates to increase the flow rate of the carbon dioxide refrigerant as the discharge pressure increases. By such a flow rate adjusting operation of the pressure expansion valve, the suction pressure does not immediately decrease, and the differential pressure in the variable displacement compressor does not increase immediately. As a result, the discharge capacity does not decrease immediately and the cooling capacity is not adjusted quickly. Further, the evaporation temperature for evaporating the carbon dioxide refrigerant does not immediately decrease. Therefore, it is difficult to perform capacity down control corresponding to fluctuations in the suction pressure based on detection of the pressure or temperature of the carbon dioxide refrigerant on the outlet side of the evaporator. Such difficulty causes the variable capacity compressor to perform more work than necessary, and power consumption and load in the variable capacity compressor become excessive.
[0006]
An object of the present invention is to reduce power consumption and load in a variable capacity compressor used in a refrigeration circuit that performs heat exchange including cooling a refrigerant in a supercritical region that exceeds the critical temperature of the refrigerant.
[0007]
[Means for Solving the Problems]
  For this purpose, the present invention is used in a refrigeration circuit that performs heat exchange including the case where the refrigerant is cooled in a supercritical region that exceeds the critical temperature of the refrigerant, and the control pressure in the control pressure chamber and the suction pressure in the suction pressure region. The present invention is directed to a variable displacement compressor that changes a discharge capacity based on a change in differential pressure. In the first aspect of the invention, the differential pressure between the control pressure and the suction pressure is determined by a first displacement control valve and a second displacement control. Controlled by valve andThe first capacity control valve is an electric capacity control valve for setting a target discharge pressure that operates so as to keep the discharge pressure constant. The first capacity control valve detects an outside air temperature and a thermal load, and detects the detected outside air temperature and the heat load. Based on this, the target discharge pressure is determined, and the current supply to the first capacity control valve is controlled so as to bring the determined target discharge pressure. According to this configuration, the discharge capacity of the variable capacity compressor is quickly adjusted to the discharge capacity corresponding to the capacity adjustment state determined based on the external information from the capacity adjustment state of the first capacity control valve. Therefore, the variable capacity compressor is prevented from performing more work than necessary. The discharge pressure maintained by the electric capacity control valve reflects the capacity adjustment state, and the increase / decrease in the differential pressure between the control pressure in the control pressure chamber and the suction pressure is the value of the discharge pressure maintained by the first capacity control valve. Reflect the increase or decrease. That is, the discharge pressure is substantially proportional to the discharge capacity, and the discharge pressure increases as the discharge capacity increases. Therefore, the discharge capacity is adjusted by changing the value of the discharge pressure maintained by the electric capacity control valve. The outside air temperature and heat load are appropriate as external information for adjusting the discharge capacity of the variable capacity compressor.
[0008]
  According to a second aspect of the present invention, in the first aspect, the refrigerant supply from the discharge pressure region to the control pressure chamber is controlled by the first capacity control valve, and the refrigerant is extracted from the control pressure chamber to the suction pressure region. Controlled by two capacity control valvesThe second2 capacity control valveNoThe amount adjustment stateIncludes ambient temperature or heat loadThe decision was made based on external information.
[0013]
  Claim3In the invention of claim 1,as well asClaim2In any one of the above, the second capacity control valve is an electric capacity control valve for setting a target suction pressure that operates so as to keep the suction pressure constant.
[0014]
When the suction pressure increases, the differential pressure between the control pressure and the suction pressure decreases, and the discharge capacity increases. The suction pressure maintained by the second capacity control valve reflects the capacity adjustment state, and the increase / decrease in the differential pressure between the control pressure in the control pressure chamber and the suction pressure is the same as the suction pressure maintained by the second capacity control valve. Reflects changes in value. That is, the discharge capacity is adjusted by changing the value of the suction pressure maintained by the second capacity control valve.
[0016]
  Claim4In the invention of claim3, Detecting a thermal load, determining the target suction pressure based on the detected thermal load, and controlling a current supply to the second capacity control valve to provide the determined target suction pressure did.
[0017]
  Claim5In the invention, a first capacity control valve that controls a differential pressure between the control pressure and the suction pressure, a second capacity control valve that controls a differential pressure between the control pressure and the suction pressure,at least,The first capacity controlValveCapacity adjustment statusDecideCapacity adjustment state control meansAn outside air temperature detecting means for detecting the outside air temperature and a heat load detecting means for detecting the heat load;WithThe capacity adjustment state control means determines the target discharge pressure based on the outside air temperature detected by the outside air temperature detection means and the thermal load detected by the heat load detection means; First current supply control means for controlling current supply to the first capacity control valve so as to provide the determined target discharge pressure.An operation control device was configured.According to this configuration, the target discharge pressure determining means determines the target discharge pressure based on the detected outside air temperature and thermal load. The first electric supply control means controls the current supply to the first capacity control valve so as to provide the determined target discharge pressure, and the first capacity control valve operates so as to provide the determined target discharge pressure. To do. The discharge pressure is quickly controlled by controlling the current supply to the first capacity control valve. Therefore, the discharge pressure reflecting the capacity adjustment state is quickly adjusted based on the external information, and the variable capacity compressor is prevented from performing work more than necessary.
[0018]
  Claim6In the invention of claim5The first capacity control valve controls refrigerant supply from the discharge pressure region to the control pressure chamber, and the second capacity control valve controls refrigerant extraction from the control pressure chamber to the suction pressure region. I did it.
[0022]
  Claim7In the invention of claim5And claims6In any one of the above, it is provided with a thermal load detection means for detecting a thermal load, and the capacity adjustment state control means determines the target suction pressure based on the thermal load detected by the thermal load detection means. An operation control device comprising pressure determining means and second current supply control means for controlling current supply to the second capacity control valve so as to bring the determined target suction pressure is configured.
[0023]
The target suction pressure determining means determines the target suction pressure based on the detected thermal load. The second electric supply control means controls the current supply to the second capacity control valve so as to provide the determined target suction pressure, and the second capacity control valve operates so as to provide the determined target suction pressure. To do. The suction pressure is quickly controlled by controlling the current supply to the second capacity control valve. Therefore, the suction pressure reflecting the capacity adjustment state is quickly adjusted based on the external information, and the variable capacity compressor is prevented from performing work more than necessary.
[0024]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, a first embodiment of the present invention will be described with reference to FIGS.
[0025]
As shown in FIG. 1, a front housing 12 and a rear housing 13 are joined and fixed before and after the cylinder block 11. A rotating shaft 14 is rotatably supported on the cylinder block 11 and the front housing 12 via radial bearings 15 and 16. The rotating shaft 14 obtains a rotational force from the engine of the compressor-equipped vehicle via an electromagnetic clutch (not shown). In the front housing 12, a disc-shaped rotary support 17 is fixed to the rotary shaft 14, and a guide hole 172 is formed in a support arm 171 formed at the peripheral edge of the rotary support 17. .
[0026]
A swash plate 18 is supported on the rotary shaft 14 so as to be tiltable and slidable in the axial direction of the rotary shaft 14. As shown in FIGS. 1 and 2, a connecting piece 181 is fixed to the swash plate 18, and a guide pin 19 is attached to the distal end portion of the connecting piece 181. The guide pin 19 is engaged with the guide hole 172, and the guide hole 172 guides the tilting of the swash plate 18 through the guide pin 19. The swash plate 18 can swing in the direction of the rotation shaft 14 and can rotate integrally with the rotation shaft 14 by the guide operation and the support operation of the rotation shaft 14.
[0027]
A piston 20 is accommodated in a cylinder bore 111 penetrating the cylinder block 11. The piston 20 defines a compression chamber 112 in the cylinder bore 111. A pair of shoes 21 are interposed between the neck portion 201 of the piston 20 and the swash plate 18. The rotational movement of the swash plate 18 accommodated in the control pressure chamber 121 is converted into the back-and-forth reciprocating movement of the piston 20 via the shoe 21, and the piston 20 moves back and forth in the cylinder bore 111.
[0028]
As shown in FIGS. 1 and 3, a suction chamber 131 serving as a suction pressure region and a discharge chamber 132 serving as a discharge pressure region are defined in the rear housing 13. A partition plate 22 and a pair of valve forming plates 23 and 24 are interposed between the cylinder block 11 and the rear housing 13, and a suction port 221 and a discharge port 222 are provided on the partition plate 22. The suction port 221 is opened and closed by a suction valve 231 on the valve forming plate 23, and the discharge port 222 is opened and closed by a discharge valve 241 on the valve forming plate 24. The opening degree of the discharge valve 241 is restricted by the retainer 37. The refrigerant in the compression chamber 112 is pushed out of the discharge valve 241 and discharged from the discharge port 222 to the discharge chamber 132 by the forward movement of the piston 20 that is in the discharge operation. The refrigerant in the suction chamber 131 is pushed away from the suction valve 231 by the backward movement of the piston 20 in the suction operation, and is sucked into the compression chamber 112 from the suction port 221.
[0029]
The refrigerant flowing out from the discharge chamber 132 to the external refrigerant circuit 38 is cooled by the condenser 39. The refrigerant that has been cooled by the condenser 39 reaches the evaporator 41 via the pressure expansion valve 40. The pressure expansion valve 40 operates to increase the passage cross-sectional area as the discharge pressure Pd increases. The refrigerant heated by the evaporator 41 returns to the suction chamber 131.
[0030]
FIG. 6 is a Mollier diagram. Curve E1 represents a saturated liquid line and a saturated vapor line. A curve E2 represents a critical temperature curve of the carbon dioxide refrigerant. The horizontal axis represents enthalpy and the vertical axis represents pressure. The straight line D1 represents the evaporation stroke in the evaporator 41, the curve D2 represents the compression stroke in the variable displacement compressor, the straight line D3 represents the condensation stroke in the condenser 39, and the straight line D4 represents the expansion stroke in the pressure expansion valve 40. In the illustrated example, the outside air temperature Te represented by the curve E3 is higher than the critical temperature represented by the critical temperature curve E2, and the condensation of the carbon dioxide refrigerant is performed in the supercritical region.
[0031]
The stroke of the piston 20 depends on the pressure difference between the control pressure Pc in the control pressure chamber 121 and the pressure in the compression chamber 112 via the piston 20, that is, the pressure difference (Pc−Ps) between the control pressure Pc and the suction pressure Ps. Thus, the inclination angle of the swash plate 18 that affects the discharge capacity changes. When the differential pressure (Pc−Ps) increases, the inclination angle of the swash plate 18 decreases, and the discharge capacity decreases. When the differential pressure (Pc−Ps) decreases, the inclination angle of the swash plate 18 increases and the discharge capacity increases. The electric first capacity control valve 25 in the rear housing 13 controls the refrigerant supply from the discharge chamber 132 to the control pressure chamber 121. The electric second capacity control valve 42 in the rear housing 13 controls the extraction of the refrigerant from the control pressure chamber 121 to the suction chamber 131. The control pressure Pc in the control pressure chamber 121 is controlled by supplying the refrigerant from the first capacity control valve 25 and extracting the refrigerant from the second capacity control valve 42.
[0032]
As shown in FIG. 4, the first capacity control valve 25 includes a solenoid 26 and a valve mechanism 27. The solenoid 26 includes a coil 261, a fixed iron core 262, a movable iron core 263, a drive rod 264 fixed to the movable iron core 263, and a return spring 265. The valve mechanism 27 includes a housing 28, a valve body 29 accommodated in a valve chamber 281 in the housing 28, and a holding spring 30 that holds the valve body 29. The movable iron core 263 is attracted and biased toward the fixed iron core 262 by supplying current to the coil 261. That is, the driving force of the solenoid 26 is transmitted to the valve body 29 via the drive rod 264, and the valve body 29 is biased in the direction of closing the valve hole 282. The return spring 265 biases the movable iron core 263 in a direction away from the fixed iron core 262.
[0033]
A port 283 is formed in the housing 28. The valve chamber 281 communicates with the control pressure chamber 121 through the port 283 and the passage 31, and the valve hole 282 communicates with the discharge chamber 132 through the passage 32. As shown in FIG. 4, when the valve element 29 is in a position where the valve hole 282 is opened, the high-pressure refrigerant in the discharge chamber 132 is a refrigerant supply passage including a passage 32, a valve hole 282, a valve chamber 281, a port 283, and a passage 31. Is sent to the control pressure chamber 121 via.
[0034]
The sum of the driving force Fd of the solenoid 26 and the spring force F2 of the holding spring 30 opposes the sum of the total pressure Pd1 of the discharge pressure Pd acting on the valve body 29 and the spring force F1 of the return spring 265. That is, when the total pressure Pd1 of the discharge pressure Pd exceeds (Fd + F2-F1), the valve element 29 opens the valve hole 282, and the high-pressure refrigerant in the discharge chamber 132 flows into the control pressure chamber 121. When the total pressure Pd1 of the discharge pressure Pd does not exceed (Fd + F2-F1), the valve element 29 closes the valve hole 282, and the high-pressure refrigerant in the discharge chamber 132 does not flow into the control pressure chamber 121. That is, the first capacity control valve 25 that controls the supply of refrigerant from the discharge chamber 132 to the control pressure chamber 121 operates so as to keep the discharge pressure Pd constant.
[0035]
The second capacity control valve 42 includes a solenoid 43 and a valve mechanism 44. The solenoid 43 includes a coil 431, a fixed iron core 432, a movable iron core 433, a drive rod 434 fixed to the movable iron core 433, and a return spring 435. The valve mechanism 44 includes a housing 45, a valve body 46 that is coupled to the drive rod 434 and accommodated in the valve chamber 451 in the housing 45, a bellows 48 that is accommodated in the valve chamber 451 and coupled to the drive rod 434, The spring 49 acts on the pressure receiving plate 481 in the direction in which the bellows 48 extends. The valve chamber 451 communicates with the control pressure chamber 121 via the valve hole 453 and the passage 47, and the port 452 communicates with the suction chamber 131 via the passage 50. As shown in FIG. 5, when the valve element 29 is in a position where the valve hole 453 is opened, the refrigerant in the control pressure chamber 121 is a refrigerant extraction passage including a passage 47, a valve hole 453, a valve chamber 451, a port 452, and a passage 50. It flows out to the suction chamber 131 via.
[0036]
The suction pressure Ps of the suction chamber 131 is applied to the valve chamber 451 via the passage 50 and the port 452, and the spring force F4 of the spring 49 opposes the total pressure Ps1 of the suction pressure Ps acting on the pressure receiving plate 481. The movable iron core 433 is attracted and biased toward the fixed iron core 432 by supplying current to the coil 431. That is, the driving force of the solenoid 43 opposes the spring force of the spring 49. The return spring 435 biases the movable iron core 433 in a direction away from the fixed iron core 432.
[0037]
  The sum of the driving force Fs of the solenoid 43 and the total pressure Ps1 of the suction pressure Ps with respect to the pressure receiving plate 481 is opposite to the sum of the spring force F3 of the return spring 435 and the spring force F4 of the spring 49. Total pressure Ps1 is (F3 + F4-Fs), The valve body 46 closes the valve hole 453 and the total pressure Ps1 is (F3 + F4-F).s), The valve body 46 opens the valve hole 453. That is, the second capacity control valve 42 that controls the extraction of the refrigerant from the control pressure chamber 121 to the suction chamber 131 operates to keep the suction pressure Ps constant.
[0038]
The solenoid 26 of the first capacity control valve 25 and the solenoid 43 of the second capacity control valve 42 are subjected to current supply control by the controller 33. The controller 33 includes a target discharge pressure determination unit 331 serving as a target discharge pressure determination unit, a target suction pressure determination unit 332 serving as a target suction pressure determination unit, and a first current supply control unit serving as a first current supply control unit. 333 and a second current supply control unit 334 serving as a second current supply control means. The controller 33 controls the capacity adjustment states of the first capacity control valve 25 and the second capacity control valve 42 based on the capacity adjustment state control program shown in the flowchart of FIG. The target discharge pressure determining unit 331 samples the outdoor temperature Te detected by the outdoor temperature detector 34 and the indoor temperature Ts detected by the indoor temperature detector 35 at predetermined time intervals. The target suction pressure determination unit 332 samples the room temperature Ts detected by the room temperature detector 35 at a predetermined time interval.
[0039]
The target discharge pressure determination unit 331 sets the outside air temperature Te detected by the outside air temperature detector 34, the indoor temperature Ts detected by the indoor temperature detector 35, and the target indoor temperature To set by the target indoor temperature setter 36. Based on this, the target discharge pressure Pdo is determined. If the outside air temperature Te increases, the discharge capacity needs to be increased. Further, if the heat load increases in a high level region, it is necessary to increase the discharge capacity. The relationship between the outside air temperature Te and the thermal load and the target discharge pressure Pdo is determined in advance based on the necessity as described above, and the target discharge pressure determination unit 331 is based on the outside air temperature information, the heat load information, and the relationship. The target discharge pressure Pdo is determined. The first current supply control unit 333 controls current supply to the solenoid 26 of the first capacity control valve 25 so as to bring about the target discharge pressure Pdo determined by the target discharge pressure determination unit 331.
[0040]
The target suction pressure determining unit 332 determines the target suction pressure Pso based on the detected room temperature Ts and the target room temperature To. The difference between the target room temperature To and the room temperature Ts reflects the heat load, and the target suction pressure determination unit 332 determines the target suction pressure Pso based on the heat load. If the heat load increases, the suction pressure Ps needs to be lowered. The relationship between the heat load and the target suction pressure Pso is determined in advance based on the necessity as described above, and the target suction pressure determination unit 332 determines the target suction pressure Pso based on the heat load information and the relationship. . The second current supply control unit 334 controls the current supply to the solenoid 43 of the second capacity control valve 42 so as to bring about the target suction pressure Pso determined by the target suction pressure determination unit 332.
[0041]
The following effects can be obtained in the first embodiment.
(1-1) The discharge capacity is adjusted by the differential pressure between the control pressure Pc in the control pressure chamber 121 and the suction pressure Ps, and the differential pressure between the control pressure Pc and the suction pressure Ps is the current to the first capacity control valve 25. It is quickly adjusted by supply control. The discharge capacity is substantially proportional to the discharge pressure Pd, and the discharge pressure Pd reflects the discharge capacity. That is, the target discharge pressure Pdo defines the capacity adjustment state of the first capacity control valve 25. The target discharge pressure determining unit 331 quickly determines the target discharge pressure Pdo based on external information such as the outside air temperature Te and the heat load. The change in the rotational speed of the vehicle engine causes the rotational speed of the rotating shaft 14 to change, and the discharge pressure Pd tends to change. The discharge pressure Pd reflecting the discharge capacity is determined based on the external information such as the outside air temperature Te. The constant pressure is controlled to a constant value of the pressure Pdo. Therefore, the fluctuation of the discharge capacity due to the fluctuation of the rotation speed of the rotating shaft 14 is suppressed by the constant pressure control of the discharge pressure according to the outside air temperature Te by the controller 33 and the first capacity control valve 25. As a result, the variable displacement compressor is prevented from performing more work than necessary due to the fluctuation in the rotational speed of the compressor, and the power consumption and load in the variable displacement compressor are reduced.
(1-2) The differential pressure between the control pressure Pc and the suction pressure Ps is quickly adjusted also by current supply control to the second capacity control valve 42. The suction pressure Ps directly reflects the heat load, and the heat load directly reflects the room temperature. Therefore, the suction pressure Ps is preferably controlled for controlling the room temperature. The target suction pressure Pso defines the capacity adjustment state of the second capacity control valve 42. The target suction pressure determination unit 332 quickly determines the target suction pressure Pso based on external information such as heat load. Although the fluctuation of the heat load causes the fluctuation of the suction pressure Ps, the suction pressure Ps reflecting the heat load is quickly controlled to the target suction pressure Pso determined based on the external information of the heat load. Therefore, it is possible to prevent the variable capacity compressor from performing more work than necessary due to fluctuations in the heat load.
(1-3) Even when the thermal load is in a high level region, the discharge pressure Pd is controlled to a constant value, ie, a target discharge pressure Pdo determined based on external information such as the heat load. Accordingly, the fluctuation of the discharge capacity corresponding to the fluctuation of the heat load in the high level range is appropriately adjusted by the control of the discharge pressure according to the heat load by the controller 33 and the first capacity control valve 25, and the variable capacity compression The machine is prevented from doing more work than necessary.
(1-4) It is desirable that the indoor temperature can be controlled precisely. The second capacity control valve 42 for controlling the suction pressure Ps is suitable for fine control of the room temperature, but is not suitable for capacity adjustment with respect to a large rotational speed fluctuation of the compressor. The first capacity control valve 25 that controls the discharge pressure Pd is suitable for adjusting the capacity against a large fluctuation in the rotational speed of the compressor, but is not suitable for fine control of the room temperature. The configuration in which the discharge pressure control with respect to the rotational speed fluctuation and the suction pressure control with respect to the thermal load fluctuation are appropriately shared by the two capacity control valves 25 and 42, while reducing the power consumption and load in the variable capacity compressor, is good. Enables air conditioning to be achieved.
(1-5) Since the fluctuation of the outside air temperature and the heat load are moderate, the controller 33 is not required to have such a high speed processing function. Therefore, the control system can be constructed at low cost.
(1-6) When the heat load is high, it is necessary to increase the discharge capacity. When the heat load is low, it is necessary to reduce the discharge capacity. Therefore, the thermal load grasped based on the room temperature Ts and the target room temperature To is appropriate as external information for quickly adjusting the discharge capacity.
[0042]
Next, a second embodiment of FIG. 8 will be described. The internal structure of the variable capacity compressor is the same as that of the first embodiment, and the same components as those of the first embodiment are denoted by the same reference numerals.
[0043]
In the second capacity control valve 51 in this embodiment, the suction pressure Ps of the suction chamber 131 is spread to the pressure sensing chamber 511, and the suction pressure Ps in the pressure sensing chamber 511 is springed by the spring 52 via the diaphragm 512. The spring force of the spring 52 can be adjusted by the screwing position of the screw 53. The displacement of the diaphragm 512 is transmitted to the valve body 514 through the displacement transmission rod 513. The second capacity control valve 51 is also a control valve for setting the target suction pressure, like the second capacity control valve 42 in the first embodiment, but the target suction pressure is set by setting the spring force of the spring 52. . The capacity adjustment state of the first capacity control valve 25 is performed by the controller 54 including the target discharge pressure determination unit 331 and the first current supply control unit 333 as in the case of the first embodiment.
[0044]
Also in this embodiment, the same effect as the items (1-1) and (1-3) in the first embodiment can be obtained.
Next, a third embodiment of FIG. 9 will be described. The internal structure of the variable capacity compressor is the same as that of the first embodiment, and the same components as those of the first embodiment are denoted by the same reference numerals.
[0045]
The solenoid 56 of the second capacity control valve 55 includes a coil 561, a fixed iron core 562, a movable iron core 563, a drive rod 564 secured to the movable iron core 563, and a return spring 565. The valve mechanism 44 is housed in a housing 57, a valve body 58 accommodated in a valve chamber 571 in the housing 57, a holding spring 59 that holds the valve body 58, and a pressure sensing chamber 572 in the housing 57. A bellows 60 coupled to the rod 564 and a spring 61 acting on the pressure receiving plate 601 in a direction in which the bellows 60 is extended. The suction pressure Ps of the suction chamber 131 is spread to the pressure sensing chamber 572 via the passage 50 and the port 575, and the spring force F4 of the spring 61 opposes the total pressure Ps1 of the suction pressure Ps acting on the pressure receiving plate 601. The movable iron core 563 is attracted and biased toward the fixed iron core 562 by supplying current to the coil 561. That is, the driving force of the solenoid 56 opposes the spring force of the spring 61. The return spring 565 biases the movable iron core 563 in a direction away from the fixed iron core 562. When the valve hole 573 is opened, the high-pressure refrigerant in the discharge chamber 132 is sent to the control pressure chamber 121 via the passages 62 and 63. The suction pressure Ps in the suction chamber 131 is spread to the pressure sensitive chamber 572 via the passage 64.
[0046]
The sum of the driving force Fo of the solenoid 56 and the total pressure Ps1 of the suction pressure Ps with respect to the pressure receiving plate 601 is opposite to the sum of the spring force F5 of the return spring 565 and the spring force F6 of the spring 61. When the total pressure Ps1 falls below (F5 + F6-Fo), the valve element 58 opens the valve hole 573. When the total pressure Ps1 exceeds (F5 + F6-Fo), the valve element 58 closes the valve hole 573. That is, the capacity control valve 55 operates to control the supply of refrigerant from the discharge chamber 132 to the control pressure chamber 121 and keep the suction pressure Ps constant.
[0047]
Refrigerant extraction from the control pressure chamber 121 to the suction chamber 131 is performed via the throttle passage 66.
The target discharge pressure determining unit 651 of the controller 65 determines the target discharge pressure Pdo based on the outside air temperature Te detected by the outside air temperature detector 34. If the outside air temperature Te increases, the discharge capacity needs to be increased. The first current supply control unit 653 controls the current supply to the solenoid 26 of the first capacity control valve 25 so as to bring the target discharge pressure Pdo determined by the target discharge pressure determination unit 651.
[0048]
The target intake pressure determination unit 652 determines the target intake pressure Pso based on the indoor temperature Ts detected by the indoor temperature detector 35 and the target indoor temperature To set by the target indoor temperature setter 36. The second current supply control unit 654 controls current supply to the solenoid 56 of the second capacity control valve 55 so as to bring about the target suction pressure Pso determined by the target suction pressure determination unit 652.
[0049]
In this embodiment, the first capacity control valve 25, the target discharge pressure determination unit 651, and the first current supply control unit 653 take charge of the discharge pressure fluctuation suppression control with respect to the rotation speed fluctuation, and the second capacity control valve 55, The target suction pressure determination unit 652 and the second current supply control unit 654 are responsible for suction pressure control for thermal load fluctuations. Therefore, also in this embodiment, the same effect as the item (1-4) in the first embodiment can be obtained.
[0050]
In the present invention, the following embodiments are also possible..
(1) In the third embodiment, the target discharge pressure is determined from the outside air temperature and the thermal load as in the case of the first embodiment.
(2) The first capacity control valve is an electromagnetic on-off valve, and the on-off control of the electromagnetic on-off valve is performed so as to bring about a target discharge pressure.
(3) The second capacity control valve is an electromagnetic on-off valve, and the on-off control of the electromagnetic on-off valve is performed so as to bring about the target suction pressure.
[0051]
【The invention's effect】
  As described above in detail, in the present invention, the first capacity control for controlling the refrigerant supply from the discharge pressure region to the control pressure chamber.ValveSince the capacity adjustment state is determined based on external information, in a variable capacity compressor used in a refrigeration circuit that performs heat exchange, including cooling the refrigerant in a supercritical region exceeding the critical temperature of the refrigerant. There is an excellent effect that power consumption and load can be reduced.
[Brief description of the drawings]
FIG. 1 is a side sectional view of an entire compressor showing a first embodiment of the present invention.
FIG. 2 is a cross-sectional view taken along line AA in FIG.
3 is a cross-sectional view taken along line BB in FIG.
FIG. 4 is an enlarged side sectional view of a main part.
FIG. 5 is an enlarged side sectional view of a main part.
FIG. 6 is a Mollier diagram.
FIG. 7 is a flowchart showing a capacity adjustment state control program.
FIG. 8 is an enlarged cross-sectional side view of a main part showing a second embodiment.
FIG. 9 is an enlarged side cross-sectional view of a main part showing a third embodiment.
[Explanation of symbols]
121: Control pressure chamber, 131: Suction chamber as a suction pressure region, 132: Discharge chamber as a discharge pressure region, 25: First capacity control valve, 42, 51 ... Second capacity control valve, 33, 54, 65 ... Controller as capacity adjustment state control means, 331, 651 ... Target discharge pressure determination section as target discharge pressure determination means, 332, 652 ... Target suction pressure determination section as target suction pressure determination means, 333, 653 ... No. A first current supply control unit serving as one current supply control unit, 334, 654 ... a second current supply control unit serving as a second current supply control unit, 34 ... an outside air temperature detector serving as an outside air temperature detection unit, 35 ... Indoor temperature detector constituting thermal load detecting means.

Claims (7)

冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられ、制御圧室の制御圧と吸入圧領域の吸入圧との差圧の変化に基づいて吐出容量を変える可変容量型圧縮機において、
前記制御圧と吸入圧との差圧を第1の容量制御弁及び第2の容量制御弁によって制御し、前記第1の容量制御弁は吐出圧を一定に保つように動作する目標吐出圧設定用の電気式容量制御弁であり、外気温度及び熱負荷を検出し、検出された外気温度及び熱負荷に基づいて前記目標吐出圧を決定し、前記決定された目標吐出圧をもたらすように前記第1の容量制御弁に対する電流供給が制御される可変容量型圧縮機の動作制御方法。
Used in refrigeration circuits that perform heat exchange, including cooling the refrigerant in a supercritical region that exceeds the critical temperature of the refrigerant, and based on the change in the differential pressure between the control pressure in the control pressure chamber and the suction pressure in the suction pressure region In variable displacement compressors that change the discharge capacity
A differential pressure between the control pressure and the suction pressure is controlled by a first capacity control valve and a second capacity control valve, and the first capacity control valve operates to keep the discharge pressure constant. An electric capacity control valve for detecting outside air temperature and heat load, determining the target discharge pressure based on the detected outside air temperature and heat load, and providing the determined target discharge pressure An operation control method for a variable displacement compressor in which current supply to a first displacement control valve is controlled .
吐出圧領域から前記制御圧室への冷媒供給を前記第1の容量制御弁によって制御し、前記制御圧室から前記吸入圧領域への冷媒抜き出しを前記第2の容量制御弁によって制御し、第2の容量制御弁の容量調整状態を外気温度又は熱負荷を含む外部情報に基づいて決定する請求項1に記載の可変容量型圧縮機の動作制御方法。The refrigerant supply from the discharge pressure region to the control pressure chamber is controlled by the first capacity control valve, the refrigerant extraction from the control pressure chamber to the suction pressure region is controlled by the second capacity control valve , operation control method for a variable displacement compressor according to claim 1 for determining on the basis of external information including the capacity adjustment state of the second capacity control valve outside air temperature or thermal load. 前記第2の容量制御弁は吸入圧を一定に保つように動作する目標吸入圧設定用の電気式容量制御弁である請求項1及び請求項2のいずれか1項に記載の可変容量型圧縮機の動作制御方法。 3. The variable capacity compression according to claim 1, wherein the second capacity control valve is an electric capacity control valve for setting a target suction pressure that operates so as to keep the suction pressure constant. 4. Machine operation control method. 熱負荷を検出し、検出された熱負荷に基づいて前記目標吸入圧を決定し、前記決定された目標吸入圧をもたらすように前記第2の容量制御弁に対する電流供給を制御する請求項3に記載の可変容量型圧縮機の動作制御方法。 4. The method according to claim 3 , wherein a thermal load is detected, the target suction pressure is determined based on the detected thermal load, and a current supply to the second capacity control valve is controlled so as to bring about the determined target suction pressure. The operation | movement control method of the variable capacity compressor of description. 冷媒の臨界温度を越えた超臨界域で冷媒を冷却するという場合を含む熱交換を行なう冷凍回路に用いられ、制御圧室の制御圧と吸入圧領域の吸入圧との差圧の変化に基づいて吐出容量を変える可変容量型圧縮機において、
前記制御圧と前記吸入圧との差圧を制御する第1の容量制御弁と、
前記制御圧と前記吸入圧との差圧を制御する第2の容量制御弁と、
少なくとも、前記第1の容量制御弁の容量調整状態を決定する容量調整状態制御手段と
外気温度を検出する外気温度検出手段及び熱負荷を検出する熱負荷検出手段とを備え、前記容量調整状態制御手段は、前記外気温度検出手段によって検出された外気温度及び前記負荷検出手段によって検出された熱負荷に基づいて前記目標吐出圧を決定する目標吐出圧決定手段と、前記決定された目標吐出圧をもたらすように前記第1の容量制御弁に対する電流供給を制御する第1の電流供給手段とを備えている可変容量型圧縮機の動作制御装置。
Used in refrigeration circuits that perform heat exchange, including cooling the refrigerant in a supercritical region that exceeds the critical temperature of the refrigerant, and based on the change in the differential pressure between the control pressure in the control pressure chamber and the suction pressure in the suction pressure region In variable displacement compressors that change the discharge capacity
A first capacity control valve that controls a differential pressure between the control pressure and the suction pressure;
A second capacity control valve for controlling a differential pressure between the control pressure and the suction pressure;
Capacity adjustment state control means for determining at least the capacity adjustment state of the first capacity control valve;
An outside air temperature detecting means for detecting an outside air temperature and a heat load detecting means for detecting a thermal load, wherein the capacity adjustment state control means is detected by the outside air temperature detected by the outside air temperature detecting means and the load detecting means. Target discharge pressure determining means for determining the target discharge pressure based on the thermal load, and first current supply means for controlling the current supply to the first capacity control valve so as to bring the determined target discharge pressure An operation control device for a variable capacity compressor .
前記第1の容量制御弁は吐出圧領域から前記制御圧室への冷媒供給を制御し、前記第2の容量制御弁は前記制御圧室から前記吸入圧領域への冷媒抜き出しを制御する請求項に記載の可変容量型圧縮機の動作制御装置 The first capacity control valve controls refrigerant supply from a discharge pressure region to the control pressure chamber, and the second capacity control valve controls refrigerant extraction from the control pressure chamber to the suction pressure region. 5. An operation control device for a variable capacity compressor according to claim 5 . 前記容量調整状態制御手段は、前記熱負荷検出手段によって検出された熱負荷に基づいて前記目標吸入圧を決定する目標吸入圧決定手段と、前記決定された目標吸入圧をもたらすように前記第2の容量制御弁に対する電流供給を制御する第2の電流供給制御手段とを備えている請求項5及び請求項6のいずれか1項に記載の可変容量型圧縮機の動作制御装置 The capacity adjustment state control means includes target suction pressure determination means for determining the target suction pressure based on the thermal load detected by the thermal load detection means, and the second target so as to bring the determined target suction pressure. The variable capacity compressor operation control device according to any one of claims 5 and 6, further comprising second current supply control means for controlling current supply to the capacity control valve .
JP02605098A 1998-02-06 1998-02-06 Operation control method and operation control apparatus for variable capacity compressor Expired - Fee Related JP3752816B2 (en)

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JP02605098A JP3752816B2 (en) 1998-02-06 1998-02-06 Operation control method and operation control apparatus for variable capacity compressor
US09/243,715 US6138468A (en) 1998-02-06 1999-02-03 Method and apparatus for controlling variable displacement compressor
DE69925653T DE69925653T2 (en) 1998-02-06 1999-02-05 Method and device for controlling a variable capacity compressor
EP99102296A EP0935107B1 (en) 1998-02-06 1999-02-05 Method and apparatus for controlling variable displacement compressor

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