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JPH036359B2 - - Google Patents
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JPH036359B2 - - Google Patents

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Publication number
JPH036359B2
JPH036359B2 JP60289227A JP28922785A JPH036359B2 JP H036359 B2 JPH036359 B2 JP H036359B2 JP 60289227 A JP60289227 A JP 60289227A JP 28922785 A JP28922785 A JP 28922785A JP H036359 B2 JPH036359 B2 JP H036359B2
Authority
JP
Japan
Prior art keywords
pump
tank
liquid
compressor
valve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60289227A
Other languages
Japanese (ja)
Other versions
JPS61167199A (en
Inventor
Masanori Tanaka
Kimisaki Ogawa
Ishinosuke Umezawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Airman Corp
Original Assignee
Hokuetsu Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hokuetsu Industries Co Ltd filed Critical Hokuetsu Industries Co Ltd
Priority to JP28922785A priority Critical patent/JPS61167199A/en
Publication of JPS61167199A publication Critical patent/JPS61167199A/en
Publication of JPH036359B2 publication Critical patent/JPH036359B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、回転圧縮機の圧縮室中に液体を吐出
せしめて冷却、潤滑、密封の作用を行わしめる回
転圧縮機の改良に関する。 [従来の技術] 一般にこの種の圧縮機は、第2図に示すよう
に、圧縮機のロータ12,22の回転中常時回転
駆動されるポンプ2を備え、該ポンプ2により液
体を圧縮室17,27中に供給するとともに、圧
縮機からガスと共に吐出される液体をガスと共に
タンク5に貯溜し、タンク内においてガスと分離
された液体を前記ポンプに供給するようにされて
いる。一方圧縮機は、圧縮ガスの需要が減少した
際は、タンク内の圧力が所定値を超えると負荷軽
減装置を作用せしめて圧縮機シリンダの吸気口面
積を閉塞弁を用いて減少または閉塞させて圧縮機
の吸入ガスを低減または零とし、必要に応じ同時
に原動機の回転を減少せしめることにより、低負
荷運転または無負荷運転を行わせ、消費動力の節
減を図つている。 ところで上記低負荷または無負荷運転時には、
閉塞弁の作動によりガスは殆んど圧縮機の圧縮室
中に吸入されないのに対し、冷却、潤滑または密
封用の液体は圧縮機のロータの回転速度に比例し
て圧縮室中に吐出されるため、前記閉塞弁による
圧縮機の吸気口開度の減少に同期せしめて、タン
クから前記ポンプに送る液体量を減少せしめる流
量調整弁を設けること、および圧縮機ロータの回
転中回転駆動される第2のポンプを設けて、前記
圧縮機ケーシングの吐出口に貯溜するガスおよび
ガスから分離される液体を該ポンプによりタンク
に還流せしめるものが、実公昭55−22227号の考
案、および特開昭51−45315号の発明等で提案さ
れている。 第2図は上記特開昭51−45315号の発明を実施
した空気圧縮機を示すものであつて、第1段圧縮
機11、第2段圧縮機21、第1のポンプ2およ
び第2のポンプ3は回転数一定のモータ1に直列
状に配列され、モータ1により圧縮機11,21
のロータ12,22およびポンプ2,3のロータ
をそれぞれ回転駆動せしめられる。圧縮機11,
12はともにスクリユー型のもので、ロータ1
2,22はそれぞれ雄型スクリユー、雌型スクリ
ユーからなり、これらスクリユーが同期して反対
方向に回転せしめられ、軸方向に気体を圧縮する
形式のものであつて、フイルタ6から吸入された
空気は負荷軽減装置31の通孔33を経て第1段
圧縮機11の吸入口14に吸入され、圧縮機11
の圧縮機17で圧縮されてその吐出口15から第
2段圧縮機21の吸入口24に入り、圧縮機21
の圧縮室27で圧縮されてその吐出口25から不
還弁4を経てタンク5内に貯溜される。 圧縮機11,21の潤滑、密封および冷却用の
油は第1のポンプ2の吐出口から通路51を経て
第1の圧縮機11のケーシング13に形成された
通孔16および第2段圧縮機21のケーシング2
3に形成された通孔26にそれぞれ連通せしめら
れて圧縮機11,21の圧縮室17,27内に噴
射され、第2段圧縮機21の吐出口25に圧縮空
気と共に吐出されタンク5内に送り込まれる。タ
ンク5内には空気と油とを分離する分離機(図示
せず)が内蔵され、タンク5の底部に溜つた油は
油排出口44よび通路52、クーラ9を経て通路
53、濾過器7、流量調整弁8を経て、通路54
により第1のポンプ2の吸入口に還流して循環せ
しめられる。第2のポンプ3は前記第2段圧縮機
21の吐出口25において分離された油をドレイ
ン28から通路55を経て該ポンプ3の吸入口に
吸い込み、吐出口から通路56を経て油還流口4
7よりタンク5内に還流せしめる。 負荷軽減装置は特開昭51−45315号公報に開示
されているように、前記タンク5内の空気圧が上
昇して所定値の調整圧力点に達したとき該タンク
5から導かれて圧力調整弁(図示せず)を経て圧
力室38に導入された空気圧と、該タンク5から
導かれて減圧弁(図示せず)を経て圧力室37に
導入された空気圧のバランスによりピストン36
を移動させて閉塞弁34を作動させて前記通孔3
3を閉塞し、第1段圧縮機11の吸入空気量を零
とするもので、前記圧力調整弁からの空気圧は同
時に前記流量調整弁8にも配分され、該弁8に内
蔵される弁体をその空気圧で移動させ、通路53
および54を結ぶ該流量調整弁8内の内部通路の
面積を絞るように構成されている。 [発明が解決しようとする問題点] 以上のように構成された回転圧縮機にあつて
は、前記タンク5の圧縮空気取出口60より圧縮
空気が消費されている間は閉塞弁34は通孔33
を全開し、圧縮機11,21は空気を圧縮してタ
ンク5に圧縮空気を吐出する全負荷運転状態と
し、油は第1のポンプ2によつて圧縮機11,2
1に噴出されて潤滑を行つているが、圧縮空気取
出口60からの取り出される圧縮空気の消費が減
少し、または消費が停止するとタンク5内の空気
圧が上昇し、所定値に達すると前記図示しない圧
力調整弁からの空気圧によつて負荷軽減装置31
は閉塞弁34が通孔33を全閉して吸気を零とす
るとともに、ポンプ3により吐出口29(吐出口
25から不還弁4までの空間)内の空気および油
を排出除去して不還弁4を閉じ、該吐出室内の圧
力を著しく低下せしめてロータ背圧を除去し、無
負荷運転に移行する。このとき第1段圧縮機11
への吸入空気量および吐出室への吐出空気量は零
となるが、流量調整弁8の作用により圧縮機1
1,21の潤滑のための最小限の量の油の供給は
確保せしめている。しかしながら第1のポンプ2
の吸入側において流量調整弁8が油の流量を絞る
ため、通路54が真空状態となつてポンプ2より
いわゆる真空音といわれる異音を発生し、同時に
該流量調整弁8の上流側のクーラ9を流れる油量
も激減するため、クーラの熱貫流率が低下する。 以上のように構成された圧縮機にあつては、万
一負荷軽減装置31の閉塞弁34が通孔33を完
全に閉塞せず、閉塞弁34と通孔33との間に空
気の流量を許す僅かの〓間が残存する閉塞不完全
の状態が生ずると、前記〓間から僅かではあるが
空気が圧縮室17,27に吸入され、圧縮されて
圧縮熱を発生する。しかしながら流量調整弁8の
作用により圧縮室17,27には最小限の量の液
体が供給されているのみであるから、冷却・潤滑
および密封用の液体は過熱されて圧縮空気ととも
に吐出室29に吐出され、タンク5内へ還流させ
られるような負荷軽減装置31の吸気閉塞不完全
の状態が続くと、タンク5内の液体温度が上昇す
る。また第2のポンプ3を具備しない圧縮機にお
いては、負荷軽減装置31の吸気閉塞不完全の状
態が生ずると、前記過熱された液体が圧縮空気と
ともに吐出室29に滞留し、不還弁4を作用せし
める圧力を超えた分だけをタンク5内に還流させ
るのみとなるので、圧縮機ケーシング23の過熱
をも併発するおそれがある。第2のポンプ3に万
一吸引不完全が生じた場合も同様である。そして
吐出室29内に圧縮空気と液体とが滞留すると吐
出室内の圧力が圧縮機のロータの背圧として作用
し、負荷軽減装置31の作動中といえども消費動
力は70%程度にしか低下しない。 [問題点を解決するための手段] 圧縮室に冷却・潤滑および密封用の液体を噴射
供給して運転する回転圧縮機においては、負荷軽
減装置を具備せしめて無負荷運転を行う際に、前
記負荷軽減装置による吸入ガスの閉塞遮断と同時
に、該負荷軽減装置の作動と同期せしめて、圧縮
室に供給する液体の量を低減せしめることが消費
動力の節減上有利である。このために、前記負荷
軽減装置の作動と同期して作動する流量調整弁
を、前記圧縮室へ液体を供給するポンプの液体通
路中に配設することを常とするが、前記ポンプの
吸入側をクーラを介してタンクの液体排出口に油
路で連結し、前記ポンプの吐出側を圧縮機ケーシ
ングの圧縮室に連通せしめた通孔に油路で連結し
た簡単な油路構成では、前記流量調整弁を前記ポ
ンプの吸入側の油路に配設しても、あるいは前記
ポンプの吐出側の油路に配設しても、前記流量調
整弁が液体流量を絞つたときは、前記ポンプを通
る液体流量が減少し、従つてクーラを通る液体流
量が減少するため、前記問題点は解決されない。 本発明は、圧縮機のケーシングと、原動機によ
り駆動されて前記ケーシングの圧縮室内において
回転自在の圧縮機ロータと、該ロータの回転中回
転駆動されるポンプと、該ポンプの吐出口に連結
され前記圧縮室にポンプの吐出する圧縮機の冷
却・潤滑および密封用の液体を供給する通路と、
前記ケーシングから吐出され不還弁を介して供給
されたガスと液体とを貯溜するタンクと、該タン
クの内圧に応じて前記圧縮室の吸収口の開度を調
節する負荷軽減装置と、該負荷軽減装置による圧
縮室の吸入口の開度調節と同期して前記圧縮室に
供給する液体の流量を調節する流量調整弁とを設
けた回転圧縮機において、前記圧縮室に液体を供
給する通路を前記流量調整弁を介して前記ポンプ
の吐出口に連結せしめるとともに、前記ポンプの
吸入口と前記タンクの液体排出口とをクーラを介
して連結せしめ、かつ前記タンクの液体還流口お
よびタンクの液体排出口と前記クーラとの間の通
路との何れか一方と前記ポンプの吐出口とを、前
記ポンプの吐出口の圧力が予め定めた値を超えた
とき過剰の圧の液体を前記タンク側に還流せしめ
るレリーフ弁を介して連結せしめたことを特徴と
し、前記流量調整弁が負荷軽減装置の作動と同期
して圧縮室に液体を供給する通路への流量を絞つ
たときにおいても、前記ポンプから吐出される液
体の余剰分はレリーフ弁を介してタンク側に流れ
るようにし、前記ポンプを流れる液体の流量、従
つてクーラを流れる液体の流量を負荷軽減装置の
作動状態の如何に拘わらず大とし、前記問題点を
解決しようとするものである。 [発明の作用] 本発明によれば、回転圧縮機のロータの回転中
はポンプが駆動され、タンクの液体排出口よりク
ーラを介して液体を吸入口より吸入する。該ポン
プの吐出側は圧縮室へ液体を供給する通路と、レ
リーフ弁を介してタンクの液体還流口および前記
タンクの液前排出口とクーラとの間の通路との少
くとも一方に、連通されているから、回転圧縮機
の全負荷運転時のように圧縮室に多量の液体が冷
却・潤滑および密封のために供給されているとき
は、ポンプから吐出される液体はレリーフ弁を介
してタンク側には還流せず、あるいは還流しても
僅かであり、負荷軽減装置が作動して流量調整弁
が圧縮室へ供給する液体量を制限したときは、ポ
ンプから吐出された液体の余剰分をタンク側に還
流させ、前記ポンプを流れる液体の流量を回転圧
縮機の運転状況に如何に拘らず不変とし、従つて
クーラを流れる液体の流量を負荷軽減装置の作動
不作動および不完全作動に無関係に保証し、冷却
する。 [実施例の説明] 第1図は、第2図と同一形式の回転圧縮機に本
発明を施した本発明の実施例を示すものであつ
て、第2図と同一部分は同一符号を付して示した
ものである。 回転圧縮機はモータ1、第1段圧縮機11、第
2段圧縮機21、第1のポンプ2および第2のポ
ンプ3を直列状に配列し、モータ1により圧縮機
11,12およびポンプ2,3を駆動するように
構成せしめられる。第1段圧縮機11および第2
段圧縮機21はスクリユー型のものであつて、雄
型ロータと雌型ロータの一対(以下単にロータ1
2,22という)が噛合し、第1段圧縮機11の
ケーシング13の吸入口14から吸入した空気を
圧縮して第2段圧縮機21の吐出口25から吐出
した圧縮空気を不還弁4を経てタンク5に貯溜せ
しめるように構成されている。第1段圧縮機11
のケーシング13には吸入口14に連接せしめて
フイルタ6および負荷軽減装置31が設けられ、
空気はフイルタ6、負荷軽減装置31の機枠32
の通孔33を経て圧縮機ケーシング13の吸入口
14に吸入される。 負荷軽減装置31は前記機枠32に軸方向に往
復動自在に装架された閉塞弁34および該閉塞弁
34の軸35に固着されたピストン36により2
個に分割される圧力室37,38を備えており、
前記タンク5内の圧力が上昇して所定値の調整圧
力点に達したとき、該タンク5から導かれる気体
管路および圧力調整弁(共に図示せず)を経て圧
力室38に導入された空気圧と、前記気体管路か
ら分岐し減圧弁(図示せず)を経て圧力室37に
導入される減圧された空気圧のバランスにより、
前記ピストン36を作動せしめて前記閉塞弁34
により通孔33の開口面積を全開し、または通孔
33を完全に閉塞せしめるものである。モータ1
は誘導型の回転数一定のものであつて、前記閉塞
弁34が通孔33を全開し圧縮機の圧縮作用を行
う間は負荷運転状態とされ、前記閉塞弁34が通
孔33を閉塞したときは第2のポンプ3によりド
レイン28より空気および油を排出除去すること
によつて圧縮機の吐出室29(吐出口25から不
還弁4までの空間)の圧力を著るしく低下せし
め、ロータに作用する背圧を除去せしめることに
より、消費動力が全負荷時の20%以下の無負荷運
転状態とされている。 冷却・潤滑および密封用液体としての潤滑油
は、第1のポンプ2の吐出口から通路40を介し
て濾過器7および流量調整弁8を経て通路41へ
送られ、ケーシング13の通孔16を通つて第1
段圧縮機11の圧縮室17へ、またケーシング2
3の通孔26を通つて第2段圧縮機21の圧縮室
27へ吐出せしめられる。圧縮機11,21の圧
縮室17,27に吐出された油はロータ12,2
2の摺動面を潤滑密封するとともに冷却作用を行
い、圧縮空気と共に第2段圧縮機21の吐出室2
5に吐出せられ、不還弁4を介して圧縮空気と共
にタンク5に入る。タンク5内には空気と油を分
離する分離器(図示せず)が内蔵されており、油
はタンク5内の下部に貯溜される。前記第1のポ
ンプ2の吸入口は通路42、クーラ9および通路
43を介して前記タンク5の油排出口44に連通
され、タンク5内で空気と分離された油はクーラ
9により冷却され、第1のポンプ2で昇圧されて
圧縮機11,12を潤滑し、タンク5に戻るよう
に循環される。一方第2のポンプ3はその吸入口
が通路45を介して第2段圧縮機21の吐出室2
9の油溜り部に設けられたドレイン28に連通せ
しめられ、前記吐出口25から吐出され、吐出室
29において空気と分離された油を吸入し、その
吐出口から通路46を介してタンク5の油還流口
47に、または点線図示の通路49および通路4
8を介して油排出口44とクーラ9とを結ぶ油路
43に還流せしめる。 前記流量調整弁8は第2図と同一の公知のもの
で、前記圧力調整弁を経て圧力気体が導入され、
該圧力気体の圧力により内蔵する弁体が移動する
と通路40から通路41へ通ずる調整弁8の内部
通路面積を絞るもので、タンク5内の空気圧が所
定値の調整圧力点に達したとき、前記負荷軽減装
置31における吸入用通孔33の閉塞と同期せし
めて前記調整弁8のの内部通路を2段階または無
段階に絞るように流量調整を行うものである。上
記流量調整弁の制御方式は図示のものに限定され
るものではなく、前記閉塞弁34の移動により直
接制御される実公昭55−22227号公報所載のもの
等も使用できる。 符号50はレリーフ弁を示し、前記第1のポン
プ2の吐出口と連結する通路40内の油圧が所定
値を超えたとき過剰圧油を通路48により前記通
路43に還流せしめ、または点線図示の通路49
により油還流口47に還流せしめるもので、上記
一方向のみの液体流れを許容する制御弁である。 上記のように構成するときは、油はタンク5の
油排出口44より通路43を経てクーラ9で冷却
され、通路42を介して第1のポンプ2に吸入さ
れ、その吐出口から通路40、濾過器7を経て流
量調整弁8により流量を調整され、通路41、お
よびケーシング13の通孔16を介して第1段圧
縮機11の圧縮室17へ、通路41、およびケー
シング23の通孔26を介して第2段圧縮機21
の圧縮室27へそれぞれ噴射供給される。圧縮室
17,27に噴射された油は圧縮空気と共に第2
段圧縮機21の吐出口25より吐出室29を経て
タンク5内に還流され、前記圧縮機21の吐出室
29において空気から分離された油はドレイン2
8から通路45を経て第2のポンプ3に吸入さ
れ、通路46を経てタンク5に戻される。 タンク5内の圧縮空気が取出口60より取り出
され消費されている間は回転圧縮機は全負荷運転
状態にあり、閉塞弁34は通孔33を全開し、流
量制御弁8は充分な量の油を圧縮機11,21に
供給するように内部通路の面積を大に調整されて
いる。 ところで圧縮空気取出口60より取り出される
空気の消費量が減り、または全く取り出さなくな
ると、タンク5内の空気圧が上昇し、これが所定
値の調整圧力点に達すると図示しない圧力調整弁
の作用により圧力室38内の圧力が図示しない減
圧弁を経て流入される圧力室37内の圧力より上
昇して閉塞弁34を通孔33に向つて移動させ、
通孔33を閉塞して吸気を停止する。この閉塞弁
34の移動と同期して前記圧力調整弁の作用によ
り流量調整弁8に内蔵する移動弁体が移動して該
調整弁8内の内部通路を絞り、通路41に供給す
る油量を減らし、無負荷運転状態に入る。 無負荷運転状態においては圧縮機11の吸入口
14の吸気を零として運転され気体の圧縮熱は生
じないが、圧縮機11,21は定速回転で運転さ
れるので、油は回転部分の潤滑に必要なだけの量
が圧縮室17,27内に吐出される。このときの
流量調整弁8による油の送出量は全負荷運転時の
半分以下とする。この潤滑用の油は前記第1のポ
ンプ2によりタンク5からクーラ9、通路42を
経て吸入され通路40に吐出されて流量調整弁8
に供給されるが、流量調整弁8の内部通路が絞ら
れたことにより通路40内の液圧が上昇するとレ
リーフ弁50が作動し、所定圧以上の余剰圧油を
通路48よりタンク5またはクーラ9の上流側へ
排出還流せしめる。従つて低負荷運転または無負
荷運転時においてもタンク5、クーラ9、通路4
2には全負荷時と同じ量の油が循環して流れ、油
の温度上昇を防止することができる。また第1の
ポンプ2は無負荷運転時において吐出側圧力が上
昇することがあつてもレリーフ弁50の存在のた
め吐出側圧力は一定値以上に上昇することはな
く、むしろ第2図に示す液体供給回路のように吸
入側が真空状態になることはないので異音発生の
心配はなく、従つて圧縮機の全負荷運転時の油の
供給量によつて選択または設計すれば足りること
となる。そして無負荷運転時においても油は流量
調整弁8を介して圧縮機の圧縮室17,27に供
給され、第2段圧縮機21の吐出口25に吐出さ
れるが、第2のポンプ3が吐出室内の空気と空気
から分離された油を排出除去するので不還弁4が
閉じており、油はドレイン28より通路45を経
て第2のポンプ3に吸入され、通路46を経てタ
ンク5の油還流口47に還流せしめられる。 即ち、前記第2のポンプ3は負荷軽減装置31
が作動して閉塞弁34が通孔33を閉塞し、従つ
て吐出口25に圧縮空気が吐出されなくなつた後
においてもドレイン28より空気および油を排出
し除去するので、吐出室29内の圧力を著るしく
低下せしめ、圧縮機の吸入口14と吐出口25と
の間の圧力差を少くし、ロータ12,22に作用
する背圧を除去するので、圧縮機の消費動力は20
%以下に大巾に低減される。しかしながら前記第
2のポンプ3を具備しない圧縮機にあつては、負
荷軽減装置31が作動して閉塞弁34が通孔33
を閉塞したとき、吐出室29内の圧力は負荷軽減
装置の作動時の圧力に維持され、圧縮機の吸入側
圧力は閉塞弁34が通孔33を閉塞することによ
り負圧になるから、圧縮機のロータ12,22に
は吐出室内の圧力以上の圧力差(背圧)が作用し
た状態で運転される。 このような無負荷運転状態において、万一閉塞
弁34の着座不完全が生じ、負荷軽減装置31の
通孔33から僅かでも空気が圧縮室17,27に
吸入された場合には、圧縮空気と該空気の圧縮熱
により過熱された潤滑油が吐出室29に吐出さ
れ、この状態が継続するとタンク5内の潤滑油温
度上昇を招来するのが通常であるが、前記第1の
ポンプ2はレリーフ弁50を介して余剰油をタン
クに還流せしめるとともに、通路48,42を介
してクーラ9に全負荷時と同じ量の油を循環せし
めて流しているので、潤滑油の温度の上昇を招来
せしめることはない。 〔発明の効果〕 以上詳細に説明したように、本発明は、原動機
で駆動されてケーシングの圧縮室内において回転
自在のロータと、該ロータの回転中回転駆動され
るポンプと、該ポンプの吐出口に連結されて前記
圧縮室にポンプの吐出する冷却・潤滑および密封
用の液体を供給する通路と、前記ケーシングから
吐出され不還弁を介して供給されたガスと液体と
を貯溜するタンクと、該タンクの内圧に応じて前
記圧縮室の吸入口の開度を調節する負荷軽減装置
と、該負荷軽減装置による圧縮室の吸入口の開度
調節と同期して液体の流量を調節する流量調整弁
とを設けた回転圧縮機において、前記圧縮室に液
体を供給する通路を前記流量調整弁を介して前記
ポンプの吐出口に連結せしめるとともに、前記ポ
ンプの吸入口と前記タンクの液体排出口とをクー
ラを介して連結せしめ、かつ前記ポンプの排出口
と前記タンクの液体還流口またはタンクの液体排
出口と前記クーラとの間の通路と前記ポンプの排
出口とを、ポンプの吐出口の圧力が所定の値を超
えたとき過剰の圧の液体をタンク側へ還流せしめ
るレリーフ弁により連結せしめたことにより、負
荷軽減装置が圧縮機の圧縮室吸入口を閉塞して無
負荷運転状態としたとき、前記流量調整弁が前記
吸入口の閉塞と同期して液体の流通面積を絞る等
の手段によつて流量を調整し、圧縮機の圧縮室に
供給する液体量を潤滑等に必要な最小限の量と
し、これに伴つて前記ポンプの吐出側の液体圧力
が上昇するときは所定値を超えた過剰圧の液体を
タンクまたはタンクの液体排出口の直後の下流側
に還流せしめることによりポンプの運転による全
負荷時と同じ量の液体の循環を確保するから、無
負荷運転状態においても液体の温度上昇を防止
し、吐出室温度の上昇を防止するとともに、前記
ポンプの異音発生の原因を除去したものである。 上記全負荷時と同じ量の液体の循環の確保は、
負荷軽減装置における吸入口閉塞が何らかの理由
で不完全であつた場合において、前記ポンプが無
負荷運転状態と同様に液体の流量を必要最小限に
設定しながら僅かの吸入空気を圧縮室で圧縮する
不測の事態における液体の温度上昇およびこれに
伴う吐出室温度の上昇を防止する極めて有効なも
のということができる。 なお、本発明の実施例として誘導型の定速回転
型モータを使用したものを示したが、かかるモー
タは通常使用されている型式のモータで廉価であ
つて、負荷軽減装置の作動により全負荷運転状態
および無負荷運転状態の二負荷状態のみのオン・
オフ制度を行う回転圧縮機に実施する場合に適切
なものである。このような回転圧縮機においては
中間負荷状態の場合にはオン・オフ制御を繰返さ
せることになるが、前記負荷軽減装置の閉塞弁
を、前記図示しない圧力調整弁の作用により吸気
通孔を全開する状態と吸気通孔を全閉する状態の
二位置の間の中間位置をとらせ、吸入空気量の調
整を行わしめることにより、全負荷運転状態と無
負荷運転状態の二負荷状態のほかに中間負荷状態
をとらせることができる。 また本発明において前記負荷運転状態に応じて
圧縮機の回転を変更せしめたい場合には、モータ
として可変回転型のモータを使用し、負荷軽減装
置の閉塞弁または前記流量調整弁あるいは前記図
示しない圧力調整弁の作動に伴つて、全負荷運転
時には回転数を最も高く無負荷運転時には回転数
を最も低く制御せしめることもできる。 さらに本発明においては原動機としてモータの
ほかに内燃機関を使用することもできる。内燃機
関を使用する場合には全負荷運転時にはトルクの
最大の回転数に、無負荷運転時にはアイドリング
回転数に、前記負荷軽減装置の閉塞弁または流量
調整弁あるいは圧力調整弁と連動せしめてスロツ
トル制御をするとよい。 以下本発明の効果の一例を示す。出力37KWの
電動機によつて駆動される実吐出量5.6m2/min
の一段式スクリユー型圧縮機であつて、全負荷時
の圧縮機軸入力37KW、循環油量50/min、入
力熱量31300KCal/hr、クーラ入口油温85℃、ク
ーラ出口油温60℃、吐出空気温度85℃の仕様の圧
縮機に第1図に示す本発明の実施例を施した場合
のデータと、第2図に示す比較例のデータとを、
負荷軽減装置が作動してシリンダへの吸気を全閉
し、かつ圧縮機軸入力を20%(7.4KW)に減少
せしめた場合(循環油量25/min)、および負
荷軽減装置の吸気閉塞が不完全で吸気圧縮を生じ
て圧縮機軸入力70%(25.9KW)で運転する場合
とをとりあげて対比すると下表のとおりである。
[Industrial Field of Application] The present invention relates to an improvement in a rotary compressor in which liquid is discharged into a compression chamber of the rotary compressor to perform cooling, lubrication, and sealing functions. [Prior Art] Generally, as shown in FIG. 2, this type of compressor includes a pump 2 that is constantly driven to rotate while the rotors 12 and 22 of the compressor are rotating, and the pump 2 pumps liquid into the compression chamber 17. , 27 and discharged together with the gas from the compressor is stored together with the gas in a tank 5, and the liquid separated from the gas in the tank is supplied to the pump. On the other hand, when the demand for compressed gas decreases, the compressor activates a load reduction device to reduce or block the intake area of the compressor cylinder using a blockage valve when the pressure in the tank exceeds a predetermined value. By reducing or eliminating the suction gas of the compressor and simultaneously reducing the rotation of the prime mover as necessary, low-load or no-load operation is performed, and power consumption is reduced. By the way, during the above low load or no load operation,
Due to the operation of the blocking valve, very little gas is drawn into the compression chamber of the compressor, whereas cooling, lubricating or sealing liquid is discharged into the compression chamber in proportion to the rotational speed of the compressor rotor. Therefore, a flow rate adjustment valve is provided that reduces the amount of liquid sent from the tank to the pump in synchronization with the decrease in the intake opening of the compressor due to the blockage valve, and a The invention of Japanese Utility Model Publication No. 55-22227 and Japanese Unexamined Patent Application Publication No. 1983-1987 discloses a system in which a second pump is provided and the gas stored at the discharge port of the compressor casing and the liquid separated from the gas are returned to the tank by the pump. This is proposed in the invention of No. 45315. FIG. 2 shows an air compressor implementing the invention of JP-A No. 51-45315, in which a first-stage compressor 11, a second-stage compressor 21, a first pump 2 and a second The pump 3 is arranged in series with a motor 1 whose rotation speed is constant, and the motor 1 drives the compressors 11 and 21.
The rotors 12, 22 and the rotors of the pumps 2, 3 are driven to rotate, respectively. compressor 11,
12 are both screw type, rotor 1
Reference numerals 2 and 22 each consist of a male type screw and a female type screw, and these screws are rotated in synchronization in opposite directions to compress the gas in the axial direction, and the air sucked from the filter 6 is The air is sucked into the suction port 14 of the first stage compressor 11 through the through hole 33 of the load reduction device 31, and the compressor 11
It is compressed by the compressor 17 and enters the suction port 24 of the second stage compressor 21 from the discharge port 15, and is compressed by the compressor 21.
It is compressed in the compression chamber 27 and stored in the tank 5 through the discharge port 25 and the non-return valve 4. Oil for lubricating, sealing, and cooling the compressors 11 and 21 is supplied from the discharge port of the first pump 2 through the passage 51 to the through hole 16 formed in the casing 13 of the first compressor 11 and to the second stage compressor. 21 casing 2
The air is injected into the compression chambers 17 and 27 of the compressors 11 and 21 through the through holes 26 formed in the second stage compressor 21, and is discharged together with the compressed air through the discharge port 25 of the second stage compressor 21 and into the tank 5. sent. A separator (not shown) that separates air and oil is built into the tank 5, and the oil accumulated at the bottom of the tank 5 passes through the oil outlet 44, the passage 52, the cooler 9, the passage 53, and the filter 7. , through the flow rate adjustment valve 8, the passage 54
The water is returned to the suction port of the first pump 2 and circulated. The second pump 3 sucks the oil separated at the discharge port 25 of the second stage compressor 21 from the drain 28 through a passage 55 to the suction port of the pump 3, and from the discharge port passes through a passage 56 to the oil return port 4.
The water is refluxed into the tank 5 from 7. As disclosed in Japanese Unexamined Patent Publication No. 51-45315, the load reduction device is a pressure regulating valve that is guided from the tank 5 when the air pressure in the tank 5 rises and reaches a predetermined regulating pressure point. Due to the balance between the air pressure introduced into the pressure chamber 38 via the pressure reducing valve (not shown) and the air pressure introduced from the tank 5 into the pressure chamber 37 via the pressure reducing valve (not shown), the piston 36
is moved to operate the blockage valve 34 to open the through hole 3.
3 to make the intake air amount of the first stage compressor 11 zero, the air pressure from the pressure regulating valve is simultaneously distributed to the flow regulating valve 8, and the valve body built in the valve 8 is moved by the air pressure, and the passage 53
and 54 is configured to narrow the area of the internal passage within the flow rate regulating valve 8. [Problems to be Solved by the Invention] In the rotary compressor configured as described above, the blockage valve 34 is closed while compressed air is being consumed from the compressed air outlet 60 of the tank 5. 33
is fully opened, the compressors 11 and 21 are in a full-load operating state in which they compress air and discharge compressed air into the tank 5, and the oil is supplied to the compressors 11 and 2 by the first pump 2.
However, when the consumption of the compressed air taken out from the compressed air outlet 60 decreases or stops, the air pressure in the tank 5 rises, and when it reaches a predetermined value, the air pressure increases as shown in the figure. Load reduction device 31 by air pressure from a pressure regulating valve that does not
In this case, the blockage valve 34 completely closes the through hole 33 to make the intake air zero, and the pump 3 discharges and removes the air and oil in the discharge port 29 (the space from the discharge port 25 to the non-return valve 4). The return valve 4 is closed, the pressure in the discharge chamber is significantly reduced, rotor back pressure is removed, and no-load operation is started. At this time, the first stage compressor 11
The amount of air taken into the compressor 1 and the amount of air discharged into the discharge chamber become zero, but due to the action of the flow rate adjustment valve 8,
The supply of a minimum amount of oil for lubrication of parts 1 and 21 is ensured. However, the first pump 2
Since the flow rate regulating valve 8 throttles the oil flow rate on the suction side of the flow rate regulating valve 8, the passage 54 becomes in a vacuum state and an abnormal noise called vacuum sound is generated from the pump 2. At the same time, the cooler 9 on the upstream side of the flow rate regulating valve 8 Since the amount of oil flowing through the cooler is also drastically reduced, the heat transmission coefficient of the cooler is reduced. In the compressor configured as described above, in the unlikely event that the blocking valve 34 of the load reduction device 31 does not completely block the through hole 33, the flow rate of air is reduced between the blocking valve 34 and the through hole 33. When a state of incomplete closure occurs in which a small gap remains, a small amount of air is drawn into the compression chambers 17, 27 from the gap and is compressed to generate compression heat. However, because only the minimum amount of liquid is supplied to the compression chambers 17 and 27 due to the action of the flow rate adjustment valve 8, the liquid for cooling, lubrication, and sealing is superheated and flows into the discharge chamber 29 together with the compressed air. If the state in which the air intake of the load reduction device 31 is incompletely blocked continues such that the liquid is discharged and recirculated into the tank 5, the temperature of the liquid in the tank 5 increases. Furthermore, in a compressor that does not include the second pump 3, if the load reduction device 31 is incompletely blocked, the superheated liquid will remain in the discharge chamber 29 together with the compressed air, causing the non-return valve 4 to close. Since only the amount exceeding the applied pressure is refluxed into the tank 5, there is a risk that the compressor casing 23 may also be overheated. The same applies if the second pump 3 should experience incomplete suction. When the compressed air and liquid remain in the discharge chamber 29, the pressure in the discharge chamber acts as back pressure on the rotor of the compressor, and even when the load reduction device 31 is in operation, the power consumption decreases by only about 70%. . [Means for solving the problem] In a rotary compressor that is operated by injecting cooling, lubricating, and sealing liquid into the compression chamber, when a load reduction device is installed and the no-load operation is performed, the above-mentioned It is advantageous in terms of power consumption to reduce the amount of liquid supplied to the compression chamber in synchronization with the operation of the load reducing device at the same time as the load reducing device blocks and interrupts the intake gas. For this purpose, a flow rate regulating valve that operates in synchronization with the operation of the load reduction device is usually disposed in the liquid passage of the pump that supplies liquid to the compression chamber, but on the suction side of the pump. In a simple oil passage configuration, in which the oil passage is connected to the liquid discharge port of the tank via the cooler, and the discharge side of the pump is connected by an oil passage to a through hole that communicates with the compression chamber of the compressor casing, the flow rate is Even if the regulating valve is disposed in the oil passage on the suction side of the pump, or even if it is disposed in the oil passage on the discharge side of the pump, when the flow rate regulating valve throttles the liquid flow rate, the pump is stopped. The problem is not solved because the liquid flow rate through the cooler is reduced and therefore the liquid flow rate through the cooler is reduced. The present invention includes a casing of a compressor, a compressor rotor that is driven by a prime mover and is rotatable within a compression chamber of the casing, a pump that is rotationally driven during rotation of the rotor, and a pump that is connected to a discharge port of the pump and that is rotatable within a compression chamber of the casing. a passage for supplying liquid for cooling, lubricating and sealing the compressor discharged by the pump into the compression chamber;
a tank for storing the gas and liquid discharged from the casing and supplied via the non-return valve; a load reduction device for adjusting the opening degree of the absorption port of the compression chamber according to the internal pressure of the tank; and the load. In a rotary compressor provided with a flow rate adjustment valve that adjusts the flow rate of liquid supplied to the compression chamber in synchronization with the adjustment of the opening of the suction port of the compression chamber by a reducing device, a passage for supplying liquid to the compression chamber is provided. It is connected to the discharge port of the pump via the flow rate adjustment valve, and the suction port of the pump and the liquid discharge port of the tank are connected via a cooler, and the liquid return port of the tank and the liquid discharge port of the tank are connected to each other via a cooler. Either one of the passages between the outlet and the cooler and the discharge port of the pump are connected so that when the pressure at the discharge port of the pump exceeds a predetermined value, excess pressure liquid is returned to the tank side. The invention is characterized in that the fluid is connected via a relief valve that prevents the liquid from being discharged from the pump even when the flow rate adjustment valve throttles the flow rate to the passage that supplies liquid to the compression chamber in synchronization with the operation of the load reduction device. The surplus liquid flowing through the pump is made to flow to the tank side via a relief valve, and the flow rate of the liquid flowing through the pump and therefore the flow rate of the liquid flowing through the cooler is increased regardless of the operating state of the load reduction device, This is an attempt to solve the above problems. [Operation of the Invention] According to the present invention, while the rotor of the rotary compressor is rotating, the pump is driven, and liquid is sucked from the liquid discharge port of the tank through the cooler and from the suction port. The discharge side of the pump communicates with at least one of a passage supplying liquid to the compression chamber and a passage between a liquid return port of the tank and a pre-discharge port of the tank and the cooler via a relief valve. Therefore, when a large amount of liquid is supplied to the compression chamber for cooling, lubrication, and sealing, such as when a rotary compressor is operating at full load, the liquid discharged from the pump is transferred to the tank via the relief valve. When the load reduction device is activated and the flow rate adjustment valve limits the amount of liquid supplied to the compression chamber, the surplus liquid discharged from the pump is The flow rate of the liquid flowing through the pump is kept unchanged regardless of the operating status of the rotary compressor, and the flow rate of the liquid flowing through the cooler is made independent of whether the load reduction device is in operation or incompletely operated. and cool it down. [Description of Embodiment] Fig. 1 shows an embodiment of the present invention in which the present invention is applied to a rotary compressor of the same type as Fig. 2, and the same parts as in Fig. 2 are given the same reference numerals. This is what was shown. The rotary compressor has a motor 1, a first stage compressor 11, a second stage compressor 21, a first pump 2, and a second pump 3 arranged in series, and the motor 1 drives the compressors 11, 12 and the pump 2. , 3. 1st stage compressor 11 and 2nd stage compressor 11
The stage compressor 21 is of a screw type, and has a pair of male rotor and female rotor (hereinafter simply referred to as rotor 1).
2 and 22) are in mesh with each other, compressing the air taken in from the suction port 14 of the casing 13 of the first stage compressor 11 and discharging the compressed air from the discharge port 25 of the second stage compressor 21 through the non-return valve 4. It is configured such that the water is stored in the tank 5 through the. 1st stage compressor 11
The casing 13 is provided with a filter 6 and a load reduction device 31 connected to the suction port 14,
The air is passed through the filter 6 and the machine frame 32 of the load reduction device 31.
The air is sucked into the suction port 14 of the compressor casing 13 through the through hole 33 . The load reduction device 31 includes a blockage valve 34 mounted on the machine frame 32 so as to be able to reciprocate in the axial direction, and a piston 36 fixed to a shaft 35 of the blockage valve 34.
It is equipped with pressure chambers 37 and 38 that are divided into individual parts,
When the pressure in the tank 5 rises and reaches a predetermined adjustment pressure point, air pressure is introduced into the pressure chamber 38 through a gas pipe led from the tank 5 and a pressure adjustment valve (both not shown). With the balance of the reduced air pressure branched from the gas pipe and introduced into the pressure chamber 37 via a pressure reducing valve (not shown),
The piston 36 is actuated to close the closure valve 34.
This allows the opening area of the through hole 33 to be fully opened or the through hole 33 to be completely closed. Motor 1
is an induction type with a constant rotation speed, and is in a loaded operation state while the closing valve 34 fully opens the through hole 33 and performs the compression action of the compressor; In this case, the pressure in the discharge chamber 29 of the compressor (the space from the discharge port 25 to the non-return valve 4) is significantly reduced by removing air and oil from the drain 28 using the second pump 3. By removing the back pressure acting on the rotor, the power consumption is reduced to 20% or less of full load, resulting in no-load operation. Lubricating oil as a liquid for cooling, lubrication, and sealing is sent from the discharge port of the first pump 2 through the passage 40 to the passage 41 via the filter 7 and the flow rate adjustment valve 8, and then through the passage hole 16 of the casing 13. first through
to the compression chamber 17 of the stage compressor 11, and to the casing 2
It is discharged into the compression chamber 27 of the second stage compressor 21 through the through hole 26 of No. 3. The oil discharged into the compression chambers 17, 27 of the compressors 11, 21 is transferred to the rotors 12, 2.
The sliding surface of the second stage compressor 21 is lubricated and sealed, and the discharge chamber 2 of the second stage compressor 21 is cooled together with the compressed air.
5 and enters the tank 5 together with compressed air via the non-return valve 4. A separator (not shown) for separating air and oil is built in the tank 5, and the oil is stored in the lower part of the tank 5. The suction port of the first pump 2 is communicated with the oil outlet 44 of the tank 5 via a passage 42, a cooler 9 and a passage 43, and the oil separated from air in the tank 5 is cooled by the cooler 9. The pressure is increased by the first pump 2 to lubricate the compressors 11 and 12, and the fluid is circulated back to the tank 5. On the other hand, the second pump 3 has its suction port connected to the discharge chamber 2 of the second stage compressor 21 via the passage 45.
It communicates with a drain 28 provided in the oil reservoir section 9, sucks oil discharged from the discharge port 25 and separated from air in the discharge chamber 29, and drains the oil from the tank 5 through a passage 46 from the discharge port. To the oil return port 47 or to the passage 49 and passage 4 shown in dotted lines.
The oil is returned to the oil passage 43 that connects the oil outlet 44 and the cooler 9 via the oil outlet 8 . The flow rate adjustment valve 8 is the same known type as shown in FIG. 2, and the pressure gas is introduced through the pressure adjustment valve.
When the built-in valve body moves due to the pressure of the pressurized gas, the internal passage area of the regulating valve 8 that communicates from the passage 40 to the passage 41 is narrowed.When the air pressure in the tank 5 reaches a predetermined regulation pressure point, The flow rate is adjusted so that the internal passage of the regulating valve 8 is narrowed in two stages or steplessly in synchronization with the closing of the suction hole 33 in the load reducing device 31. The control method for the flow rate regulating valve is not limited to the one shown in the drawings, but the method described in Japanese Utility Model Publication No. 55-22227, which is directly controlled by the movement of the closing valve 34, can also be used. Reference numeral 50 indicates a relief valve, which allows excess pressure oil to flow back to the passage 43 through the passage 48 when the oil pressure in the passage 40 connected to the discharge port of the first pump 2 exceeds a predetermined value, or as shown in the dotted line diagram. aisle 49
This is a control valve that allows liquid to flow in only one direction as described above. When configured as described above, oil passes through the passage 43 from the oil discharge port 44 of the tank 5, is cooled by the cooler 9, is sucked into the first pump 2 through the passage 42, and from the discharge port passes through the passage 40, The flow rate is adjusted by the flow rate adjustment valve 8 through the filter 7, and the flow is passed through the passage 41 and the through hole 16 of the casing 13 to the compression chamber 17 of the first stage compressor 11. through the second stage compressor 21
are injected and supplied to the compression chambers 27, respectively. The oil injected into the compression chambers 17 and 27 flows into the second chamber together with the compressed air.
The oil is returned from the discharge port 25 of the stage compressor 21 through the discharge chamber 29 into the tank 5, and is separated from the air in the discharge chamber 29 of the compressor 21.
8, is sucked into the second pump 3 via a passage 45, and is returned to the tank 5 via a passage 46. While the compressed air in the tank 5 is taken out from the outlet 60 and consumed, the rotary compressor is in full-load operation, the blockage valve 34 fully opens the through hole 33, and the flow control valve 8 is operated with a sufficient amount of air. The area of the internal passage is adjusted to be large so as to supply oil to the compressors 11 and 21. By the way, when the consumption amount of air taken out from the compressed air outlet 60 decreases or no air is taken out at all, the air pressure inside the tank 5 increases, and when this reaches a predetermined adjustment pressure point, the pressure is increased by the action of a pressure adjustment valve (not shown). The pressure in the chamber 38 rises above the pressure in the pressure chamber 37, which is inflowed through a pressure reducing valve (not shown), and the blockage valve 34 is moved toward the through hole 33;
The air intake is stopped by closing the through hole 33. In synchronization with the movement of the blockage valve 34, the movable valve body built into the flow rate regulating valve 8 is moved by the action of the pressure regulating valve to throttle the internal passage within the regulating valve 8 and reduce the amount of oil supplied to the passage 41. reduce the load and enter the no-load operation state. In the no-load operating state, the compressor 11 is operated with zero intake air at the suction port 14, and no heat of compression of the gas is generated. However, since the compressors 11 and 21 are operated at constant speed, oil lubricates the rotating parts. The required amount is discharged into the compression chambers 17, 27. At this time, the amount of oil delivered by the flow rate regulating valve 8 is set to be less than half of that during full load operation. This lubricating oil is sucked from the tank 5 by the first pump 2 through the cooler 9 and the passage 42, and is discharged into the passage 40, and is discharged into the flow rate regulating valve 8.
However, when the internal passage of the flow rate adjustment valve 8 is narrowed and the hydraulic pressure in the passage 40 increases, the relief valve 50 is activated, and excess pressure oil above a predetermined pressure is transferred from the passage 48 to the tank 5 or the cooler. 9 is discharged and recirculated to the upstream side. Therefore, even during low-load or no-load operation, the tank 5, cooler 9, and passage 4
2, the same amount of oil as at full load circulates and flows, preventing the oil temperature from rising. Furthermore, even if the pressure on the discharge side of the first pump 2 increases during no-load operation, due to the presence of the relief valve 50, the pressure on the discharge side will not increase above a certain value; rather, as shown in FIG. Unlike the liquid supply circuit, the suction side is not in a vacuum state, so there is no need to worry about abnormal noise, and therefore it is sufficient to select or design according to the amount of oil supplied during full load operation of the compressor. . Even during no-load operation, oil is supplied to the compression chambers 17 and 27 of the compressor via the flow rate adjustment valve 8 and is discharged to the discharge port 25 of the second stage compressor 21. Since the air in the discharge chamber and the oil separated from the air are discharged and removed, the non-return valve 4 is closed, and the oil is sucked into the second pump 3 from the drain 28 through the passage 45, and then through the passage 46 into the tank 5. The oil is refluxed to the oil reflux port 47. That is, the second pump 3 is a load reducing device 31.
Even after the closing valve 34 closes the passage hole 33 and the compressed air is no longer discharged to the discharge port 25, air and oil are discharged and removed from the drain 28, so that the air and oil in the discharge chamber 29 are removed. Since the pressure is significantly reduced, the pressure difference between the compressor suction port 14 and the discharge port 25 is reduced, and the back pressure acting on the rotors 12, 22 is removed, the power consumption of the compressor is 20%.
% or less. However, in the case of a compressor that does not include the second pump 3, the load reduction device 31 operates and the blockage valve 34 closes the through hole 33.
When the valve 34 is closed, the pressure in the discharge chamber 29 is maintained at the pressure at the time of operation of the load reduction device, and the pressure on the suction side of the compressor becomes negative pressure when the closing valve 34 closes the passage hole 33. The machine is operated with a pressure difference (back pressure) greater than the pressure inside the discharge chamber acting on the rotors 12 and 22 of the machine. In such a no-load operating state, if the closing valve 34 is not fully seated and even a small amount of air is sucked into the compression chambers 17, 27 from the through hole 33 of the load reduction device 31, the compressed air and Lubricating oil superheated by the heat of compression of the air is discharged into the discharge chamber 29, and if this state continues, the temperature of the lubricating oil in the tank 5 will normally rise. Excess oil is returned to the tank via the valve 50, and the same amount of oil as at full load is circulated to the cooler 9 via the passages 48 and 42, causing an increase in the temperature of the lubricating oil. Never. [Effects of the Invention] As described in detail above, the present invention provides a rotor that is driven by a prime mover and is rotatable in a compression chamber of a casing, a pump that is rotationally driven while the rotor is rotating, and a discharge port of the pump. a passage connected to the compression chamber for supplying cooling, lubricating and sealing liquid discharged by the pump to the compression chamber; and a tank storing gas and liquid discharged from the casing and supplied via the non-return valve; a load reduction device that adjusts the opening of the suction port of the compression chamber according to the internal pressure of the tank; and a flow rate adjustment that adjusts the flow rate of liquid in synchronization with the adjustment of the opening of the suction port of the compression chamber by the load reduction device. In a rotary compressor provided with a valve, a passage for supplying liquid to the compression chamber is connected to a discharge port of the pump via the flow rate adjustment valve, and an inlet port of the pump and a liquid discharge port of the tank are connected. are connected via a cooler, and the passage between the outlet of the pump and the liquid return port of the tank or the liquid outlet of the tank and the cooler is connected to the outlet of the pump, and the pressure at the outlet of the pump is When the pressure exceeds a predetermined value, the load reduction device closes the compression chamber suction port of the compressor, resulting in no-load operation. , the flow rate adjustment valve adjusts the flow rate by means such as narrowing down the liquid circulation area in synchronization with the closure of the suction port, and reduces the amount of liquid supplied to the compression chamber of the compressor to the minimum amount necessary for lubrication, etc. When the liquid pressure on the discharge side of the pump increases accordingly, the excess pressure liquid that exceeds a predetermined value is returned to the tank or to the downstream side immediately after the liquid outlet of the tank, thereby increasing the pressure of the pump. Since the same amount of liquid is circulated as during full load operation, it prevents the temperature of the liquid from rising even during no-load operation, prevents the temperature of the discharge chamber from rising, and eliminates the cause of abnormal noise in the pump. It has been removed. To ensure circulation of the same amount of liquid as at full load,
If the suction port in the load reduction device is incompletely blocked for some reason, the pump compresses a small amount of intake air in the compression chamber while setting the flow rate of the liquid to the necessary minimum, similar to the no-load operation state. This can be said to be extremely effective in preventing an increase in the temperature of the liquid and an accompanying increase in the temperature of the discharge chamber in an unexpected situation. Although the embodiment of the present invention uses an induction-type constant-speed rotary motor, such a motor is of a commonly used type and is inexpensive. ON/OFF only in two load states: operating state and no-load operating state.
This is suitable for use in rotary compressors that operate in the off system. In such a rotary compressor, on-off control is repeated in the case of an intermediate load state, but the closing valve of the load reduction device is fully opened by the action of the pressure regulating valve (not shown). By adjusting the amount of intake air by adjusting the amount of intake air between the two positions of fully closing the intake vent and fully closing the intake vent, the It is possible to take an intermediate load state. Further, in the present invention, when it is desired to change the rotation of the compressor according to the load operating state, a variable rotation type motor is used as the motor, and the blockage valve of the load reduction device, the flow rate adjustment valve, or the pressure (not shown) is used. In conjunction with the operation of the regulating valve, the rotational speed can be controlled to be the highest during full-load operation, and the rotational speed to be the lowest during no-load operation. Furthermore, in the present invention, an internal combustion engine can be used as the prime mover in addition to a motor. When using an internal combustion engine, the throttle is controlled at the maximum torque rotation speed during full-load operation, and at idling rotation speed during no-load operation, in conjunction with the blockage valve, flow control valve, or pressure control valve of the load reduction device. It is a good idea to do this. An example of the effects of the present invention will be shown below. Actual discharge volume 5.6m 2 /min driven by an electric motor with an output of 37KW
It is a single stage screw type compressor with compressor shaft input of 37KW at full load, circulating oil flow rate of 50/min, input heat amount of 31300KCal/hr, cooler inlet oil temperature 85℃, cooler outlet oil temperature 60℃, and discharge air temperature. The data when the embodiment of the present invention shown in FIG. 1 is applied to a compressor with specifications of 85°C and the data of the comparative example shown in FIG.
When the load reduction device operates and fully closes the intake air to the cylinder and reduces the compressor shaft input to 20% (7.4KW) (circulating oil amount 25/min), and the load reduction device does not block the intake air. The table below compares the case where the compressor is completely compressed and the compressor shaft input is 70% (25.9KW).

【表】 上記表から明確なように、第2図に示す比較例
の場合はクーラ放熱能力も全負荷運転時に比して
低下し、特に負荷軽減装置の吸気閉塞が不完全で
吸気圧縮を生じた場合に油温および吐出空気温度
が著るしく高温となるのに対し、本発明実施例に
おいてはクーラ放電能力は全負荷運転時と変わら
ず、油温、吐出空気温度ともに低く押えることが
できることが判る。 なお前記実施例としてスクリユー型圧縮機につ
いて説明したが、本発明はスクリユー型に限定さ
れるものではなく、ベーン型、ウオーム型など他
の型式の回転圧縮機にも適用でき、負荷軽減装置
も明細書中に説明した方式のもののほか本発明の
目的に反しない限り適宜の方式のものも採用でき
る。
[Table] As is clear from the above table, in the case of the comparative example shown in Figure 2, the cooler heat dissipation capacity also decreases compared to when operating at full load, and in particular, the intake air is compressed due to incomplete air intake blockage of the load reduction device. In contrast, in the embodiment of the present invention, the cooler discharge capacity remains the same as during full load operation, and both the oil temperature and the discharge air temperature can be kept low. I understand. Although a screw type compressor has been described as the above embodiment, the present invention is not limited to the screw type, and can be applied to other types of rotary compressors such as vane type and worm type. In addition to the methods described in this book, any other suitable method may be employed as long as it does not contradict the purpose of the present invention.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例、第2図は対比のた
め示した従来装置の比較例、を示すものである。 なお図中1はモータ、11,21は圧縮機、1
2,22はそのロータ、13,23はそのケーシ
ング、14,24はその吸入口、15,25はそ
の吐出口、16,26はその油通孔、17,27
はその圧縮室、2,3はポンプ、5はタンク、8
は流量調整弁、9はクーラ、31は負荷軽減装
置、33はその通孔、34はその閉塞弁、50は
レリーフ弁を示すものである。
FIG. 1 shows an embodiment of the present invention, and FIG. 2 shows a comparative example of a conventional device for comparison. In the figure, 1 is a motor, 11 and 21 are compressors, 1
2, 22 are its rotors, 13, 23 are its casings, 14, 24 are its suction ports, 15, 25 are its discharge ports, 16, 26 are its oil holes, 17, 27
is its compression chamber, 2 and 3 are pumps, 5 is tank, 8
9 is a flow regulating valve, 9 is a cooler, 31 is a load reduction device, 33 is a through hole thereof, 34 is a closing valve thereof, and 50 is a relief valve.

Claims (1)

【特許請求の範囲】[Claims] 1 圧縮機のケーシングと、原動機により駆動さ
れて前記ケーシングの圧縮室内において回転自在
の圧縮機ロータと、該ロータの回転中回転駆動さ
れるポンプと、該ポンプの吐出口に連結され前記
圧縮室にポンプの吐出する圧縮機の冷却・潤滑お
よび密封用の液体を供給する通路と、前記ケーシ
ングから吐出され不還弁を介して供給されたガス
と液体とを貯溜するタンクと、該タンクの内圧に
応じて前記圧縮室の吸入口の開度を調節する負荷
軽減装置と、該負荷軽減装置による圧縮室の吸入
口の開度調節と同期して前記圧縮室に供給する液
体の流量を調節する流量調整弁とを設けた回転圧
縮機において、前記圧縮室に液体を供給する通路
を前記流量調整弁を介して前記ポンプの吐出口に
連結せしめるとともに、前記ポンプの吸入口と前
記タンクの液体排出口とをクーラを介して連結せ
しめ、かつ前記タンクの液体還流口およびタンク
の液体排出口と前記クーラとの間の通路との何れ
か一方と前記ポンプの吐出口とを、前記ポンプの
吐出口の圧力が予め定めた値を超えたとき過剰の
圧の液体を前記タンク側に還流せしめるレリーフ
弁を介して連結せしめたことを特徴とする回転圧
縮機。
1. A compressor casing, a compressor rotor driven by a prime mover and rotatable within the compression chamber of the casing, a pump that is rotationally driven while the rotor is rotating, and a compressor rotor that is connected to a discharge port of the pump and is connected to the compression chamber. A passage for supplying liquid for cooling, lubricating and sealing the compressor discharged by the pump, a tank for storing the gas and liquid discharged from the casing and supplied via the non-return valve, and an internal pressure of the tank. a load reduction device that adjusts the opening degree of the suction port of the compression chamber according to the load reduction device; and a flow rate that adjusts the flow rate of the liquid supplied to the compression chamber in synchronization with the adjustment of the opening degree of the suction port of the compression chamber by the load reduction device. In a rotary compressor provided with a regulating valve, a passage for supplying liquid to the compression chamber is connected to a discharge port of the pump via the flow rate regulating valve, and an inlet port of the pump and a liquid discharge port of the tank. are connected via a cooler, and either one of the liquid return port of the tank and the passage between the liquid discharge port of the tank and the cooler is connected to the discharge port of the pump. 1. A rotary compressor, characterized in that the rotary compressor is connected via a relief valve that causes excess pressure liquid to flow back to the tank side when the pressure exceeds a predetermined value.
JP28922785A 1985-12-24 1985-12-24 Rotary compressor Granted JPS61167199A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28922785A JPS61167199A (en) 1985-12-24 1985-12-24 Rotary compressor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28922785A JPS61167199A (en) 1985-12-24 1985-12-24 Rotary compressor

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP14218880A Division JPS5765895A (en) 1980-10-11 1980-10-11 Rotating compressor

Publications (2)

Publication Number Publication Date
JPS61167199A JPS61167199A (en) 1986-07-28
JPH036359B2 true JPH036359B2 (en) 1991-01-29

Family

ID=17740430

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28922785A Granted JPS61167199A (en) 1985-12-24 1985-12-24 Rotary compressor

Country Status (1)

Country Link
JP (1) JPS61167199A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4933291U (en) * 1972-06-30 1974-03-23
JPS5145315A (en) * 1974-10-16 1976-04-17 Hokuetsu Kogyo Co EKIREISHIKITADANKAITENATSUSHUKUKINO EKITAISHORINYORU DORYOKUSE TSUGENHOHO

Also Published As

Publication number Publication date
JPS61167199A (en) 1986-07-28

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