JPS5930240Y2 - centrifugal refrigerator - Google Patents

centrifugal refrigerator

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Publication number
JPS5930240Y2
JPS5930240Y2 JP1978175189U JP17518978U JPS5930240Y2 JP S5930240 Y2 JPS5930240 Y2 JP S5930240Y2 JP 1978175189 U JP1978175189 U JP 1978175189U JP 17518978 U JP17518978 U JP 17518978U JP S5930240 Y2 JPS5930240 Y2 JP S5930240Y2
Authority
JP
Japan
Prior art keywords
gas
economizer
inlet
mainstream
centrifugal
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
Application number
JP1978175189U
Other languages
Japanese (ja)
Other versions
JPS5590799U (en
Inventor
泰 古谷
真次 四十宮
Original Assignee
株式会社荏原製作所
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 株式会社荏原製作所 filed Critical 株式会社荏原製作所
Priority to JP1978175189U priority Critical patent/JPS5930240Y2/en
Publication of JPS5590799U publication Critical patent/JPS5590799U/ja
Application granted granted Critical
Publication of JPS5930240Y2 publication Critical patent/JPS5930240Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、遠心式多段圧縮機を用い、エコノマイザサイ
クルを採用した遠心式冷凍機に関するものである。
[Detailed Description of the Invention] The present invention relates to a centrifugal refrigerator that uses a centrifugal multi-stage compressor and employs an economizer cycle.

一般に遠心式多段圧縮機を用いた冷凍機ではエコノマイ
ザサイクルがサイクル上の効率を上げるために用いられ
ることが知られている。
It is generally known that an economizer cycle is used in refrigerators using centrifugal multi-stage compressors to increase cycle efficiency.

即ちエコノマイザサイクルとは、多段圧縮の冷凍サイク
ルに用いられるシステムで1段目羽根車出口以降の流路
にエコノマイザガスを流入せしめることにより圧縮機全
体のサイクル上の効率を上げる為に使用される圧縮シス
テムであるが、従来ではこの中間段のガス導入には後段
の羽根車の直前もしくは戻りガイドベーン出口近傍又は
戻りガイドベーン入口前に導入することが行なわれてい
る。
In other words, an economizer cycle is a system used in a multi-stage compression refrigeration cycle, and is used to increase the cycle efficiency of the entire compressor by allowing economizer gas to flow into the flow path after the first stage impeller outlet. Conventionally, gas is introduced into this intermediate stage by introducing it immediately before the impeller in the latter stage, near the exit of the return guide vane, or before the inlet of the return guide vane.

このうち、エコノマイザなどからのガスを羽根車直前又
は戻りガイドベーン出口近傍に誘導人するものでは合流
点から後流の羽根車人口1での流路が短い。
Among these, in the case where gas from an economizer or the like is guided to just before the impeller or near the exit of the return guide vane, the flow path from the confluence point to the impeller population 1 downstream is short.

一方、エコノマイザガス流量は主流ガスの10〜15饅
にも及ぶので、流路が短いと主流ガスとの混合が不完全
となり、温度、速度などが不均一な状態で羽根車に吸い
込壕れることになり羽根車の効率を低下させる。
On the other hand, the economizer gas flow rate is as much as 10 to 15 times the mainstream gas, so if the flow path is short, mixing with the mainstream gas will be incomplete, and the gas will be sucked into the impeller with uneven temperature and velocity. This reduces the efficiency of the impeller.

一方戻りガイドベーン入口前にエコノマイザガスを導入
するものに関してはその流路の方向を決定し難い。
On the other hand, in the case where the economizer gas is introduced before the return guide vane inlet, it is difficult to determine the direction of the flow path.

すなわちガイドベーンより上流の主流ガスの方向は、回
転軸を含む平面に対して角度(以下流れ角度と称す)を
有し、スクリュー状の流れとなっているが、この流れ角
度は圧縮機の運転状態によって変化するため、エコノマ
イザガス流路の方向を固定した場合にはエコノマイザガ
スが常に主流に円滑に合流するとは限らない。
In other words, the direction of the mainstream gas upstream from the guide vane has an angle (hereinafter referred to as the flow angle) with respect to the plane containing the rotation axis, resulting in a screw-like flow, but this flow angle depends on the operation of the compressor. Since it changes depending on the state, if the direction of the economizer gas flow path is fixed, the economizer gas does not always smoothly merge into the mainstream.

一般に圧縮機は設計点に於いて運転する頻度が少ないか
ら、例えば設計点での主流ガスの方向に合わせてエコノ
マイザガスの流れの方向を決めると、設計点以外での運
転の場合には、主流方向が変ってし1うため主流方向と
合わずに合流は円滑に行なわれず、混合損失が大きくな
ることで圧縮効率を低下させるばかりでなく騒音発生の
原因ともなつて問題があった。
In general, compressors are operated infrequently at the design point, so for example, if the direction of the economizer gas flow is determined according to the direction of the mainstream gas at the design point, if the compressor is operated at a point other than the design point, Since the direction changes, it does not match the main flow direction, and the merging cannot be performed smoothly, which increases mixing loss, which not only reduces compression efficiency but also causes problems.

考案者らは、従来のものの欠点を改良するために研究を
重ね、従来のものの欠点が上述の如き原因によることを
確かめ、効率低下を改善するためには、二つのガスの合
流にあたり、 (i) 合流時に主流の方向とエコノマイザガスの方
向とを合わせること。
The inventors conducted repeated research to improve the shortcomings of the conventional system, and confirmed that the shortcomings of the conventional system were due to the causes mentioned above.In order to improve the efficiency drop, when the two gases merged, (i ) When merging, align the direction of the mainstream with the direction of economizer gas.

(11)合流直後は、オだよく混合しないので、次段羽
根車人口1で十分距離をとること。
(11) Immediately after merging, the mixture will not be very good, so the next stage impeller population should be 1 to keep a sufficient distance.

に想到し、またさらに好曾しくは (iii) 合流の直前で両者の速度を同じにするこ
と。
Ideally, (iii) both vehicles should have the same speed just before merging.

にも想到し本考案をなすに至ったのである。I came up with this idea and came up with this idea.

本考案は、前述の従来の欠点を適確に除去しようとする
もので、戻りガイドベーンの裏側であって、かつ戻りガ
イドベーン入口の直後の位置に、主流ガスの流れ方向に
添うようにエコノマイザガス流入口を設けることにより
、主流ガスの方向が運転状態に関係なくほぼ一定となる
領域で、しかも、次の段の羽根車入口から十分な距離が
とれる位置でエコノマイザガスの混入が行なわれ、運転
状態の変化に拘らず、混合損失も小さく速度の均一化が
容易、円滑に行なわれ、圧縮機の効率を向上しうる遠心
式冷凍機を提供することを目的としたものである。
The present invention is an attempt to accurately eliminate the above-mentioned conventional drawbacks, and is to install an economizer on the back side of the return guide vane and immediately after the return guide vane inlet along the flow direction of the mainstream gas. By providing a gas inlet, the economizer gas is mixed in an area where the direction of the mainstream gas is almost constant regardless of the operating state, and at a location that is a sufficient distance from the impeller inlet of the next stage. It is an object of the present invention to provide a centrifugal refrigerator which has a small mixing loss, can easily and smoothly equalize the speed, and can improve the efficiency of the compressor regardless of changes in operating conditions.

本考案は遠心式多段圧縮機、凝縮器、蒸発器、エコノマ
イザを備えて、冷凍システムを形成し、前記エコノマイ
ザから導いたエコノマイザガスを前記多段圧縮機の第1
段目羽根車出口より以降の主流ガス流路の流路壁に設け
たエコノマイザガス流入口を経て主流ガスに混入せしめ
るようにした遠心式冷凍機において、前記流入口が、戻
りガイドベーンの裏側の近傍であって、かつ戻りガイド
ベーン入口の直後の位置に、主流ガスの流れ方向に添う
よう所定の方向に指向されて設けられていることを特徴
とする遠心式冷凍機である。
The present invention comprises a centrifugal multi-stage compressor, a condenser, an evaporator, and an economizer to form a refrigeration system, and the economizer gas led from the economizer is transferred to the first stage of the multi-stage compressor.
In a centrifugal refrigerator in which the economizer gas is mixed into the mainstream gas through an economizer gas inlet provided on the wall of the mainstream gas flow path after the outlet of the stage impeller, the inlet is located on the back side of the return guide vane. This centrifugal refrigerator is characterized in that the centrifugal refrigerator is provided in the vicinity and immediately after the return guide vane inlet, oriented in a predetermined direction along the flow direction of mainstream gas.

本考案の実施例を第1図及至第4図に示された2段圧縮
の遠心式冷凍機について説明する。
An embodiment of the present invention will be described with reference to a two-stage compression centrifugal refrigerator shown in FIGS. 1 to 4.

この遠心式圧縮機においては、2段圧縮を行なうため、
回転軸1に設けた前段羽根車2と後段羽根車5とが圧縮
機本体3内に備えられ、中胴3.3□により、前段羽根
車2の出口からの流れを後段羽根車50入口に吸込1せ
るガス流路8が前段羽根車2と後段羽根車5との間に形
成され、このガス流路8の中間に戻りガイドベー77が
設けられている。
This centrifugal compressor performs two-stage compression, so
A front stage impeller 2 and a rear stage impeller 5 provided on the rotating shaft 1 are provided in the compressor main body 3, and the flow from the outlet of the front stage impeller 2 is transferred to the rear stage impeller 50 inlet by the middle body 3.3□. A gas passage 8 for suction 1 is formed between the front stage impeller 2 and the rear stage impeller 5, and a return guide bay 77 is provided in the middle of this gas passage 8.

この遠心式圧縮機と凝縮器12、エコノマイザ11、蒸
発器13とにより、冷凍サイクルが形成されている。
This centrifugal compressor, condenser 12, economizer 11, and evaporator 13 form a refrigeration cycle.

この遠心式圧縮機の中間段には、エコノマイザ11又は
中高温蒸発器(図示せず)からのガスを導入させるよう
にガス流入口9が設けられ、このガス流入口9はエコノ
マイザ流路10によりエコノマイザ11に連絡されてい
る。
A gas inlet 9 is provided at an intermediate stage of the centrifugal compressor to introduce gas from an economizer 11 or a medium-high temperature evaporator (not shown). Economizer 11 has been contacted.

しかしてこのガス流入口9は、戻りガイドベーン7の裏
側(凸面)であって、戻りガイドベーン入口直後の位置
に主流ガスの流れ方向に添うように所定の方向に指向さ
れて設けられている。
However, the lever gas inlet 9 is provided on the back side (convex surface) of the return guide vane 7 at a position immediately after the return guide vane inlet and is oriented in a predetermined direction along the flow direction of the mainstream gas. .

なお、エコノマイザガスを前記ガス流入口9に滑らかに
導くために第1図に二点鎖線で示した如く、一部又は全
部を円錐面33で形成した壁面を加えて流れの整流効果
を改善することも可能である。
In addition, in order to smoothly guide the economizer gas to the gas inlet 9, as shown by the two-dot chain line in FIG. 1, a wall surface partially or entirely formed of a conical surface 33 is added to improve the flow rectification effect. It is also possible.

前記ガス流入口9は戻りガイドベーン7の入ロア□ よ
り少なくとも下流側で且つガイドベーン人ロア□に近寄
った直後の位置でガイドベーン根元端縁T2をガス流入
口端縁とし、主流に向うエコノマイザガスを円滑に主流
に合流混合させるようにしである。
The gas inlet 9 is at least downstream of the input lower □ of the return guide vane 7 and immediately after approaching the guide vane lower □, with the guide vane root edge T2 as the gas inlet edge, and the economizer facing the mainstream. This is to allow the gas to smoothly merge into the main stream and mix.

即ち前段羽根車2よりの旋回エネルギを回収すべく戻り
ガイドベーン7内に導入された主流ガスの流れは、戻り
ガイドベー77の入口で整流され、この入口以降におい
ては、主流ガスの流れの方向は、圧縮機の運転状態の変
化に拘らずほぼ一定となるので、この主流ガスの方向に
合わせてエコノマイザガス流入口9の方向を所定の角度
に決めれば、圧縮機の運転状態の変化に拘らず円滑な合
流を行なうことができる。
That is, the flow of the mainstream gas introduced into the return guide vane 7 to recover the swirling energy from the front stage impeller 2 is rectified at the inlet of the return guide vane 77, and after this inlet, the direction of the flow of the mainstream gas is , remains almost constant regardless of changes in the operating state of the compressor, so if the direction of the economizer gas inlet 9 is set at a predetermined angle in accordance with the direction of this mainstream gas, regardless of changes in the operating state of the compressor. Smooth merging can be achieved.

その上後段羽根車5の入口1では十分距離をとることが
できるので、量的にも温度も速度も異なる二つの流れを
十分混合して得られた均一なガスが吸い込昔れ、吸込条
件が良好となり、効率の向上がはかれる。
Moreover, since the inlet 1 of the rear impeller 5 can be sufficiently far away, a uniform gas obtained by sufficiently mixing two flows with different quantities, temperatures, and speeds can be sucked in and the suction conditions is improved, and efficiency is improved.

特にエコノマイザガスを円滑に主流に合流させるが為エ
コノマイザガス通路の方向を第1図の如く半径方向に傾
げるだけでなく第3図の如く周方向にも傾げである。
In particular, in order to smoothly merge the economizer gas into the main stream, the direction of the economizer gas passage is not only inclined in the radial direction as shown in FIG. 1, but also in the circumferential direction as shown in FIG.

オたエコノマイザ通路出口を第2図の如く戻りガイドベ
ーフフ裏側(凸面)近傍に位置させれば、合流が主流ガ
スの流路の中心付近で行なわれ、速度の均一化がなお一
層円滑に行なわれる。
If the exit of the economizer passage is located near the back side (convex surface) of the return guide valve as shown in FIG. 2, the merging will occur near the center of the mainstream gas flow path, and the velocity will be evened out even more smoothly.

なお前記エコノマイザ流路10は圧縮機本体3内の空室
部を活用し配管10、でエコノマイザ11に連絡しであ
るが、ガス流入口9を配管10、に直接連結する形態と
することもできる。
Although the economizer flow path 10 is connected to the economizer 11 through a pipe 10 by utilizing a vacant space in the compressor main body 3, it is also possible to connect the gas inlet 9 directly to the pipe 10. .

また、エコノマイザガスは圧力差のみにより流れるので
、エコノマイザガス流入口9よりも前のエコノマイザガ
ス速度は、主流ガス速度に比べればかなり小さい。
Furthermore, since the economizer gas flows only due to the pressure difference, the economizer gas velocity before the economizer gas inlet 9 is considerably smaller than the mainstream gas velocity.

従ってガス流入口9の開口面積を次第に絞って高速にし
て、開口面積で速度を主流ガス速度に合わせるようにし
、エコノマイザガスが常に円滑に合流し混合損失ができ
る限り小さくなるように考慮しである。
Therefore, the opening area of the gas inlet 9 is gradually narrowed down to increase the speed, and the opening area is used to match the velocity with the mainstream gas velocity, so that the economizer gas always joins smoothly and the mixing loss is minimized. .

図中4はスリンガ、6はライナーリング、14は駆動機
、15,16は膨張弁、17,18,1920はサイク
ル系配管、21は可変ベーンである。
In the figure, 4 is a slinger, 6 is a liner ring, 14 is a driver, 15, 16 are expansion valves, 17, 18, 1920 are cycle system piping, and 21 is a variable vane.

本考案により、次の如き特別顕著な効果を奏する遠心式
冷凍機を提供することができる。
According to the present invention, it is possible to provide a centrifugal refrigerator that has the following particularly remarkable effects.

(1)圧縮機の運転状態の変化に拘らず、常にエコノマ
イザガスの流入方向を主流ガスの方向にほぼ合わせるこ
とができ、合流が円滑に行なわれ、渦などの発生がなく
、混合損失が少ない。
(1) Regardless of changes in compressor operating conditions, the inflow direction of the economizer gas can always be aligned with the direction of the mainstream gas, allowing for smooth merging, no generation of vortices, and low mixing loss. .

(2)合流が、主流ガスの流路のほぼ中心付近で行なわ
れるので速度の均一化が円滑に、短時間で行かわれるへ (3)合流点から次段の羽根車人口1での距離が十分と
れるので、性状の異なる二つの流れの混合が良好に行な
われ、均一なガスとなり、次段の羽根車での吸込条件が
良好になる。
(2) Since the merging takes place almost near the center of the mainstream gas flow path, the velocity can be equalized smoothly and in a short time. (3) The distance from the merging point to the next stage impeller population 1 is Since sufficient amount of gas can be obtained, the two flows having different properties are mixed well, resulting in a uniform gas, and the suction conditions for the impeller of the next stage are favorable.

(4)以上の結果圧縮機の効率を向上せしめることがで
きる。
(4) As a result of the above, the efficiency of the compressor can be improved.

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

図面は本考案の実施例を示し、第1図は縦断面図、第2
図は第1図A−A線における切断面図、第3図は第1図
B−B線における切断面図、第4図は使用状態の系統説
明図である。 1・・・・・・回転軸、2・・・・・・前段羽根車、3
・・・・・・圧縮機本体、3□ 、32・・・・・・中
胴、33・・・・・・円錐面、4・・・・・・スリンガ
、5・・・・・・後段羽根車、6・・・・・・ライナー
リング、7・・・・・・戻りガイドベーン、7、・・・
・・・ガイドベーン入口、72・・・・・・ガイドベー
ン根元端縁、8・・・・・・ガス流路、9・・・・・・
ガス流入口、10・・・・・・エコノマイザ流路、10
□・・・・・・配管、11・・・・・・エコノマイザ、
12・・・・・・凝縮器、13・・・・・・蒸発器、1
4・・・・・・駆動機、15,16・・・・・・膨張弁
、17゜18.19,20・・・・・・サイクル系配管
、21・・・・・・可変ベーン。
The drawings show an embodiment of the present invention, with FIG. 1 being a longitudinal sectional view and FIG.
The figures are a sectional view taken along the line AA in FIG. 1, FIG. 3 is a sectional view taken along the line BB in FIG. 1, and FIG. 4 is an explanatory diagram of the system in use. 1...Rotating shaft, 2...Pre-stage impeller, 3
...Compressor main body, 3□, 32...Middle body, 33...Conical surface, 4...Slinger, 5...Late stage Impeller, 6... Liner ring, 7... Return guide vane, 7...
... Guide vane inlet, 72 ... Guide vane root edge, 8 ... Gas flow path, 9 ...
Gas inlet, 10...Economizer flow path, 10
□・・・Piping, 11・・・Economizer,
12... Condenser, 13... Evaporator, 1
4... Drive machine, 15, 16... Expansion valve, 17° 18. 19, 20... Cycle system piping, 21... Variable vane.

Claims (1)

【実用新案登録請求の範囲】 1 遠心式多段圧縮機、凝縮器、蒸発器、エコノマイザ
を備えて、冷凍システムを形成し、前記エコノマイザか
ら導いたエコノマイザガスを、前記多段圧縮機の第1段
目羽根車出口より以降の主流ガス流路の流路壁に設けた
エコノマイザガス流入口を経て主流ガスに混入せしめる
ようにした遠心式冷凍機において、前記流入口が、戻り
ガイドベーンの裏側の近傍であって、かつ戻りガイドベ
ーン入口の直後の位置に、主流ガスの流れ方向に添うよ
う所定の方向に指向されて設けられていることを特徴と
する遠心式冷凍機。 2 前記ガス流入口が、圧縮機の主流ガス速度に合わせ
た開口面積をもっているものである実用新案登録請求の
範囲第1項記載の遠心式冷凍機。
[Claims for Utility Model Registration] 1. A refrigeration system is formed by comprising a centrifugal multi-stage compressor, a condenser, an evaporator, and an economizer, and the economizer gas led from the economizer is transferred to the first stage of the multi-stage compressor. In a centrifugal refrigerator in which the economizer gas is mixed into the mainstream gas through an economizer gas inlet provided on the flow path wall of the mainstream gas flow path after the impeller outlet, the inlet is located near the back side of the return guide vane. What is claimed is: 1. A centrifugal refrigerating machine, characterized in that the refrigerating machine is provided at a position immediately after the return guide vane inlet and oriented in a predetermined direction along the flow direction of mainstream gas. 2. The centrifugal refrigerator according to claim 1, wherein the gas inlet has an opening area that matches the mainstream gas velocity of the compressor.
JP1978175189U 1978-12-18 1978-12-18 centrifugal refrigerator Expired JPS5930240Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1978175189U JPS5930240Y2 (en) 1978-12-18 1978-12-18 centrifugal refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1978175189U JPS5930240Y2 (en) 1978-12-18 1978-12-18 centrifugal refrigerator

Publications (2)

Publication Number Publication Date
JPS5590799U JPS5590799U (en) 1980-06-23
JPS5930240Y2 true JPS5930240Y2 (en) 1984-08-29

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP1978175189U Expired JPS5930240Y2 (en) 1978-12-18 1978-12-18 centrifugal refrigerator

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Country Link
JP (1) JPS5930240Y2 (en)

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JP7085306B2 (en) * 2017-02-20 2022-06-16 三菱重工コンプレッサ株式会社 Centrifugal compressor
JP7125639B1 (en) * 2021-03-30 2022-08-25 ダイキン工業株式会社 compressor

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