JPH01285692A - Control method for screw compressor driven by expansion machine - Google Patents
Control method for screw compressor driven by expansion machineInfo
- Publication number
- JPH01285692A JPH01285692A JP11777288A JP11777288A JPH01285692A JP H01285692 A JPH01285692 A JP H01285692A JP 11777288 A JP11777288 A JP 11777288A JP 11777288 A JP11777288 A JP 11777288A JP H01285692 A JPH01285692 A JP H01285692A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- expander
- exhaust
- flow path
- air supply
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims description 22
- 238000001514 detection method Methods 0.000 claims description 15
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
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- Applications Or Details Of Rotary Compressors (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、容積形の膨張機を用いた膨張機駆動スクリュ
圧縮機の制御方法に関するしのである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method of controlling an expander-driven screw compressor using a positive displacement expander.
(従来の技術)
従来、第4図に示すように、例えば省エネルギの見地か
ら、本来成る用途のために消費地に送給される蒸気を利
用した膨張機駆動スクリュ圧縮機が公知である。(Prior Art) Conventionally, as shown in FIG. 4, an expander-driven screw compressor is known, for example from the standpoint of energy saving, which utilizes steam delivered to a consumption area for its original purpose.
この圧縮機は、駆動源として容積形のスクリュ膨張機I
を用いており、スクリュ膨張機lの吸込側には給気加減
弁2.しゃ断弁3を有する給気流路4が、排気側には排
気圧力検出用の第1圧力検出画5を取付けた排気流路6
が続いている。また給気加減弁2の上流側から、バイパ
ス弁7を介して直接排気流路6に至るバイパス流路8を
設けて、第1圧力検出器5により給気加減弁2.バイパ
ス弁7の開度を制御するようにして駆動部を形成しであ
る。さらに、スクリュ膨張機lの出力軸部分には、回転
数リレー9が設けてあり、スクリュ膨張機lの回転数が
許容下限値以下になった場合には、この回転数リレー9
によりこの回転数の低下を検出して上記しゃ断弁3を閉
にするように形成しである。This compressor uses a positive displacement screw expander I as a driving source.
A supply air control valve 2. is used on the suction side of the screw expander l. An air supply flow path 4 having a shutoff valve 3 is connected to an exhaust flow path 6 having a first pressure detection screen 5 for detecting exhaust pressure on the exhaust side.
It is continuing. Further, a bypass flow path 8 is provided from the upstream side of the air supply control valve 2 via a bypass valve 7 to directly reach the exhaust flow path 6, and the first pressure detector 5 detects the air supply control valve 2. A driving section is formed to control the opening degree of the bypass valve 7. Furthermore, a rotation speed relay 9 is provided on the output shaft portion of the screw expander l, and when the rotation speed of the screw expander l falls below the allowable lower limit, this rotation speed relay 9
The cutoff valve 3 is configured to detect this decrease in rotational speed and close the shutoff valve 3.
一方、スクリュ膨張機lには変速機lOを介して回転駆
動可能にスクリュ圧縮機本体11が結合してあり、この
スクリュ圧縮機本体IIの吸込側に吸込フィルタ12を
設けるととらに、吐出側には油分離器+3.逆止弁14
を備えた吐出流路15が続いている。On the other hand, a screw compressor main body 11 is rotatably connected to the screw expander l via a transmission lO, and a suction filter 12 is provided on the suction side of the screw compressor main body II, and a suction filter 12 is provided on the discharge side of the screw compressor main body II. Oil separator +3. Check valve 14
A discharge flow path 15 continues therefrom.
そして、例えば図示しないボイラにより発生した蒸気、
あるいはその他の駆動用流体(以下、単に蒸気という。For example, steam generated by a boiler (not shown),
Or other driving fluid (hereinafter simply referred to as steam).
)を給気流路4より、スクリュ膨張機lに供給し、ここ
で減圧した後、排気流路6より排出している。蒸気の減
圧によってスクリュ膨張機!において発生した動力は、
変速機IOを介してスクリュ圧縮機本体11に伝達され
、このスクリュ圧縮機本体!■により吸込フィルタ12
から吸込んだ空気を圧縮した後、吐出流路15に吐出し
、油分離器I3にて気液分離して圧送するようにしであ
る。) is supplied to the screw expander l through the air supply flow path 4, where it is depressurized and then discharged through the exhaust flow path 6. Screw expansion machine by steam decompression! The power generated in
It is transmitted to the screw compressor main body 11 via the transmission IO, and this screw compressor main body! ■By suction filter 12
After compressing the air sucked in from the compressor, it is discharged into the discharge passage 15, separated into gas and liquid by the oil separator I3, and then pumped.
ところで、上述の蒸気の量は変動する場合が多く、以下
のようにスクリュ膨張機を蒸気量に応じて回転数制御す
るように形成しである。By the way, the above-mentioned amount of steam often fluctuates, and the screw expander is formed so as to control the rotation speed according to the amount of steam as described below.
即ち、蒸気の供給量が変動する場合、スクリュ膨張機l
への給気圧力も変動しようとするので、第1圧力検出器
5により、この検出圧力が一定値以下になるように給気
加減弁2の開度調節を行って、スクリュ膨張機lへの給
気量が許容容量以上になる場合には、バイパス弁7を開
いて、余剰の蒸気を直接排気流路6にバイパスさせてい
る。That is, when the amount of steam supplied fluctuates, the screw expander l
Since the air supply pressure to the screw expander l is also about to fluctuate, the first pressure detector 5 adjusts the opening of the air supply control valve 2 so that the detected pressure is below a certain value. When the amount of supplied air exceeds the allowable capacity, the bypass valve 7 is opened to directly bypass the excess steam to the exhaust flow path 6.
一方、排気流路6側での蒸気使用量が変動する場合にも
、排気流路6の圧力が変動しようとするので、上記同様
第1圧力検出器5により、その検出圧力が一定範囲内に
入るように給気加減弁2の開度調節を行って、さらに給
気加減弁2を全開にしても、なお圧力が低い場合にはバ
イパス弁7を開いて圧力を適正に保つようにして、スク
リュ膨張機Iの回転数制御が行われている。On the other hand, even when the amount of steam used on the exhaust flow path 6 side fluctuates, the pressure in the exhaust flow path 6 tends to fluctuate, so the first pressure detector 5 as described above ensures that the detected pressure is within a certain range. Even if the supply air adjustment valve 2 is fully opened and the pressure is still low, the bypass valve 7 is opened to maintain the pressure at an appropriate level. The rotation speed of the screw expander I is controlled.
(発明が解決しようとする課題)
上記従来の制御方法では、第1圧力検出器5による検出
圧力に基いて制御が行われているので、蒸気量の変動に
対するスクリュ膨張機Iの回転数制御だけが行われるこ
とになり、スクリュ膨張機lにより駆動されるスクリュ
圧縮機本体11は圧縮空気所要量とは無関係に回転数制
御されるという問題がある。(Problem to be Solved by the Invention) In the conventional control method described above, control is performed based on the pressure detected by the first pressure detector 5, so only the rotation speed of the screw expander I is controlled in response to fluctuations in the amount of steam. Therefore, there is a problem that the rotation speed of the screw compressor main body 11 driven by the screw expander 1 is controlled regardless of the required amount of compressed air.
本発明は、斯る従来の問題点を課題としてなされたもの
で、蒸気圧力だけでなく、スクリュ圧縮機本体側の吐出
圧力も検出し、圧縮空気所要量が少ない場合には、蒸気
供給量が充分な場合でも、膨張機の回転数を減少させて
、不必要な空気圧縮による蒸気のエンタルピ低下の損失
を無くすようにした膨張機駆動スクリュ圧縮機の制御方
法を提供しようとするものである。The present invention was developed to address these conventional problems, and detects not only the steam pressure but also the discharge pressure on the screw compressor main body side, and when the required amount of compressed air is small, the steam supply amount is reduced. It is an object of the present invention to provide a control method for an expander-driven screw compressor in which the rotational speed of the expander is reduced even in cases where the rotation speed of the expander is reduced to eliminate the loss of enthalpy reduction of steam due to unnecessary air compression.
(課題を解決するための手段)
上記従来の課題を解決するために、本発明は、膨張機と
、この吸込側に続く給気加減弁、しゃ断弁を有する給気
流路と、上記膨張機の排気側に続く排気流路と、上記給
気加減弁の上流側からバイパス弁を介して、直接上記排
気流路に至るバイパス流路とを備えた駆動部の上記膨張
機によりスクリュ圧縮機本体を駆動させるようにした膨
張機駆動スクリュ圧縮機の制御方法において、上記排気
流路に第1圧力検出手段と、上記圧縮機本体の吐出流路
に第2圧力検出手段と、第1.第2圧力検出手段から信
号を受けて上記給気加減弁の開度を制御する制御手段と
を設けて、吐出ガス圧と膨張機排気圧のうちのいずれか
一方が設定値を超える第1の場合には上記給気加減弁の
開度を小さくし、その他の場合のうち上記排気圧が設定
値に等しい第2の場合には現状の運転状態を維持し、上
記排気圧が設定値より小さい第3の場合には、上記第1
、第2の状態になる迄上記給気加減弁の開度を大きくし
てゆき、上気排気圧が予め定めた設定値より低くなると
上記バイパス弁を開いて上記排気圧の制御を行い、再度
上記第1.第2圧力検出手段からの信号に基づく上記制
御を繰返すように形成した。(Means for Solving the Problems) In order to solve the above-mentioned conventional problems, the present invention provides an expander, an air supply flow path having an air supply control valve and a shutoff valve following the suction side, and an air supply flow path for the expander. The screw compressor main body is driven by the expander of the drive unit, which is equipped with an exhaust flow path that continues to the exhaust side, and a bypass flow path that runs from the upstream side of the air supply control valve directly to the exhaust flow path via a bypass valve. In the method for controlling an expander-driven screw compressor, the expander-driven screw compressor is driven by: a first pressure detection means in the exhaust flow path; a second pressure detection means in the discharge flow path of the compressor main body; and control means for controlling the opening degree of the air supply control valve in response to a signal from the second pressure detection means, the first control means for controlling the opening degree of the air supply control valve in response to a signal from the second pressure detection means, In other cases, in the second case where the exhaust pressure is equal to the set value, the current operating state is maintained and the exhaust pressure is smaller than the set value. In the third case, the first
, the opening degree of the air supply control valve is increased until the second state is reached, and when the upper air exhaust pressure becomes lower than a predetermined set value, the bypass valve is opened to control the exhaust pressure, and the exhaust pressure is controlled again. Above 1st. The above control based on the signal from the second pressure detection means is repeated.
(実施例) 次に、本発明の一実施例を図面にしたがって説明する。(Example) Next, one embodiment of the present invention will be described with reference to the drawings.
第1図は本発明に係る制御方法を適用したスクリュ膨張
機を駆動手段とする膨張機駆動スクリュ圧縮機を示し、
制御系を除き、他は実質的に第4図に示すものと同一で
あり、対応する部分には互いに同一番号を付して説明を
省略する。FIG. 1 shows an expander-driven screw compressor using a screw expander as a driving means to which the control method according to the present invention is applied,
Except for the control system, the rest is substantially the same as that shown in FIG. 4, and corresponding parts are given the same numbers and their explanation will be omitted.
本圧縮機では、第4図に示す圧縮機と同様に第1圧力検
出器5を設けるとともに、さらに吐出流路15に第2圧
力検出器I6と、バイパス流路8のバイパス弁7の排気
流路6側に圧力調節計(PIC)17とスクリュ膨張機
lの回転軸部分に回転数リレー9と、第1.第2圧力検
出器5.16と給気加減弁2との間に介在さ仕た制御手
段I8とを設けて、給気加減弁2.バイパス弁7.しゃ
断弁3の制御を行うことによりスクリュ膨張機Iの回転
数制御を行うように形成しである。This compressor is provided with a first pressure detector 5 like the compressor shown in FIG. A pressure regulator (PIC) 17 is provided on the side of the passage 6, a rotation speed relay 9 is provided on the rotating shaft portion of the screw expander 1, and the first. A control means I8 interposed between the second pressure detector 5.16 and the supply air adjustment valve 2 is provided. Bypass valve7. By controlling the shutoff valve 3, the rotation speed of the screw expander I is controlled.
即ち、上記のように構成することにより、以下に説明す
る本発明に係る制御方法を実行するようになっている。That is, by configuring as described above, the control method according to the present invention described below can be executed.
次に、第2図に基いて上記装置に適用する本発明に係る
制御方法について説明する。Next, a control method according to the present invention applied to the above device will be explained based on FIG.
まず、装置が起動されると制御がスタートし、第1ステ
ツプ(Sl)で、制御手段8において、第2圧力検出器
16からの信号に基いて、これと予め設定した設定値(
1)とを比較して、(吐出圧カー設定値(1))が正(
〉0)の場合には第3ステツプ(S3)に、その他の場
合には第2ステツプ(S2)に進む。First, when the device is started up, control starts, and in the first step (Sl), the control means 8 uses the signal from the second pressure detector 16 to set the preset value (
1), (discharge pressure car setting value (1)) is positive (
>0), the process proceeds to the third step (S3); otherwise, the process proceeds to the second step (S2).
第2ステツプで、制御手段8において第1圧力検出器5
からの信号に基いて、これと予め設定した設定値(2)
とを比較して、(排気流路圧カー設定値(2))が正(
〉0)の場合には第3ステツプに、負(〈0)の場合に
は第6ステツプ(S6)に進み、0の場合には再度第1
ステツプに戻り、現状の運転状態を維持する。In a second step, the control means 8 detects the first pressure detector 5.
This and the preset setting value (2) based on the signal from
(Exhaust passage pressure car set value (2)) is positive (
If 〉0), proceed to the third step, if negative (〈0), proceed to the sixth step (S6), and if 0, proceed to the first step again.
Return to step and maintain current operating condition.
第3ステツプで、制御手段18により給気加減弁2の開
度を一定量だけ小さくする。In the third step, the control means 18 reduces the opening degree of the air supply control valve 2 by a certain amount.
第4ステツプ(S4)で、回転数リレー9により検出し
たスクリュ膨張機1の回転数と許容値とを比較させて、
この回転数が許容値以下の場合には第5ステツプ(S5
)に進み、その他の場合には再度第1ステツプに戻る。In the fourth step (S4), the rotation speed of the screw expander 1 detected by the rotation speed relay 9 is compared with an allowable value,
If this rotation speed is below the allowable value, the fifth step (S5
), otherwise return to the first step.
第5ステツプで、上記回転数リレー9からの信号により
しゃ断弁3を閉じ、スクリュ膨張機1を停止さけ、これ
に伴ってスクリュ圧縮機本体11も停止させた後、再度
第1ステツプに戻る。In the fifth step, the shutoff valve 3 is closed by the signal from the rotation speed relay 9, the screw expander 1 is stopped, and the screw compressor main body 11 is also stopped accordingly, and then the process returns to the first step again.
一方、第6ステツプで、制御手段18により給気加減弁
2の開度を一定量だけ大きくする。On the other hand, in the sixth step, the control means 18 increases the opening degree of the air supply control valve 2 by a certain amount.
第7ステツプ(S7)で、圧力調節計17により検出し
たバイパス流路圧(=膨張機排気圧)と予め設定した設
定値(3)とを比較して(バイパス流路圧−設定値(3
))が正の場合は第8ステツプ(S8)に、その他の場
合には第9ステツプ(S9)に進む。In the seventh step (S7), the bypass flow path pressure (=expander exhaust pressure) detected by the pressure regulator 17 is compared with a preset set value (3) (bypass flow path pressure - set value (3)
)) is positive, the process proceeds to the eighth step (S8); otherwise, the process proceeds to the ninth step (S9).
第8ステツプで、バイパス弁7を閉じた後、再度第1ス
テツプに戻る。After closing the bypass valve 7 in the eighth step, the process returns to the first step again.
第9ステツプで、バイパス弁7を開いた後再度第1ステ
ツプに戻る。In the ninth step, the bypass valve 7 is opened and then the process returns to the first step.
以後、上記各ステップの緑返しとなる。After that, each of the above steps will be repeated.
上記装置は本来的な用途に使用する蒸気を、補助的に別
の用途に利用するようにしたもので、基本的には膨張機
側の運転条件を優先した形になっているため、圧縮機側
で必要とする圧縮ガスが十分に供給することが出来ない
場合が生じるが、この時には別に他の圧縮機より圧縮ガ
スを供給する必要がある。即ち、本装置による圧縮ガス
の供給は、補助的に行うものである。The above device is designed to supplementally use the steam used for the original purpose for another purpose, and basically prioritizes the operating conditions of the expander, so the compressor There may be cases where the compressed gas required by the compressor cannot be sufficiently supplied, and in this case, it is necessary to separately supply compressed gas from another compressor. That is, the supply of compressed gas by this device is performed auxiliary.
なお、上記装置では図示しない制御フローにより例えば
スクリュ膨張機lの回転数が異常に上昇した場合、ある
いはその軸受部分の温度が異常に上昇した場合にはしゃ
断弁4を閉じスクリュ膨張機lを緊急停止(トリップ)
させるように形成しであるが、しゃ断弁4が閉まるとそ
れまでスクリュ膨張機lを通っていた蒸気の流れが止ま
るので、この蒸気をバイパス流路8から排気流路6に流
す必要がある。しかし、通常のしゃ断弁では全閉。In addition, in the above device, if the rotation speed of the screw expander 1 abnormally increases due to a control flow (not shown), or if the temperature of the bearing part of the screw expander 1 increases abnormally, the shutoff valve 4 is closed and the screw expander 1 is activated in an emergency manner. Stop (trip)
However, when the shutoff valve 4 closes, the flow of steam that has been passing through the screw expander 1 until then stops, so it is necessary to flow this steam from the bypass flow path 8 to the exhaust flow path 6. However, with a normal shutoff valve, it is fully closed.
全開の動作速度が遅く、排気流路圧力の変動が生じるこ
とがある。Fully open operation speed is slow and fluctuations in exhaust flow path pressure may occur.
そこで、これを防止するために、第1図中の一点鎖線枠
1内の部分を第3図に示すように制御手段I8によりバ
イパス弁7の制御も行えるようにして、第1圧力検出器
5からの圧力信号が異常に低い場合には、これに基いて
制御手段18によりバイパス弁7を緊急間とする信号を
発するように形成してもよい。Therefore, in order to prevent this, as shown in FIG. 3, the portion within the dashed-dotted line frame 1 in FIG. If the pressure signal from the bypass valve 7 is abnormally low, the control means 18 may be configured to issue a signal indicating that the bypass valve 7 is in an emergency state based on this signal.
また、上記実施例では油冷式のスクリュ圧縮機本体を使
用したものを示したが、本発明はこれに限るものでなく
、無給油式のスクリュ圧縮機本体を使用したものであっ
てもよい。Further, although the above embodiment uses an oil-cooled screw compressor main body, the present invention is not limited to this, and an oil-free screw compressor main body may be used. .
(発明の効果)
以上の説明より明らかなように、本発明によれば、膨張
機と、この吸込側に続く給気加減弁、しゃ断弁を有する
給気流路と、上記膨張機の排気側に続く排気流路と、上
記給気加減弁の上流側からバイパス弁を介して、直接上
記排気流路に至るバイパス流路とを備えた駆動部の上記
膨張機によりスクリュ圧縮機本体を駆動させるようにし
た膨張機駆動スクリュ圧縮機の制御方法において、上記
排気流路に第1圧力検出手段と、上記圧縮機本体の吐出
流路に第2圧力検出手段と、第1.第2圧力検出手段か
ら信号を受けて上記給気加減弁の開度を制御する制御手
段とを設けて、吐出ガス圧と膨張機排気圧のうちのいず
れか一方が設定値を超える第1の場合には上記給気加減
弁の開度を小さくし、その他の場合のうち上記排気圧が
設定値に等しい第2の場合には現状の運転状態を維持し
、上記排気圧が設定値より小さい第3の場合には、上記
第1.第2の状態になる迄上記給気加減弁の開度を大き
くしてゆき、上気排気圧が予め定めた設定値より低くな
ると上記バイパス弁を開いて上記排気圧の制御を行い、
再度上記第1.第2圧力検出手段からの信号に基づく上
記制御を繰返すように形成しである。(Effects of the Invention) As is clear from the above description, according to the present invention, there is provided an expander, an air supply flow path having an air supply control valve and a shutoff valve following the suction side, and an air supply flow path on the exhaust side of the expander. The screw compressor main body is driven by the expander of the drive unit, which has a continuous exhaust flow path and a bypass flow path that extends directly from the upstream side of the air supply control valve to the exhaust flow path via a bypass valve. In the control method for an expander-driven screw compressor, the method includes: a first pressure detection means in the exhaust flow path; a second pressure detection means in the discharge flow path of the compressor body; and control means for controlling the opening degree of the air supply control valve in response to a signal from the second pressure detection means, the first control means for controlling the opening degree of the air supply control valve in response to a signal from the second pressure detection means, In other cases, the opening degree of the air supply control valve is reduced, and in the second case where the exhaust pressure is equal to the set value, the current operating state is maintained, and the exhaust pressure is smaller than the set value. In the third case, the above-mentioned first. The opening degree of the air supply control valve is increased until a second state is reached, and when the upper air exhaust pressure becomes lower than a predetermined set value, the bypass valve is opened to control the exhaust pressure,
Repeat the above No. 1. It is configured to repeat the above control based on the signal from the second pressure detection means.
このため、蒸気および圧縮ガスの使用量に応じて膨張機
の回転数を制御し、また余剰の蒸気はバイパス流路より
排気流路に流して給気流路を減圧することにより外部膨
張比を一定にすることが出来、高効率点での連続運転が
可能になるという効果を奏する。For this reason, the external expansion ratio is kept constant by controlling the rotation speed of the expander according to the amount of steam and compressed gas used, and by flowing excess steam from the bypass flow path to the exhaust flow path to reduce the pressure in the supply air flow path. This has the effect of enabling continuous operation at a high efficiency point.
第1図は本発明に係る制御方法を適用した膨張機駆動ス
フリス圧縮機の蒸気の系統図、第2図は第1図に示す装
置に適用する制御方法を示すフローチャート、第3図は
第1図とは別の本発明の適用例の一部を示す系統図、第
4図は従来の制御方法を適用した膨張機駆動スクリュ圧
縮機の蒸気の系統図である。
I・・・スクリュ膨張機、2・・・給気加減弁、3・・
・しゃ断弁、4・・・給気流路、5・・・第1圧力検出
器、6・・・排気流路、7・・・バイパス弁、!■・・
・スクリュ圧縮機本体、15・・・吐出流路、16・・
・第2圧力検出器、17・・・圧力調節計、18・・・
制御手段。
第1図
第3図Fig. 1 is a steam system diagram of an expander-driven Suflis compressor to which the control method according to the present invention is applied, Fig. 2 is a flowchart showing the control method applied to the device shown in Fig. FIG. 4 is a system diagram showing a part of an application example of the present invention other than the one shown in the figure, and FIG. 4 is a steam system diagram of an expander-driven screw compressor to which a conventional control method is applied. I...Screw expander, 2...Air supply control valve, 3...
- Shutoff valve, 4... Air supply flow path, 5... First pressure detector, 6... Exhaust flow path, 7... Bypass valve,! ■・・・
・Screw compressor main body, 15...Discharge flow path, 16...
-Second pressure detector, 17...pressure regulator, 18...
control means. Figure 1 Figure 3
Claims (1)
弁を有する給気流路と、上記膨張機の排気側に続く排気
流路と、上記給気加減弁の上流側からバイパス弁を介し
て、直接上記排気流路に至るバイパス流路とを備えた駆
動部の上記膨張機によりスクリュ圧縮機本体を駆動させ
るようにした膨張機駆動スクリュ圧縮機の制御方法にお
いて、上記排気流路に第1圧力検出手段と、上記圧縮機
本体の吐出流路に第2圧力検出手段と、第1、第2圧力
検出手段から信号を受けて上記給気加減弁の開度を制御
する制御手段とを設けて、吐出ガス圧と膨張機排気圧の
うちのいずれか一方が設定値を超える第1の場合には上
記給気加減弁の開度を小さくし、その他の場合のうち上
記排気圧が設定値に等しい第2の場合には現状の運転状
態を維持し、上記排気圧が設定値より小さい第3の場合
には、上記第1、第2の状態になる迄上記給気加減弁の
開度を大きくしてゆき、上気排気圧が予め定めた設定値
より低くなると上記バイパス弁を開いて上記排気圧の制
御を行い、再度上記第1、第2圧力検出手段からの信号
に基づく上記制御を繰返すようにしたことを特徴とする
膨張機駆動スクリュ圧縮機の制御方法。(1) An expander, an air supply flow path having an air supply control valve and a shutoff valve following the suction side, an exhaust flow path following the exhaust side of the expander, and a bypass valve from the upstream side of the air supply control valve. In the method for controlling an expander-driven screw compressor, the screw compressor main body is driven by the expander of the drive section, which has a bypass flow path leading directly to the exhaust flow path through the exhaust flow path. a first pressure detection means in the discharge passage of the compressor main body, a second pressure detection means in the discharge passage of the compressor main body, and a control means for receiving signals from the first and second pressure detection means and controlling the opening degree of the air supply control valve. In the first case where either the discharge gas pressure or the expander exhaust pressure exceeds the set value, the opening degree of the air supply control valve is reduced, and in other cases, the exhaust pressure In the second case where the exhaust pressure is equal to the set value, the current operating state is maintained, and in the third case where the exhaust pressure is lower than the set value, the supply air control valve is operated until the above first and second states are reached. When the upper air exhaust pressure becomes lower than a predetermined set value, the bypass valve is opened to control the exhaust pressure, and the signal from the first and second pressure detection means is again increased. A control method for an expander-driven screw compressor, characterized in that the above-mentioned control based on the above is repeated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11777288A JPH01285692A (en) | 1988-05-12 | 1988-05-12 | Control method for screw compressor driven by expansion machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11777288A JPH01285692A (en) | 1988-05-12 | 1988-05-12 | Control method for screw compressor driven by expansion machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01285692A true JPH01285692A (en) | 1989-11-16 |
Family
ID=14719945
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11777288A Pending JPH01285692A (en) | 1988-05-12 | 1988-05-12 | Control method for screw compressor driven by expansion machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01285692A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5467613A (en) * | 1994-04-05 | 1995-11-21 | Carrier Corporation | Two phase flow turbine |
US5957668A (en) * | 1996-01-17 | 1999-09-28 | The United States Of America As Represented By The Secretary Of The Navy | Brake actuation means for a rotary pump system |
JP2008169777A (en) * | 2007-01-12 | 2008-07-24 | Kobe Steel Ltd | Power generating device |
JP2009250196A (en) * | 2008-04-10 | 2009-10-29 | Kobe Steel Ltd | Steam expander driving air compression device |
JP2009257119A (en) * | 2008-04-14 | 2009-11-05 | Kobe Steel Ltd | Steam expander driven air compression apparatus |
CN102840136A (en) * | 2011-06-22 | 2012-12-26 | 株式会社神户制钢所 | Steam drive type compression device |
CN102840139A (en) * | 2011-06-22 | 2012-12-26 | 株式会社神户制钢所 | Steam drive type compression device |
-
1988
- 1988-05-12 JP JP11777288A patent/JPH01285692A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5467613A (en) * | 1994-04-05 | 1995-11-21 | Carrier Corporation | Two phase flow turbine |
US5957668A (en) * | 1996-01-17 | 1999-09-28 | The United States Of America As Represented By The Secretary Of The Navy | Brake actuation means for a rotary pump system |
JP2008169777A (en) * | 2007-01-12 | 2008-07-24 | Kobe Steel Ltd | Power generating device |
JP2009250196A (en) * | 2008-04-10 | 2009-10-29 | Kobe Steel Ltd | Steam expander driving air compression device |
JP2009257119A (en) * | 2008-04-14 | 2009-11-05 | Kobe Steel Ltd | Steam expander driven air compression apparatus |
CN102840136A (en) * | 2011-06-22 | 2012-12-26 | 株式会社神户制钢所 | Steam drive type compression device |
CN102840139A (en) * | 2011-06-22 | 2012-12-26 | 株式会社神户制钢所 | Steam drive type compression device |
JP2013007284A (en) * | 2011-06-22 | 2013-01-10 | Kobe Steel Ltd | Steam driven compressor apparatus |
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