JP2009257119A - Steam expander driven air compression apparatus - Google Patents

Steam expander driven air compression apparatus Download PDF

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JP2009257119A
JP2009257119A JP2008104653A JP2008104653A JP2009257119A JP 2009257119 A JP2009257119 A JP 2009257119A JP 2008104653 A JP2008104653 A JP 2008104653A JP 2008104653 A JP2008104653 A JP 2008104653A JP 2009257119 A JP2009257119 A JP 2009257119A
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steam
expander
pressure
air compressor
positive displacement
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Masaki Matsukuma
正樹 松隈
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Kobe Steel Ltd
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Kobe Steel Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a steam expander driven air compression apparatus capable of stably recovering pressure difference energy irrespective of the amount of steam used. <P>SOLUTION: The steam expander driven air compression apparatus 1 includes a displacement type steam expander 2, a displacement type air compressor 3 driven by the displacement type steam expander 2, a capacity regulation valve 6 which can regulate the air intake amount of the displacement type steam expander 2, and a control device 12 for controlling the opening degree of the capacity regulation valve 6 so that the pressure on the discharge side of the displacement type air compressor 3 may be constant. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、蒸気膨張機駆動空気圧縮装置に関する。   The present invention relates to a steam expander driven air compressor.

ボイラで発生した蒸気を使用するプラントにおいて、ボイラが発生する高圧(例えば1.2〜1.6MPa)の蒸気を減圧弁で減圧し、低圧(例えば0.8〜0.9MPa)の蒸気を需要設備に供給するのが一般的である。減圧弁で蒸気を減圧すると、蒸気の圧力差エネルギを廃棄することになるため、このエネルギを回収することが望まれる。   In a plant that uses steam generated in a boiler, high pressure (for example, 1.2 to 1.6 MPa) steam generated by the boiler is reduced by a pressure reducing valve, and low pressure (for example, 0.8 to 0.9 MPa) steam is demanded. It is common to supply equipment. When the pressure of the steam is reduced by the pressure reducing valve, the pressure difference energy of the steam is discarded, and it is desired to recover this energy.

特許文献1のように、スクリュ式蒸気膨張機で発電機を駆動することで、蒸気の圧力差エネルギを電気エネルギとして回収する装置が提案されている。一般に、発電機は、一定の速度で運転することが必要であるが、スクリュ式蒸気膨張機の速度を一定に保つと、低圧側の蒸気圧力が変動することになってしまう。   As in Patent Document 1, an apparatus that recovers steam pressure difference energy as electric energy by driving a generator with a screw-type steam expander has been proposed. Generally, the generator needs to be operated at a constant speed, but if the speed of the screw-type steam expander is kept constant, the steam pressure on the low pressure side will fluctuate.

スクリュ式蒸気膨張機の速度制御は、特許文献1に記載されているように、吐出圧が一定になるように、吸込側に設けた流量調整弁の開度を制御するのが一般的である。そこで、速度変化に対応可能な発電機を用いて、スクリュ式蒸気膨張機の吐出圧が一定になるように制御することで、蒸気使用量の変化に対応することが可能になる。   As described in Patent Document 1, the speed control of the screw-type steam expander generally controls the opening degree of the flow rate adjusting valve provided on the suction side so that the discharge pressure becomes constant. . Therefore, it is possible to cope with a change in the amount of steam used by controlling the discharge pressure of the screw-type steam expander to be constant by using a generator that can respond to the speed change.

しかしながら、小規模のプラントでは、蒸気使用量が不安定であるため、スクリュ式蒸気膨張機の吐出側の圧力を一定に保とうとすると、スクリュ式蒸気膨張機の回転数の変動が非常に大きくなる。このため、蒸気使用量が低下したときに、スクリュ式蒸気膨張機の出力トルクが不足して発電機を駆動できなくなる場合がある。   However, since the amount of steam used is unstable in a small-scale plant, if the pressure on the discharge side of the screw-type steam expander is kept constant, the fluctuation of the rotational speed of the screw-type steam expander becomes very large. . For this reason, when the amount of steam used decreases, the output torque of the screw steam expander may be insufficient and the generator may not be driven.

特許文献2には、スクリュ式蒸気膨張機でスクリュ式空気圧縮機を駆動して、空気を圧縮する装置が記載されている。しかしながら、蒸気使用量と圧縮空気消費量とが比例関係にない場合には、スクリュ式蒸気膨張機の吐出側の圧力を一定に保つと、発生する圧縮空気の量が制御できず、圧縮空気に過不足が生じて、圧縮空気の圧力が変動してしまうという問題がある。   Patent Document 2 describes an apparatus that compresses air by driving a screw-type air compressor with a screw-type steam expander. However, if the amount of steam used and the amount of compressed air consumed are not proportional, keeping the pressure on the discharge side of the screw-type steam expander constant prevents the amount of compressed air generated from being controlled. There is a problem that the pressure of the compressed air fluctuates due to excess or deficiency.

しかしながら、
特開2007−16614号公報 特開昭63−50692号公報
However,
JP 2007-16614 A Japanese Patent Laid-Open No. 63-50692

前記問題点に鑑みて、本発明は、蒸気の使用量に拘わらず、安定して圧力差エネルギを回収できる蒸気膨張機駆動空気圧縮装置を提供することを課題とする。   In view of the above problems, an object of the present invention is to provide a steam expander-driven air compressor that can stably recover pressure difference energy regardless of the amount of steam used.

前記課題を解決するために、本発明による蒸気膨張機駆動空気圧縮装置は、容積形蒸気膨張機と、前記容積形蒸気膨張機によって駆動される容積形空気圧縮機と、前記容積形蒸気膨張弁の吸気量を調節可能な容量調整弁と、前記容積形空気圧縮機の吐出側の圧力が一定になるように、前記容量調整弁の開度を制御する制御装置とを有するものとする。   In order to solve the above problems, a steam expander-driven air compressor according to the present invention includes a positive displacement steam expander, a positive displacement air compressor driven by the positive displacement steam expander, and the positive displacement steam expansion valve. And a control device for controlling the opening degree of the capacity adjusting valve so that the pressure on the discharge side of the positive displacement air compressor is constant.

この構成によれば、容量調整弁によって、容積形空気圧縮機に必要な駆動トルクに応じた量の蒸気を容積形蒸気膨張機に供給するので、容積形空気圧縮機を安定して駆動できる。   According to this configuration, since the amount of steam corresponding to the drive torque required for the positive displacement air compressor is supplied to the positive displacement steam expander by the capacity adjustment valve, the positive displacement air compressor can be driven stably.

また、本発明の蒸気膨張機駆動空気圧縮装置は、前記容積形空気圧縮機の吐出側の圧力を検出する圧力検出器を有し、前記制御装置は、前記圧力検出器の検出信号に基づいて、前記容量調整弁の開度をPID制御してもよい   The steam expander-driven air compressor of the present invention has a pressure detector that detects the pressure on the discharge side of the positive displacement air compressor, and the control device is based on a detection signal of the pressure detector. The PID control may be performed on the opening of the capacity adjustment valve.

この構成によれば、広く流通しているPIDコントローラを使用でき、構成が簡単で、低コストである。   According to this configuration, a widely distributed PID controller can be used, the configuration is simple, and the cost is low.

また、本発明の蒸気膨張機駆動空気圧縮装置において、前記容積形蒸気膨張機は、減速機を介して前記容積形空気圧縮機を駆動してもよい。   In the steam expander-driven air compressor of the present invention, the positive displacement steam expander may drive the positive displacement air compressor via a speed reducer.

この構成によれば、容積形空気圧縮機の負荷トルクに応じて減速機の減速比を選択することで、機械効率が高くなる。   According to this structure, mechanical efficiency becomes high by selecting the reduction ratio of a reduction gear according to the load torque of a positive displacement air compressor.

また、本発明の蒸気膨張機駆動空気圧縮装置において、前記容積形蒸気膨張機は、スクリュ膨張機であり、前記容積形空気圧縮機は、スクリュ圧縮機であってもよい。   In the steam expander-driven air compressor according to the present invention, the positive displacement steam expander may be a screw expander, and the positive displacement air compressor may be a screw compressor.

この構成によれば、スクリュ膨張機およびスクリュ圧縮機のトルク変動が小さいために、運転可能な圧力範囲が広く、安定した運転ができる。   According to this configuration, since the torque fluctuation of the screw expander and the screw compressor is small, the operable pressure range is wide and stable operation can be performed.

また、本発明の蒸気膨張機駆動空気圧縮装置において、前記容量調整弁の上流と前記容積形蒸気膨張機の吐出側とを減圧弁を介して接続してもよい。   In the steam expander-driven air compressor of the present invention, the upstream side of the capacity adjustment valve and the discharge side of the positive displacement steam expander may be connected via a pressure reducing valve.

この構成によれば、蒸気の使用量が多い場合に、減圧弁を介して、蒸気膨張機駆動空気圧縮装置をバイパスして必要な蒸気を需要設備に供給できる。   According to this configuration, when the amount of steam used is large, it is possible to supply necessary steam to the demand facility by bypassing the steam expander-driven air compression device via the pressure reducing valve.

本発明によれば、容積形蒸気膨張機で容積形空気圧縮機を駆動し、容積形空気圧縮機の吐出側の圧力を一定に保つように、容積形蒸気膨張機の吸込側に設けた容量調整弁の開度を調節するので、蒸気の供給圧力と使用圧力との差圧エネルギを空圧エネルギとして安定して回収できる。   According to the present invention, the capacity provided on the suction side of the positive displacement steam expander so as to drive the positive displacement air compressor with the positive displacement steam expander and keep the pressure on the discharge side of the positive displacement air compressor constant. Since the opening degree of the regulating valve is adjusted, the differential pressure energy between the supply pressure of steam and the operating pressure can be stably recovered as pneumatic energy.

これより、本発明の実施形態について、図面を参照しながら説明する。
図1は、本発明の1つの実施形態の蒸気膨張機駆動空気圧縮装置1の概要を示す。蒸気膨張機駆動空気圧縮装置1は、容積形蒸気膨張機であるスクリュ膨張機(エキスパンダ)2と、容積形空気圧縮機であるスクリュ圧縮機3とを有し、スクリュ膨張機2の出力軸とスクリュ圧縮機3の入力軸とが減速機4を介して接続されている。
Embodiments of the present invention will now be described with reference to the drawings.
FIG. 1: shows the outline | summary of the steam expander drive air compression apparatus 1 of one Embodiment of this invention. The steam expander-driven air compressor 1 has a screw expander (expander) 2 that is a positive displacement steam expander and a screw compressor 3 that is a positive displacement air compressor, and an output shaft of the screw expander 2. And an input shaft of the screw compressor 3 are connected via a speed reducer 4.

スクリュ膨張機2には、不図示のボイラから高圧蒸気がスチームトラップ5および容量調整弁6を介して供給されている。スクリュ膨張機2は、吸気した蒸気の膨張力を回転力に変換して、膨張により減圧された低圧蒸気を不図示の需要設備に供給するようになっている。また、蒸気膨張機駆動空気圧縮装置1は、高圧蒸気を減圧弁7を介して、スクリュ膨張機2を介さずに低圧側に供給することができるようになっている。   The screw expander 2 is supplied with high-pressure steam from a boiler (not shown) via a steam trap 5 and a capacity adjustment valve 6. The screw expander 2 converts the expansion force of the inhaled steam into a rotational force, and supplies low-pressure steam decompressed by expansion to a demand facility (not shown). The steam expander-driven air compressor 1 can supply high-pressure steam to the low pressure side via the pressure reducing valve 7 and not via the screw expander 2.

スクリュ圧縮機3は、エアフィルタ8を介して空気を吸引し、圧縮して吐出する。スクリュ圧縮機3が吐出した圧縮空気は、オイルセパレータ9で潤滑油が分離され、アフタークーラ10で冷却されて需要設備に供給される。   The screw compressor 3 sucks air through the air filter 8, compresses it, and discharges it. The compressed air discharged from the screw compressor 3 is separated from the lubricating oil by the oil separator 9, cooled by the aftercooler 10, and supplied to the demand facility.

蒸気膨張機駆動空気圧縮装置1は、オイルセパレータ9の出口配管に圧力検出器11が設置されており、PID制御装置12によって圧力検出器11の検出圧力が所定の設定圧力になるように、容量調整弁6の開度をPID制御するようになっている。   The steam expander-driven air compressor 1 is provided with a pressure detector 11 at the outlet pipe of the oil separator 9 so that the PID controller 12 can detect the pressure detected by the pressure detector 11 at a predetermined set pressure. The opening degree of the regulating valve 6 is PID controlled.

オイルセパレータ9で分離された潤滑油は、自動温度調整弁13、オイルクーラ14およびオイルフィルタ15を介して、スクリュ膨張機2の軸受部およびスクリュ圧縮機3のロータ室に供給される。また、スクリュ膨張機2が停止したとき、スクリュ膨張機2の軸受部への潤滑油の供給を直ちに停止できるように、電磁弁16が配設されている。さらに、スクリュ膨張機2の軸受部に供給された潤滑油は、減速機4に流入して減速機4を潤滑し、減速機4から流出した潤滑油は、逆止弁17を介してスクリュ圧縮機3のロータ室に供給される。   The lubricating oil separated by the oil separator 9 is supplied to the bearing portion of the screw expander 2 and the rotor chamber of the screw compressor 3 via the automatic temperature control valve 13, the oil cooler 14, and the oil filter 15. Moreover, when the screw expander 2 stops, the solenoid valve 16 is arrange | positioned so that supply of the lubricating oil to the bearing part of the screw expander 2 can be stopped immediately. Furthermore, the lubricating oil supplied to the bearing portion of the screw expander 2 flows into the speed reducer 4 to lubricate the speed reducer 4, and the lubricating oil flowing out of the speed reducer 4 is screw-compressed via the check valve 17. It is supplied to the rotor chamber of the machine 3.

本実施形態の蒸気膨張機駆動空気圧縮装置1では、圧縮空気の需要が少ない場合、圧力検出器11の検出圧力、つまり、スクリュ圧縮機3の吐出側の空気圧が上昇するため、PID制御装置12によって、スクリュ膨張機2の吸込の容量調整弁6の開度が制限され、スクリュ膨張機2への蒸気供給量が少なくなる。これによって、スクリュ膨張機2の回転数は減少し、スクリュ圧縮機3の吐出圧も低下するので、スクリュ圧縮機3の吐出側の圧力(圧縮空気の需要設備への供給圧力)が低下し、所定の設定圧力に回復する。   In the steam expander-driven air compressor 1 of the present embodiment, when the demand for compressed air is small, the pressure detected by the pressure detector 11, that is, the air pressure on the discharge side of the screw compressor 3 increases, so the PID control device 12. Thus, the opening degree of the capacity adjustment valve 6 for suction of the screw expander 2 is limited, and the amount of steam supplied to the screw expander 2 is reduced. As a result, the rotational speed of the screw expander 2 decreases and the discharge pressure of the screw compressor 3 also decreases, so the pressure on the discharge side of the screw compressor 3 (supply pressure to the demand facility of compressed air) decreases. Recover to the preset pressure.

また、圧縮空気の需要が多い場合、スクリュ圧縮機3の吐出側の圧力が低下するため、PID制御装置12によって、スクリュ膨張機2の吸込の容量調整弁6が大きく開かれる。これによって、スクリュ膨張機2の回転数が増大し、スクリュ圧縮機3の吐出圧も上昇するので、圧縮空気の供給圧力が上昇し、設定圧力を回復する。   In addition, when the demand for compressed air is high, the pressure on the discharge side of the screw compressor 3 decreases, so the PID control device 12 opens the suction capacity adjustment valve 6 of the screw expander 2 widely. As a result, the rotational speed of the screw expander 2 increases and the discharge pressure of the screw compressor 3 also increases, so that the supply pressure of the compressed air increases and the set pressure is restored.

詳しく説明すると、容積形蒸気膨張機であるスクリュ膨張機2の出力トルクは、吸込圧力と吐出圧力との差によって決まる。また、同様に、容積形空気圧縮機であるスクリュ圧縮機3の駆動トルクは、吸気圧力と吐出圧力との差圧によって決まる。このため、スクリュ圧縮機3の駆動に必要なトルクに合わせて、容量調整弁6の開度を調節することによって実質的なスクリュ膨張機2の吸気圧力を低下させることで、スクリュ膨張機2の出力を制御して、所望の圧力の圧縮空気を発生させることができる。   More specifically, the output torque of the screw expander 2 that is a positive displacement steam expander is determined by the difference between the suction pressure and the discharge pressure. Similarly, the driving torque of the screw compressor 3, which is a positive displacement air compressor, is determined by the differential pressure between the intake pressure and the discharge pressure. For this reason, by adjusting the opening degree of the capacity adjusting valve 6 in accordance with the torque required for driving the screw compressor 3, the substantial intake pressure of the screw expander 2 is reduced. The output can be controlled to generate the desired pressure of compressed air.

このように、本実施形態では、圧縮空気の圧力に応じて、スクリュ膨張機2の蒸気流量を調節するので、ボイラから供給される高圧蒸気と、常用設備で使用する低圧蒸気との差圧エネルギを空圧エネルギとして安定して回収し、一定圧力の圧縮空気を供給することができる。   Thus, in this embodiment, since the steam flow rate of the screw expander 2 is adjusted according to the pressure of the compressed air, the differential pressure energy between the high-pressure steam supplied from the boiler and the low-pressure steam used in the regular equipment. Can be stably recovered as pneumatic energy, and compressed air with a constant pressure can be supplied.

また、本実施形態において、減速機4は、スクリュ膨張機2を最適な条件で運転したときのスクリュ膨張機2の出力が、スクリュ圧縮機3によって空気を圧縮するのに最適なトルクとなるように減速している。これによって、蒸気膨張機駆動空気圧縮装置1全体の機械効率が最適化され、エネルギ回収効率を高めている。   Further, in the present embodiment, the speed reducer 4 is configured so that the output of the screw expander 2 when the screw expander 2 is operated under an optimal condition is an optimum torque for compressing air by the screw compressor 3. Has slowed down. This optimizes the mechanical efficiency of the entire steam expander-driven air compressor 1 and increases the energy recovery efficiency.

また、本実施形態において、圧縮空気の需要に比して蒸気の需要が多い場合は、減圧弁7を介して蒸気需要設備に蒸気を供給することができる。   In the present embodiment, when the demand for steam is greater than the demand for compressed air, the steam can be supplied to the steam demand facility via the pressure reducing valve 7.

本発明の蒸気膨張機駆動空気圧縮装置は、蒸気タービンのような速度形の機器と比べて、運転可能範囲の広い容積形の蒸気膨張機および空気圧縮機、特に、回転形で振動(回転中の位相によるトルク変動)の小さいスクリュ膨張機およびスクリュ圧縮機を使用することで、圧縮空気の需要変動に拘わらず、安定した運転が可能である。   The steam expander-driven air compressor of the present invention has a larger capacity steam expander and air compressor, particularly a rotary type that vibrates (during rotation) compared to a speed-type device such as a steam turbine. By using a screw expander and a screw compressor that have a small torque fluctuation due to the phase of the compressor, stable operation is possible regardless of fluctuations in demand for compressed air.

また、本発明において、蒸気膨張機の吸気側の容量調整弁の空気圧縮機の吐出側の圧力に基づいた制御は、PID制御に限らず、いかなる制御を用いてもよい。   In the present invention, the control based on the pressure on the discharge side of the air compressor of the capacity adjustment valve on the intake side of the steam expander is not limited to PID control, and any control may be used.

本発明の実施形態の蒸気膨張機駆動空気圧縮装置の概略図。1 is a schematic diagram of a steam expander-driven air compression device according to an embodiment of the present invention.

符号の説明Explanation of symbols

1…蒸気膨張機駆動空気圧縮装置
2…スクリュ膨張機(容積形蒸気膨張機)
3…スクリュ圧縮機(容積形空気圧縮機)
4…減速機
6…流量調整弁
7…減圧弁
11…圧力検出器
12…PID制御装置
DESCRIPTION OF SYMBOLS 1 ... Steam expander drive air compressor 2 ... Screw expander (volume type steam expander)
3 ... Screw compressor (displacement type air compressor)
DESCRIPTION OF SYMBOLS 4 ... Reducer 6 ... Flow control valve 7 ... Pressure reducing valve 11 ... Pressure detector 12 ... PID control apparatus

Claims (5)

容積形蒸気膨張機と、
前記容積形蒸気膨張機によって駆動される容積形空気圧縮機と、
前記容積形蒸気膨張機の吸気量を調節可能な容量調整弁と、
前記容積形空気圧縮機の吐出側の圧力が一定になるように、前記容量調整弁の開度を制御する制御装置とを有することを特徴とする蒸気膨張機駆動空気圧縮装置。
A positive displacement steam expander;
A positive displacement air compressor driven by the positive displacement steam expander;
A capacity adjustment valve capable of adjusting an intake amount of the positive displacement steam expander;
A steam expander-driven air compressor, comprising: a controller that controls an opening of the capacity adjustment valve so that a pressure on a discharge side of the positive displacement air compressor is constant.
前記容積形空気圧縮機の吐出側の圧力を検出する圧力検出器を有し、
前記制御装置は、前記圧力検出器の検出信号に基づいて、前記容量調整弁の開度をPID制御することを特徴とする請求項1に記載の蒸気膨張機駆動空気圧縮装置。
A pressure detector for detecting the pressure on the discharge side of the positive displacement air compressor;
2. The steam expander-driven air compressor according to claim 1, wherein the control device performs PID control of an opening of the capacity adjustment valve based on a detection signal of the pressure detector.
前記容積形蒸気膨張機は、減速機を介して前記容積形空気圧縮機を駆動することを特徴とする請求項1または2に記載の蒸気膨張機駆動空気圧縮装置。   The steam expander-driven air compressor according to claim 1 or 2, wherein the positive displacement steam expander drives the positive displacement air compressor via a speed reducer. 前記容積形蒸気膨張機は、スクリュ膨張機であり、前記容積形空気圧縮機は、スクリュ圧縮機であることを特徴とする請求項1から3のいずれかに記載の蒸気膨張機駆動空気圧縮装置。   4. The steam expander-driven air compressor according to claim 1, wherein the positive displacement steam expander is a screw expander, and the positive displacement air compressor is a screw compressor. 5. . 前記容量調整弁の上流と前記容積形蒸気膨張機の吐出側とを減圧弁を介して接続したことを特徴とする請求項1から4のいずれかに記載の蒸気膨張機駆動空気圧縮装置。   5. The steam expander-driven air compressor according to claim 1, wherein an upstream side of the capacity adjustment valve and a discharge side of the positive displacement steam expander are connected via a pressure reducing valve.
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