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JP3854489B2 - Crusher explosion-proof system - Google Patents
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JP3854489B2 - Crusher explosion-proof system - Google Patents

Crusher explosion-proof system Download PDF

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Publication number
JP3854489B2
JP3854489B2 JP2001324543A JP2001324543A JP3854489B2 JP 3854489 B2 JP3854489 B2 JP 3854489B2 JP 2001324543 A JP2001324543 A JP 2001324543A JP 2001324543 A JP2001324543 A JP 2001324543A JP 3854489 B2 JP3854489 B2 JP 3854489B2
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Japan
Prior art keywords
crusher
gas
oxygen concentration
exhaust gas
explosion
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JP2001324543A
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Japanese (ja)
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JP2003126725A (en
Inventor
尚 矢作
清一郎 井上
誠二 佐藤
康治 真野
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Takuma Co Ltd
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Takuma Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、例えば廃棄物を破砕処理する破砕施設で用いられる破砕機防爆システムの改良に関する。
【0002】
【従来の技術】
従来、この種の破砕機防爆システムとしては、例えば実開昭53−132071号、特開昭54−108062号、実開昭56−34554号(実公昭58−8340号)、特開昭56−89849号(特公昭58−13220号)、特開昭58−81451号、特開昭59−130544号(特公平2−33421号)、特開昭60−94154号(特公平5−39665号)、実開昭63−152645号(実公平3−56258号)、実開平3−115043号、特開平4−87645号、特開平5−7793号、実開平6−72639号等に記載されたものが知られている。
【0003】
而して、従来のものは、空気(希釈気体)、水蒸気、水、不活性ガス、蒸気を含んだ燃焼排ガス等の非酸素ガスを破砕機内に吹き込んで破砕機内の酸素濃度を可燃ガスの爆発限界外に保持し、爆発を未然に防ごうとするものである。
【0004】
【発明が解決しようとする課題】
ところが、従来の何れのものも、非酸素ガスを供給する供給源は、非酸素ガスだけしか発生させる事ができず、所謂破砕機の防爆に対する専用のものであった。
この為、従来のものは、トータル的なイニシャルコストとランニングコストが高く付くと共に、省エネルギ効果を発揮する事ができなかった。
【0005】
本発明は、叙上の問題点に鑑み、これを解消する為に創案されたもので、その課題とする処は、トータル的なイニシャルコストとランニングコストの低減を図ると共に、省エネルギ効果を充分に発揮できる様にした破砕機防爆システムを提供するにある。
【0006】
【課題を解決するための手段】
本発明の破砕機防爆システムは、基本的には、廃棄物を破砕処理する破砕機と、燃焼ガスに依りタービンを回転させてその動力に依り発電するガスタービン発電装置と、ガスタービン発電装置からの排ガスを破砕機内に供給して破砕機内の酸素濃度を可燃性ガスの爆発限界外に保持する排ガス供給装置と、から構成した事に特徴が存する。
【0007】
ガスタービン発電装置からの排ガスは、排ガス供給装置に依り破砕機内に吹き込まれる。この時、排ガス供給装置に依り破砕機内の酸素濃度が可燃性ガスの爆発限界外に保持されるので、爆発が抑制される。
ガスタービン発電装置に依り発電された電力は、破砕施設内での必要電力に利用される。
排ガスを供給するガスタービン発電装置は、破砕機の防爆に対する排ガスだけでなく電力も発電するので、破砕施設としては、トータル的なイニシャルコストとランニングコストの低減を図る事ができると共に、省エネルギ効果を充分に発揮できる。
【0008】
ガスタービン発電装置からの排ガスの酸素濃度を低下させる酸素濃度調整装置を備えているのが好ましい。この様にすれば、ガスタービン発電装置からの排ガスの酸素濃度が高い場合でも、これを低下させる事ができ、破砕機内の酸素濃度を可燃性ガスの爆発限界外に容易に保持できる。
【0009】
ガスタービン発電装置からの排ガスを熱交換する熱交換器を備えているのが好ましい。この様にすれば、ガスタービン発電装置からの排ガスの熱を破砕施設内で利用する事ができ、破砕施設に於ける省エネルギ効果をより一層高める事ができる。
【0010】
破砕機の入口側と出口側に配されてガスの漏洩を防ぐシール装置を備えているのが好ましい。この様にすれば、破砕機内の酸素濃度を可燃ガスの爆発限度外に容易に保持する事ができる。
【0011】
酸素濃度が設定値より越えた際に破砕機への廃棄物の供給を停止する廃棄物供給停止装置を備えているのが好ましい。この様にすれば、それ以上の可燃ガスの増加を防止でき、爆発を未然に防止できる。
【0012】
破砕機の入口側から出口側へ排ガスを循環させる排ガス循環装置を備えているのが好ましい。この様にすれば、破砕機内の下部から上部への気流特性を利用して排ガスを循環させる事ができ、排ガスの供給量を低減できる。
【0013】
排ガス供給装置は、ガスタービン発電装置からの排ガスを破砕機内に噴射するノズルと、ガスタービン発電装置とノズルとを接続する導入路と、導入路の途中に設けられて排ガスの供給量を調整する調整弁と、破砕機内の酸素濃度を検出する酸素濃度計と、破砕機内の可燃ガスを検知する可燃ガス検知器と、酸素濃度計からの信号と可燃ガス検知器からの信号に基づき酸素濃度が設定値以下になる様に調整弁を制御する制御器とを備えているのが好ましい。この様にすれば、ガスタービン発電装置からの排ガスを破砕機内に効率良く供給する事ができる。
【0014】
廃棄物供給停止装置は、廃棄物を供給する供給コンベアと、破砕機内の酸素濃度を検出する酸素濃度計と、破砕機内の可燃ガスを検知する可燃ガス検知器と、酸素濃度計からの信号と可燃ガス検知器からの信号に基づき酸素濃度が設定値以上になった際には供給コンベアを停止制御する制御器とを備えているのが好ましい。この様にすれば、排ガス供給装置の構成の一部を利用できるので、構造の簡単化とコストの低減を図る事ができる。
【0015】
排ガス循環装置は、破砕機の入口側と出口側とを連通する連通路と、連通路の途中に設けられて破砕機の入口側から出口側へ排ガスを送給する送風機とを備えているのが好ましい。この様にすれば、簡単な構成に依り能率良く排ガスを循環する事ができる。
【0016】
【発明の実施の形態】
以下、本発明の実施の形態を、図面に基づいて説明する。
図1は、本発明の破砕機防爆システムを示す概要図である。
【0017】
破砕機防爆システム1は、破砕機2、ガスタービン発電装置3、排ガス供給装置4、酸素濃度調整装置5、熱交換器6、シール装置7、廃棄物供給停止装置8、排ガス循環装置9とからその主要部が構成されて居り、廃棄物を破砕処理する破砕施設で用いられる。
【0018】
破砕機2は、廃棄物を破砕処理するものであり、この例では、横軸回転式のものにしてあり、上下に入口10と出口11が形成されたケーシング12と、これに横軸廻りに回転可能に設けられた回転軸13と、図略しているが、これに設けられた回転刃と、ケーシング12に固定された固定刃とを備えて居り、回転刃と固定刃に依り廃棄物が衝撃力や剪断力や磨り潰し作用を受けて破砕される様になっている。
破砕機2の入口10には、廃棄物を供給するエプロンコンベア等の供給コンベア14が設けられていると共に、破砕機2の出口11には、破砕された破砕物を排出する振動コンベア等の排出コンベア15が設けられている。
【0019】
ガスタービン発電装置3は、燃焼ガスに依りタービンを回転させてその動力に依り発電するもので、この例では、燃焼ガスに依りタービンを回して回転力を得るガスタービン16と、これに依り回転駆動されて電力を得る発電機17とを備えている。
ガスタービン16は、図略しているが、空気を圧縮する圧縮機と、これからの高圧空気中に燃料を噴射して高圧・高温の燃焼ガスを発生させる燃焼器と、これからの燃焼ガスの膨張に依り回転力が発生されるタービンとを備えている。発電機17は、これに依り発電された電力Bが破砕施設の電気負荷(図示せず)に利用される様にしてある。
【0020】
排ガス供給装置4は、ガスタービン発電装置3からの排ガスAを破砕機2内に供給して破砕機2内の酸素濃度を可燃性ガスの爆発限界外に保持するものであり、この例では、ガスタービン発電装置3のガスタービン16からの排ガスAを破砕機2内に噴射するノズル18と、ガスタービン発電装置3のガスタービン16とノズル18とを接続する導入路19と、導入路19の途中に設けられて排ガスAの供給量を調整する調整弁20と、破砕機2内の酸素濃度を検出する酸素濃度計21と、破砕機2内の可燃ガスを検知する可燃ガス検知器22と、酸素濃度計21からの信号と可燃ガス検知器22からの信号に基づき酸素濃度が設定値以下(14%以下)つまり可燃性ガスの爆発限界外になる様に調整弁20を制御する制御器23とを備えている。
ノズル18は、破砕機2のケーシング12の上位と中位と下位の三箇所に設けられている。導入路19は、上位と中位のノズル18に並列接続されたものと、下位のノズル18に直結されたものの二つにしてある。調整弁20は、電動式にしてあり、各導入路19に介設された二つのものにしてある。酸素濃度計21と可燃ガス検知器22は、破砕機2の入口10付近(上位のノズル18より上方位置)と出口11付近(下位のノズル18より下方位置)の二箇所に設けられている。
【0021】
酸素濃度調整装置5は、ガスタービン発電装置3からの排ガスAの酸素濃度を低下させるものであり、この例では、ガスタービン発電装置3のガスタービン15の直後の導入路19に介設された酸素濃度調整バーナにしてあり、ガスタービン15からの排ガスAの酸素濃度が高い場合には、この排ガスAを追い炊きして酸素濃度を下げる様にしてある。
【0022】
熱交換器6は、ガスタービン発電装置3からの排ガスAを熱交換するものであり、この例では、酸素濃度調整装置5の直後の導入路19に介設された排熱回収ボイラにしてあり、ガスタービン16の排ガスAから熱回収して蒸気又は温水Cを発生させ、その蒸気又は温水Cが破砕施設の蒸気又は温水負荷(図示せず)に利用される様にしてある。
【0023】
シール装置7は、破砕機2の入口10側と出口11側に配されてガスの漏洩を防ぐものであり、この例では、供給コンベア12の途中と排出コンベア13の途中に設けられて居り、廃棄物や破砕物の通過を許容すると共に排ガスAや可燃性ガスの漏洩を防ぐ複数のノレン24(供給コンベア12には三つ、排出コンベア13には二つ)を列置して構成されている。ノレン24は、合成樹脂やゴム等の可撓性部材に依り作製されている。
而して、シール装置7で仕切られた供給コンベア12の上流側と排出コンベア13の下流側は、導路25を介して排気装置26に連通されて居り、排気装置26に依り排気される。
【0024】
廃棄物供給停止装置8は、酸素濃度が設定値より越えた際に破砕機2への廃棄物の供給を停止するものであり、この例では、供給コンベア12を駆動するモータ27と、破砕機2内の酸素濃度を検出する酸素濃度計21と、破砕機2内の可燃ガスを検知する可燃ガス検知器22と、酸素濃度計21からの信号と可燃ガス検知器22からの信号に基づき酸素濃度が設定値以上(14%以上)つまり可燃性ガスの爆発限界内になった際には供給コンベア12のモータ27を停止制御する制御器23とを備えている。酸素濃度計21と可燃ガス検知器22と制御器23は、前記排ガス供給装置4を構成するものを利用している。
【0025】
排ガス循環装置9は、破砕機2の入口10側から出口11側へ排ガスAを循環させるものであり、この例では、破砕機2の入口10側(上部)と出口11側(下部)とを連通する連通路28と、連通路28の途中に設けられて破砕機2の入口10側から出口11側へ排ガスAを送給する送風機29とを備えている。
【0026】
次に、この様な構成に基づいてその作用を述解する。
廃棄物は、供給コンベア14に依り破砕機2の入口10から供給され、破砕機2の回転刃と固定刃に依り衝撃力や剪断力や磨り潰し作用を受けて破砕される。破砕された破砕物は、破砕機2の出口11を経て排出コンベア15に依り排出される。
【0027】
ガスタービン発電装置3のガスタービン16からの排ガスAは、排ガス供給装置4の導入路19に依り導かれて酸素濃度調整装置5に依り酸素濃度が低下されると共に、熱交換器6に依り熱交換された後、調整弁20を介してノズル18から破砕機2内に吹き込まれる。この時、調整弁20は、酸素濃度計21からの信号と可燃ガス検知器22からの信号に基づき酸素濃度が設定値以下(14%以下)になる様に制御器23に依り制御される。この為、破砕機2内の酸素濃度は、可燃性ガスの爆発限界外に保持されて爆発が抑制される。
ガスタービン発電装置3の発電機17に依り発電された電力は、破砕施設内での必要電力に利用される。
排ガスAを供給するガスタービン発電装置3は、破砕機2の防爆に対する排ガスAだけでなく電力Bも発電するので、破砕施設としては、トータル的なイニシャルコストとランニングコストの低減を図る事ができると共に、省エネルギ効果を充分に発揮できる。
【0028】
熱交換器6に依りガスタービン発電装置3のガスタービン16からの排ガスAを熱交換する事ができるので、排ガスAの熱を破砕施設内で利用する事ができる。その結果、破砕施設に於ける省エネルギ効果をより一層高める事ができる。
シール装置7に依り破砕機2内からのガスの漏洩を防ぐ事ができるので、破砕機2内の酸素濃度を可燃ガスの爆発限度外に容易に保持する事ができる。
廃棄物供給停止装置8に依り酸素濃度が設定値より越えた際には破砕機2への廃棄物の供給を停止する事ができるので、それ以上の可燃ガスの増加を防止でき、爆発を未然に防止できる。
排ガス循環装置9に依り破砕機2内の下部から上部への気流特性を利用して排ガスAを循環させる事ができるので、排ガスAの供給量を低減できる。
【0029】
尚、破砕機2は、先の例では、横軸回転式であったが、これに限らず、例えば縦軸回転式等でも良い。
排ガス供給装置4は、酸素濃度計21と可燃ガス検知器22とを用いたが、これに限らず、例えば可燃ガス検知器22を割愛しても良い。
【0030】
【発明の効果】
以上、既述した如く、本発明に依れば、次の様な優れた効果を奏する事ができる。
(1) 廃棄物を破砕処理する破砕機と、燃焼ガスに依りタービンを回転させてその動力に依り発電するガスタービン発電装置と、ガスタービン発電装置からの排ガスを破砕機内に供給して破砕機内の酸素濃度を可燃性ガスの爆発限界外に保持する排ガス供給装置とで構成し、とりわけガスタービン発電装置を設けてこれからの排ガスだけでなく電力も利用できる様にしたので、トータル的なイニシャルコストとランニングコストの低減を図る事ができると共に、省エネルギ効果を充分に発揮できる。
【図面の簡単な説明】
【図1】本発明の破砕機防爆システムを示す概要図。
【符号の説明】
1…破砕機防爆システム、2…破砕機、3…ガスタービン発電装置、4…排ガス供給装置、5…酸素濃度調整装置、6…熱交換器、7…シール装置、8…廃棄物供給停止装置、9…排ガス循環装置、10…入口、11…出口、12…ケーシング、13…回転軸、14…供給コンベア、15…排出コンベア、16…ガスタービン、17…発電機、18…ノズル、19…導入路、20…調整弁、21…酸素濃度計、22…可燃ガス検知器、23…制御器、24…ノレン、25…導路、26…排気装置、27…モータ、28…連通路、29…送風機、A…排ガス、B…電力、C…蒸気又は温水。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an improvement of a crusher explosion-proof system used, for example, in a crushing facility for crushing waste.
[0002]
[Prior art]
Conventionally, as this type of crusher explosion-proof system, for example, Japanese Utility Model Laid-Open No. 53-132011, Japanese Patent Laid-Open No. 54-108062, Japanese Utility Model Laid-Open No. 56-34554 (Japanese Utility Model Publication No. 58-8340), Japanese Patent Application Laid-Open No. Sho 56- No. 89898 (JP-B-58-13220), JP-A-58-81451, JP-A-59-130544 (JP-B-2-33421), JP-A-60-94154 (JP-B-5-39665) No. 63-152645 (No. 3-56258), No. 3-1-15433, No. 4-87645, No. 5-7793, No. 6-72639, etc. It has been known.
[0003]
Thus, in the conventional type, non-oxygen gas such as air (diluted gas), water vapor, water, inert gas, and combustion exhaust gas containing steam is blown into the crusher, and the oxygen concentration in the crusher is reduced by the explosion of the combustible gas. It is intended to keep out of limits and prevent explosions.
[0004]
[Problems to be solved by the invention]
However, in any of the conventional devices, the supply source for supplying the non-oxygen gas can only generate the non-oxygen gas, and is dedicated to the so-called crusher explosion prevention.
For this reason, the conventional one has high total initial cost and running cost, and has not been able to exhibit the energy saving effect.
[0005]
The present invention was devised in view of the above-mentioned problems, and was devised to solve this problem. The problem is that the total initial cost and running cost are reduced and the energy saving effect is sufficient. The purpose is to provide a crusher explosion-proof system that can be used in the future.
[0006]
[Means for Solving the Problems]
The crusher explosion-proof system of the present invention basically includes a crusher that crushes waste, a gas turbine power generator that rotates a turbine by combustion gas and generates power by using the power, and a gas turbine power generator. The exhaust gas supply device for supplying the exhaust gas in the crusher to keep the oxygen concentration in the crusher outside the explosive limit of the combustible gas is characteristic.
[0007]
The exhaust gas from the gas turbine power generator is blown into the crusher by the exhaust gas supply device. At this time, since the oxygen concentration in the crusher is kept outside the explosion limit of the combustible gas by the exhaust gas supply device, the explosion is suppressed.
The electric power generated by the gas turbine power generator is used for the necessary power in the crushing facility.
The gas turbine power generator that supplies exhaust gas generates not only exhaust gas for explosion proofing of the crusher but also electric power, so the crushing facility can reduce total initial cost and running cost, and also save energy. Can be fully demonstrated.
[0008]
It is preferable to provide an oxygen concentration adjusting device that reduces the oxygen concentration of the exhaust gas from the gas turbine power generator. In this way, even when the oxygen concentration of the exhaust gas from the gas turbine power generator is high, it can be reduced, and the oxygen concentration in the crusher can be easily maintained outside the explosive limit of the combustible gas.
[0009]
It is preferable to provide a heat exchanger for exchanging heat from the exhaust gas from the gas turbine power generator. In this way, the heat of the exhaust gas from the gas turbine power generator can be used in the crushing facility, and the energy saving effect in the crushing facility can be further enhanced.
[0010]
It is preferable to provide a sealing device disposed on the inlet side and the outlet side of the crusher to prevent gas leakage. In this way, the oxygen concentration in the crusher can be easily kept outside the explosion limit of the combustible gas.
[0011]
It is preferable to provide a waste supply stop device that stops the supply of waste to the crusher when the oxygen concentration exceeds a set value. In this way, further increase in combustible gas can be prevented and explosion can be prevented.
[0012]
It is preferable to provide an exhaust gas circulation device for circulating exhaust gas from the inlet side to the outlet side of the crusher. If it does in this way, exhaust gas can be circulated using the airflow characteristic from the lower part to the upper part in a crusher, and the supply amount of exhaust gas can be reduced.
[0013]
The exhaust gas supply device is provided in the middle of the introduction path for connecting the gas turbine power generation device and the nozzle to inject the exhaust gas from the gas turbine power generation device into the crusher, and adjusts the supply amount of the exhaust gas. The oxygen concentration is determined based on the control valve, the oxygen concentration meter that detects the oxygen concentration in the crusher, the combustible gas detector that detects the combustible gas in the crusher, the signal from the oxygen concentration meter and the signal from the combustible gas detector. It is preferable to include a controller that controls the regulating valve so as to be equal to or lower than the set value. In this way, the exhaust gas from the gas turbine power generator can be efficiently supplied into the crusher.
[0014]
The waste supply stop device includes a supply conveyor for supplying waste, an oxygen concentration meter for detecting oxygen concentration in the crusher, a combustible gas detector for detecting combustible gas in the crusher, and a signal from the oxygen concentration meter. It is preferable to include a controller for stopping and controlling the supply conveyor when the oxygen concentration becomes a set value or more based on a signal from the combustible gas detector. In this way, since a part of the configuration of the exhaust gas supply device can be used, the structure can be simplified and the cost can be reduced.
[0015]
The exhaust gas circulation device includes a communication path that connects the inlet side and the outlet side of the crusher, and a blower that is provided in the middle of the communication path and that supplies exhaust gas from the inlet side to the outlet side of the crusher. Is preferred. In this way, the exhaust gas can be circulated efficiently with a simple configuration.
[0016]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic diagram showing a crusher explosion-proof system according to the present invention.
[0017]
The crusher explosion-proof system 1 includes a crusher 2, a gas turbine power generation device 3, an exhaust gas supply device 4, an oxygen concentration adjustment device 5, a heat exchanger 6, a seal device 7, a waste supply stop device 8, and an exhaust gas circulation device 9. Its main part is configured and used in crushing facilities that crush waste.
[0018]
The crusher 2 crushes waste. In this example, the crusher 2 is of a horizontal axis rotating type, and a casing 12 having an inlet 10 and an outlet 11 formed on the top and bottom, and a casing 12 around the axis. The rotary shaft 13 is provided so as to be rotatable, and although not shown in the drawing, the rotary shaft 13 is provided with a rotary blade provided on the rotary shaft 13 and a fixed blade fixed to the casing 12. It is designed to be crushed by impact, shearing force and grinding action.
The inlet 10 of the crusher 2 is provided with a supply conveyor 14 such as an apron conveyor that supplies waste, and the outlet 11 of the crusher 2 discharges a vibrating conveyor or the like that discharges the crushed crushed material. A conveyor 15 is provided.
[0019]
The gas turbine power generation device 3 rotates a turbine according to combustion gas and generates power according to its power. In this example, the gas turbine 16 that rotates by the combustion gas to obtain a rotational force, and rotates according to the gas turbine 16. And a generator 17 that is driven to obtain electric power.
Although not shown, the gas turbine 16 is used for a compressor that compresses air, a combustor that injects fuel into high-pressure air from now on to generate high-pressure and high-temperature combustion gas, and expansion of the combustion gas from now on. And a turbine in which a rotational force is generated. The generator 17 is configured such that the electric power B generated thereby is used for an electric load (not shown) of the crushing facility.
[0020]
The exhaust gas supply device 4 supplies the exhaust gas A from the gas turbine power generation device 3 into the crusher 2 and keeps the oxygen concentration in the crusher 2 outside the explosion limit of the combustible gas. In this example, A nozzle 18 that injects the exhaust gas A from the gas turbine 16 of the gas turbine power generation device 3 into the crusher 2, an introduction path 19 that connects the gas turbine 16 and the nozzle 18 of the gas turbine power generation apparatus 3, An adjustment valve 20 provided in the middle for adjusting the supply amount of the exhaust gas A, an oxygen concentration meter 21 for detecting the oxygen concentration in the crusher 2, and a combustible gas detector 22 for detecting the combustible gas in the crusher 2. Based on the signal from the oxygen concentration meter 21 and the signal from the combustible gas detector 22, the controller that controls the regulating valve 20 so that the oxygen concentration is less than the set value (14% or less), that is, outside the explosive limit of the combustible gas With 23 That.
The nozzles 18 are provided at three locations, upper, middle and lower, of the casing 12 of the crusher 2. There are two introduction paths 19, one that is connected in parallel to the upper and middle nozzles 18 and one that is directly connected to the lower nozzle 18. The regulating valve 20 is an electric type, and two valves are interposed in each introduction path 19. The oxygen concentration meter 21 and the combustible gas detector 22 are provided at two locations near the inlet 10 of the crusher 2 (position above the upper nozzle 18) and near the outlet 11 (position below the lower nozzle 18).
[0021]
The oxygen concentration adjusting device 5 reduces the oxygen concentration of the exhaust gas A from the gas turbine power generation device 3. In this example, the oxygen concentration adjustment device 5 is interposed in the introduction path 19 immediately after the gas turbine 15 of the gas turbine power generation device 3. When the oxygen concentration adjustment burner is used, and the oxygen concentration of the exhaust gas A from the gas turbine 15 is high, the exhaust gas A is cooked to reduce the oxygen concentration.
[0022]
The heat exchanger 6 exchanges heat of the exhaust gas A from the gas turbine power generation device 3. In this example, the heat exchanger 6 is a waste heat recovery boiler interposed in the introduction path 19 immediately after the oxygen concentration adjusting device 5. Then, heat is recovered from the exhaust gas A of the gas turbine 16 to generate steam or hot water C, and the steam or hot water C is used for steam or hot water load (not shown) of the crushing facility.
[0023]
The sealing device 7 is arranged on the inlet 10 side and the outlet 11 side of the crusher 2 to prevent gas leakage. In this example, the sealing device 7 is provided in the middle of the supply conveyor 12 and in the middle of the discharge conveyor 13. A plurality of norens 24 (three for the supply conveyor 12 and two for the discharge conveyor 13) are arranged in a row to allow passage of waste and crushed materials and prevent leakage of the exhaust gas A and the combustible gas. Yes. Nolen 24 is made of a flexible member such as synthetic resin or rubber.
Thus, the upstream side of the supply conveyor 12 partitioned by the sealing device 7 and the downstream side of the discharge conveyor 13 are communicated with the exhaust device 26 via the conduit 25 and are exhausted by the exhaust device 26.
[0024]
The waste supply stop device 8 stops the supply of waste to the crusher 2 when the oxygen concentration exceeds a set value. In this example, the motor 27 that drives the supply conveyor 12 and the crusher The oxygen concentration meter 21 for detecting the oxygen concentration in the gas 2, the combustible gas detector 22 for detecting the combustible gas in the crusher 2, the signal from the oxygen concentration meter 21 and the signal from the combustible gas detector 22 A controller 23 is provided for stopping and controlling the motor 27 of the supply conveyor 12 when the concentration exceeds the set value (14% or more), that is, within the explosion limit of the combustible gas. The oxygen concentration meter 21, the combustible gas detector 22, and the controller 23 use what constitutes the exhaust gas supply device 4.
[0025]
The exhaust gas circulation device 9 circulates the exhaust gas A from the inlet 10 side to the outlet 11 side of the crusher 2, and in this example, the inlet 10 side (upper part) and the outlet 11 side (lower part) of the crusher 2 are connected. A communication path 28 that communicates with each other and a blower 29 that is provided in the middle of the communication path 28 and that supplies exhaust gas A from the inlet 10 side to the outlet 11 side of the crusher 2 are provided.
[0026]
Next, the operation will be described based on such a configuration.
The waste is supplied from the inlet 10 of the crusher 2 by the supply conveyor 14 and is crushed by the impact force, shearing force and grinding action by the rotating blade and the fixed blade of the crusher 2. The crushed crushed material is discharged by the discharge conveyor 15 through the outlet 11 of the crusher 2.
[0027]
The exhaust gas A from the gas turbine 16 of the gas turbine power generation device 3 is guided by the introduction path 19 of the exhaust gas supply device 4, the oxygen concentration is lowered by the oxygen concentration adjusting device 5, and the heat is exchanged by the heat exchanger 6. After the replacement, it is blown into the crusher 2 from the nozzle 18 through the regulating valve 20. At this time, the regulating valve 20 is controlled by the controller 23 so that the oxygen concentration becomes a set value or less (14% or less) based on the signal from the oximeter 21 and the signal from the combustible gas detector 22. For this reason, the oxygen concentration in the crusher 2 is kept outside the explosion limit of combustible gas, and explosion is suppressed.
The electric power generated by the generator 17 of the gas turbine power generation device 3 is used as necessary electric power in the crushing facility.
Since the gas turbine power generation device 3 that supplies the exhaust gas A generates not only the exhaust gas A but also the electric power B for the explosion prevention of the crusher 2, the crushing facility can reduce the total initial cost and the running cost. At the same time, the energy saving effect can be fully exhibited.
[0028]
Since the exhaust gas A from the gas turbine 16 of the gas turbine power generation device 3 can be heat-exchanged by the heat exchanger 6, the heat of the exhaust gas A can be used in the crushing facility. As a result, the energy saving effect in the crushing facility can be further enhanced.
Since the gas leakage from the crusher 2 can be prevented by the sealing device 7, the oxygen concentration in the crusher 2 can be easily maintained outside the explosion limit of the combustible gas.
Since the waste supply to the crusher 2 can be stopped when the oxygen concentration exceeds the set value due to the waste supply stop device 8, further increase in combustible gas can be prevented, and an explosion has not occurred. Can be prevented.
Since the exhaust gas A can be circulated by utilizing the air flow characteristics from the lower part to the upper part in the crusher 2 by the exhaust gas circulation device 9, the supply amount of the exhaust gas A can be reduced.
[0029]
In addition, although the crusher 2 was a horizontal axis rotation type in the previous example, it is not restricted to this, For example, a vertical axis rotation type etc. may be sufficient.
Although the exhaust gas supply device 4 uses the oxygen concentration meter 21 and the combustible gas detector 22, the present invention is not limited thereto, and for example, the combustible gas detector 22 may be omitted.
[0030]
【The invention's effect】
As described above, according to the present invention, the following excellent effects can be obtained.
(1) A crusher that crushes waste, a gas turbine power generator that generates power by rotating the turbine using combustion gas, and supplies exhaust gas from the gas turbine power generator to the crusher. It is composed of an exhaust gas supply device that keeps the oxygen concentration outside the explosive limit of flammable gas, and in particular, a gas turbine power generator is installed so that not only exhaust gas in the future but also electric power can be used, so the total initial cost The running cost can be reduced, and the energy saving effect can be fully demonstrated.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing a crusher explosion-proof system according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Crusher explosion-proof system, 2 ... Crusher, 3 ... Gas turbine power generation device, 4 ... Exhaust gas supply device, 5 ... Oxygen concentration adjustment device, 6 ... Heat exchanger, 7 ... Sealing device, 8 ... Waste supply stop device , 9 ... exhaust gas circulation device, 10 ... inlet, 11 ... outlet, 12 ... casing, 13 ... rotating shaft, 14 ... supply conveyor, 15 ... discharge conveyor, 16 ... gas turbine, 17 ... generator, 18 ... nozzle, 19 ... Introducing path, 20 ... regulating valve, 21 ... oxygen concentration meter, 22 ... combustible gas detector, 23 ... controller, 24 ... noren, 25 ... conduit, 26 ... exhaust device, 27 ... motor, 28 ... communication path, 29 ... blower, A ... exhaust gas, B ... electric power, C ... steam or hot water.

Claims (8)

廃棄物を破砕処理する破砕機と、燃焼ガスに依りタービンを回転させてその動力に依り発電するガスタービン発電装置と、ガスタービン発電装置からの排ガスを破砕機内に供給して破砕機内の酸素濃度を可燃性ガスの爆発限界外に保持する排ガス供給装置と、から構成し、酸素濃度が設定値より越えた際に破砕機への廃棄物の供給を停止する廃棄物供給停止装置を備えている事を特徴とする破砕機防爆システム。A crusher that crushes waste, a gas turbine power generator that generates power by rotating the turbine according to combustion gas, and an exhaust gas from the gas turbine power generator is supplied into the crusher and the oxygen concentration in the crusher And a waste gas supply device that holds the waste gas outside the explosive limit of the combustible gas, and has a waste supply stop device that stops the supply of waste to the crusher when the oxygen concentration exceeds a set value Crusher explosion-proof system characterized by things. ガスタービン発電装置からの排ガスの酸素濃度を低下させる酸素濃度調整装置を備えている請求項1に記載の破砕機防爆システム。  The crusher explosion-proof system according to claim 1, further comprising an oxygen concentration adjusting device that reduces an oxygen concentration of exhaust gas from the gas turbine power generation device. ガスタービン発電装置からの排ガスを熱交換する熱交換器を備えている請求項1に記載の破砕機防爆システム。  The crusher explosion-proof system of Claim 1 provided with the heat exchanger which heat-exchanges the waste gas from a gas turbine power generator. 破砕機の入口側と出口側に配されてガスの漏洩を防ぐシール装置を備えている請求項1に記載の破砕機防爆システム。  The crusher explosion-proof system of Claim 1 provided with the sealing device which is distribute | arranged to the inlet side and exit side of a crusher, and prevents the leakage of gas. 破砕機の入口側から出口側へ排ガスを循環させる排ガス循環装置を備えている請求項1に記載の破砕機防爆システム。  The crusher explosion-proof system according to claim 1, further comprising an exhaust gas circulation device that circulates the exhaust gas from the inlet side to the outlet side of the crusher. 排ガス供給装置は、ガスタービン発電装置からの排ガスを破砕機内に噴射するノズルと、ガスタービン発電装置とノズルとを接続する導入路と、導入路の途中に設けられて排ガスの供給量を調整する調整弁と、破砕機内の酸素濃度を検出する酸素濃度計と、破砕機内の可燃ガスを検知する可燃ガス検知器と、酸素濃度計からの信号と可燃ガス検知器からの信号に基づき酸素濃度が設定値以下になる様に調整弁を制御する制御器とを備えている請求項1に記載の破砕機防爆システム。  The exhaust gas supply device is provided in the middle of the introduction path for connecting the gas turbine power generation device and the nozzle, a nozzle for injecting the exhaust gas from the gas turbine power generation device into the crusher, and adjusts the supply amount of the exhaust gas The oxygen concentration is determined based on the regulating valve, the oxygen concentration meter that detects the oxygen concentration in the crusher, the combustible gas detector that detects the combustible gas in the crusher, the signal from the oxygen concentration meter, and the signal from the combustible gas detector. The crusher explosion-proof system according to claim 1, further comprising a controller that controls the adjustment valve so as to be equal to or less than a set value. 廃棄物供給停止装置は、廃棄物を供給する供給コンベアと、破砕機内の酸素濃度を検出する酸素濃度計と、破砕機内の可燃ガスを検知する可燃ガス検知器と、酸素濃度計からの信号と可燃ガス検知器からの信号に基づき酸素濃度が設定値以上になった際には供給コンベアを停止制御する制御器とを備えている請求項1に記載の破砕機防爆システム。  The waste supply stop device includes a supply conveyor that supplies waste, an oxygen concentration meter that detects oxygen concentration in the crusher, a combustible gas detector that detects combustible gas in the crusher, and a signal from the oxygen concentration meter. The crusher explosion-proof system according to claim 1, further comprising a controller for stopping and controlling the supply conveyor when the oxygen concentration exceeds a set value based on a signal from the combustible gas detector. 排ガス循環装置は、破砕機の入口側と出口側とを連通する連通路と、連通路の途中に設けられて破砕機の入口側から出口側へ排ガスを送給する送風機とを備えている請求項に記載の破砕機防爆システム。The exhaust gas circulation device includes a communication path that connects the inlet side and the outlet side of the crusher, and a blower that is provided in the middle of the communication path and that supplies exhaust gas from the inlet side to the outlet side of the crusher. Item 6. The crusher explosion-proof system according to Item 5 .
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