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JP6288841B2 - Water-cooled stoker device for waste incinerator and operation method thereof - Google Patents
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JP6288841B2 - Water-cooled stoker device for waste incinerator and operation method thereof - Google Patents

Water-cooled stoker device for waste incinerator and operation method thereof Download PDF

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JP6288841B2
JP6288841B2 JP2014078325A JP2014078325A JP6288841B2 JP 6288841 B2 JP6288841 B2 JP 6288841B2 JP 2014078325 A JP2014078325 A JP 2014078325A JP 2014078325 A JP2014078325 A JP 2014078325A JP 6288841 B2 JP6288841 B2 JP 6288841B2
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懇 望月
懇 望月
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Takuma Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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    • Y02E20/30Technologies for a more efficient combustion or heat usage

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Description

本発明は、主に都市ごみや産業廃棄物等を焼却処理するごみ焼却炉の水冷式ストーカ装置及びその運転方法の改良に係り、従来から水冷ストーカ内を循環流通する火格子冷却水の冷却に用いられていた冷却塔やベンチレータの代わりに、間接熱交換器と冷水(井水又は雨水)とを使用し、間接熱交換器で火格子冷却水を冷却した後の前記冷水をごみ焼却炉の排ガス排出経路に必ず設置されている排ガス冷却室への噴射水として利用することによって、設備の簡略化や設備費及びランニングコストの削減等を図れるようにしたごみ焼却炉の水冷式ストーカ装置及びその運転方法に関するものである。   The present invention mainly relates to improvements in a water-cooled stoker device for a waste incinerator for incinerating municipal waste and industrial waste, etc. and its operation method, and for cooling grate cooling water conventionally circulating in a water-cooled stoker. Instead of the cooling tower and ventilator used, an indirect heat exchanger and cold water (well water or rainwater) are used, and after cooling the grate cooling water with the indirect heat exchanger, the cold water is used in the waste incinerator. Wastewater incinerator water-cooled stoker device that can simplify equipment and reduce equipment costs and running costs by using it as spray water to an exhaust gas cooling chamber that is always installed in the exhaust gas discharge route, and its It relates to the driving method.

従来、水冷式ストーカ装置としては、例えば、特表平10−504890号公報(特許文献1)や特開2003−4218号公報(特許文献2)に開示された構造のものが知られている。   Conventionally, as a water-cooled stoker device, for example, one having a structure disclosed in Japanese Patent Laid-Open No. 10-504890 (Patent Document 1) or Japanese Patent Application Laid-Open No. 2003-4218 (Patent Document 2) is known.

即ち、前者の水冷式ストーカ装置A′は、図4に示す如く、可動火格子及び固定火格子を交互に並列させて成る水冷式ストーカB′と、水冷式ストーカB′へ火格子冷却水を循環流通させる火格子冷却水循環・冷却機構C′とから構成されている。   That is, as shown in FIG. 4, the former water-cooled stalker apparatus A ′ has a water-cooled stalker B ′ in which a movable grate and a fixed grate are alternately arranged in parallel, and grate cooling water to the water-cooled stalker B ′. It is composed of a grate cooling water circulation / cooling mechanism C ′ that circulates and circulates.

また、火格子冷却水循環・冷却機構C′は、ポンプ40、流量測定装置41、膨張容器42、温度測定装置43、圧力測定装置44、再冷却器45、ベンチレータ46、圧力調整弁47等から構成されており、圧力調整弁47を通して供給された火格子冷却水をポンプ40により水冷式ストーカB′へ循環流通させ、水冷式ストーカB′から流出した火格子冷却水を再冷却器45及びベンチレータ46で冷却するようにしている。   The grate cooling water circulation / cooling mechanism C 'includes a pump 40, a flow rate measuring device 41, an expansion vessel 42, a temperature measuring device 43, a pressure measuring device 44, a recooler 45, a ventilator 46, a pressure regulating valve 47, and the like. The grate cooling water supplied through the pressure regulating valve 47 is circulated and circulated by the pump 40 to the water-cooled stalker B ′, and the grate cooling water flowing out from the water-cooled stalker B ′ is recooled by the recooler 45 and the ventilator 46. I'm trying to cool it down.

しかし、前者の水冷式ストーカ装置A′は、火格子冷却水を再冷却器45及びベンチレータ46で冷却するようにしているため、冷却能力が相対的に低いだけでなく、温度制御の応答性が極めて悪いと云う問題があった。しかも、膨張容器42の内圧をコンプレッサー(図示省略)の運転制御を介して調整することによって、火格子冷却水系の内圧を制御する構成としているため、火格子冷却水循環・冷却機構C′の圧力保持機構構造や運転制御操作が複雑になる等の問題があった。   However, the former water-cooled stoker device A ′ cools the grate cooling water by the recooler 45 and the ventilator 46, so that not only the cooling capacity is relatively low but also the responsiveness of the temperature control. There was a problem of being extremely bad. In addition, since the internal pressure of the grate cooling water system is controlled by adjusting the internal pressure of the expansion vessel 42 through operation control of a compressor (not shown), the pressure of the grate cooling water circulation / cooling mechanism C ′ is maintained. There were problems such as complicated mechanism structure and operation control operation.

一方、後者の水冷式ストーカ装置A′は、図5に示す如く、可動火格子50と固定火格子51とを交互に階段状又は傾斜状に組み合せて成る水冷式ストーカB′と、水冷式ストーカB′へ火格子冷却水W′を循環流通させる火格子冷却水循環・冷却機構C′とから構成されている。   On the other hand, as shown in FIG. 5, the latter water-cooled stalker apparatus A ′ includes a water-cooled stalker B ′ formed by alternately combining a movable grate 50 and a fixed grate 51 in a stepped or inclined manner, and a water-cooled stalker. It comprises a grate cooling water circulation / cooling mechanism C ′ for circulating the grate cooling water W ′ to B ′.

また、火格子冷却水循環・冷却機構C′は、火格子冷却部C1′と火格子冷却水W′の冷却部C2′とから構成されており、両冷却部C1′,C2′は間接型熱交換器52を介して熱的に連結されている。   The grate cooling water circulation / cooling mechanism C ′ is composed of a grate cooling part C1 ′ and a cooling part C2 ′ of the grate cooling water W ′, and both cooling parts C1 ′ and C2 ′ are indirect heat. Thermally connected via the exchanger 52.

即ち、火格子冷却部C1′は、火格子冷却水タンク53、加圧循環ポンプ54、火格子冷却水循環量制御弁55、給水側ヘッダ56、排水側ヘッダ57、間接型熱交換器52の火格子冷却水側熱交換エレメント52a、圧力制御弁58、温度制御器59、温度検出器59a、圧力制御器60及び圧力検出器60a等から構成されており、火格子冷却水タンク53内の火格子冷却水W′を加圧循環ポンプ54により水冷式ストーカB′へ循環流通させるようになっている。   That is, the grate cooling unit C1 ′ includes the grate cooling water tank 53, the pressurization circulation pump 54, the grate cooling water circulation amount control valve 55, the water supply side header 56, the drain side header 57, and the fire of the indirect heat exchanger 52. The grate cooling water side heat exchange element 52 a, the pressure control valve 58, the temperature controller 59, the temperature detector 59 a, the pressure controller 60, the pressure detector 60 a, and the like, and the grate in the grate cooling water tank 53. The cooling water W ′ is circulated and circulated to the water-cooled stalker B ′ by the pressurized circulation pump 54.

一方、火格子冷却水W′の冷却部C2′は、冷水タンク61、冷水循環ポンプ62、冷水循環量制御弁63、間接型熱交換器52の冷水側熱交換エレメント52b、冷却塔64、温度制御器65及び温度検出器65a等から構成されており、冷水タンク61内の冷水Wo′を冷水循環ポンプ62により間接型熱交換器52の冷水側熱交換エレメント52bへ送り、間接型熱交換器52内で火格子冷却水W′を冷却した後の冷水Wo′を冷却塔64で冷却して冷水タンク61に戻すようにしている。   On the other hand, the cooling part C2 ′ of the grate cooling water W ′ includes a cold water tank 61, a cold water circulation pump 62, a cold water circulation amount control valve 63, a cold water side heat exchange element 52b of the indirect heat exchanger 52, a cooling tower 64, a temperature. The chilled water Wo ′ in the chilled water tank 61 is sent to the chilled water side heat exchange element 52b of the indirect heat exchanger 52 by the chilled water circulation pump 62, and is configured by an indirect heat exchanger. The cold water Wo ′ after the grate cooling water W ′ is cooled in 52 is cooled by the cooling tower 64 and returned to the cold water tank 61.

後者の水冷式ストーカ装置A′は、間接型熱交換器52を用いて火格子冷却部C1′と火格子冷却水W′の冷却部C2′とを完全に分割した構成としているため、前者の水冷式ストーカ装置A′の問題を解決することができる。   The latter water-cooled stoker device A ′ has a configuration in which the grate cooling part C1 ′ and the grate cooling water W ′ cooling part C2 ′ are completely divided by using the indirect heat exchanger 52. The problem of the water-cooled stoker device A ′ can be solved.

しかし、後者の水冷式ストーカ装置A′は、火格子冷却水W′の冷却部C2′に冷却塔64を設けているため、設備が複雑になって設備費が増大すると云う問題があった。   However, the latter water-cooled stoker device A ′ has a problem that the equipment becomes complicated and the equipment cost increases because the cooling tower 64 is provided in the cooling part C2 ′ of the grate cooling water W ′.

また、冷却塔64を使用する循環冷却水系では、冷水Wo′を循環利用しているため、蒸発による冷水Wo′の濃縮が生じ、スケール障害、腐食障害、スライム障害が発生し易いので、火格子冷却水W′の冷却部C2′の冷水Wo′に薬剤(腐食防止剤、防スケール剤、防スライム剤)を注入するための注入装置(図示省略)が必要になり、設備費がより増大すると云う問題があった。   Further, in the circulating cooling water system using the cooling tower 64, the cold water Wo ′ is circulated and used, so that the cold water Wo ′ is concentrated by evaporation, and scale failure, corrosion failure, and slime failure are likely to occur. If an injection device (not shown) for injecting chemicals (corrosion inhibitor, anti-scale agent, anti-slime agent) into the cold water Wo ′ of the cooling part C2 ′ of the cooling water W ′ is required, the equipment cost will increase. There was a problem.

更に、火格子冷却水W′の冷却部C2′の冷水Wo′に薬剤を注入するため、ランニングコストも増大すると云う問題があった。   Furthermore, since the chemical | medical agent is inject | poured into the cold water Wo 'of the cooling part C2' of the grate cooling water W ', there existed a problem that a running cost also increased.

加えて、冷却塔64に用いる充填材の材質が一般的にポリ塩化ビニル(PVC)であるため、耐熱の限界が45℃未満であり、また、耐熱仕様でも45℃〜70℃であるので、誤って耐熱以上の水が流入すると、充填材が座屈し、交換する必要が生じる。この場合には、休炉を余儀なくされ、交換費も発生すると云う問題があった。   In addition, since the material of the filler used for the cooling tower 64 is generally polyvinyl chloride (PVC), the heat resistance limit is less than 45 ° C, and the heat resistance specification is 45 ° C to 70 ° C. If water that exceeds heat resistance flows in by mistake, the filler will buckle and need to be replaced. In this case, there was a problem that the furnace was forced to shut down and a replacement cost was incurred.

特表平10−504890号公報Japanese National Patent Publication No. 10-504890 特開2003−4218号公報JP 2003-4218 A

本発明は、このような問題点に鑑みて為されたものであり、その目的は、間接熱交換器と冷水(井水又は雨水)とを使用し、間接熱交換器で火格子冷却水を冷却した後の前記冷水をごみ焼却炉の排ガス排出経路に設置されている排ガス冷却室への噴射水として利用することによって、冷却塔を削減できて薬剤の注入装置及び薬剤が不要となり、設備の簡略化を図れると共に、設備費及びランニングコストの削減等を図れるようにしたごみ焼却炉の水冷式ストーカ装置及びその運転方法を提供することにある。   The present invention has been made in view of such problems, and its purpose is to use an indirect heat exchanger and cold water (well water or rainwater), and to add grate cooling water with the indirect heat exchanger. By using the chilled water after cooling as spray water to the exhaust gas cooling chamber installed in the exhaust gas discharge path of the garbage incinerator, the cooling tower can be reduced, and the chemical injection device and chemical are not required. It is an object of the present invention to provide a water-cooled stoker device for a waste incinerator and a method for operating the same, which can be simplified and can reduce facility costs and running costs.

上記目的を達成するために、本発明の請求項1の発明は、火格子冷却水通路をそれぞれ形成した可動火格子と固定火格子とを階段状又は傾斜状に組み合せて成る水冷式ストーカと、水冷式ストーカへ火格子冷却水を循環流通させつつ冷却する火格子冷却水循環・冷却機構とから構成したごみ焼却炉の水冷式ストーカ装置に於いて、前記火格子冷却水循環・冷却機構は、火格子冷却水を循環流通させる火格子冷却部と火格子冷却部の火格子冷却水を冷水により冷却する火格子冷却水冷却部とを間接熱交換器を介して熱的に連結すると共に、火格子冷却水冷却部の冷水をごみ焼却炉の排ガス排出経路に設置されている排ガス冷却室に水を噴射する水噴射供給装置へ供給する構成とし、前記火格子冷却部は、火格子冷却水を貯留する火格子冷却水タンクと、火格子冷却水の循環ポンプと、火格子冷却水を各可動火格子及び固定火格子の火格子冷却水通路へ供給する給水側ヘッダと、各火格子冷却水通路から火格子冷却水を排水する排水側ヘッダと、排水側ヘッダからの火格子冷却水を冷却する間接熱交換器の火格子冷却水側熱交換エレメントととから成り、また、前記火格子冷却水冷却部は、冷水を貯留する冷水タンクと、冷水の送水ポンプと、間接熱交換器の冷水側熱交換エレメントと、冷水側熱交換エレメントの入口側又は出口側に設けた冷水量調節弁と、間接熱交換器の出口側の火格子冷却水の検出温度により冷水量調節弁を制御する温度制御器とから成ることに特徴がある。   In order to achieve the above object, the invention of claim 1 of the present invention comprises a water-cooled stoker comprising a movable grate and a fixed grate, each having a grate cooling water passage formed in a stepwise or inclined manner, In a water-cooled stoker device for a refuse incinerator configured to circulate and circulate grate cooling water to a water-cooled stoker, the grate cooling water circulation / cooling mechanism is a grate cooling water circulation / cooling mechanism. The grate cooling unit for circulating and circulating the cooling water and the grate cooling water cooling unit for cooling the grate cooling water of the grate cooling unit with cold water are thermally connected via an indirect heat exchanger, and the grate cooling is performed. The water cooling unit is configured to supply cold water to a water injection supply device that injects water into an exhaust gas cooling chamber installed in an exhaust gas discharge path of a waste incinerator, and the grate cooling unit stores grate cooling water. Grate cooling water A grate cooling water circulation pump, a water supply side header for supplying grate cooling water to the grate cooling water passages of each movable grate and fixed grate, and grate cooling water from each grate cooling water passage And a grate cooling water side heat exchange element of an indirect heat exchanger that cools grate cooling water from the drain side header. A chilled water tank, a chilled water feed pump, a chilled water side heat exchange element of the indirect heat exchanger, a chilled water amount adjusting valve provided on the inlet side or the outlet side of the chilled water side heat exchange element, and an indirect heat exchanger It is characterized by comprising a temperature controller that controls the chilled water amount adjusting valve according to the detected temperature of the grate cooling water on the outlet side.

本発明の請求項2の発明は、請求項1に記載の発明に於いて、火格子冷却水循環・冷却機構は、熱利用設備及び第2間接熱交換器を備えており、前記熱利用設備と火格子冷却部の火格子冷却水系とを、間接熱交換器と排水側ヘッダとの間に設けた第2間接熱交換器を介して熱的に連結したことに特徴がある。   The invention according to claim 2 of the present invention is the invention according to claim 1, wherein the grate cooling water circulation / cooling mechanism includes a heat utilization facility and a second indirect heat exchanger, The grate cooling water system of the grate cooling unit is characterized in that it is thermally connected via a second indirect heat exchanger provided between the indirect heat exchanger and the drainage side header.

本発明の請求項3の発明は、火格子冷却水通路をそれぞれ形成した可動火格子と固定火格子とを階段状又は傾斜状に組み合せて成る水冷式ストーカと、水冷式ストーカへ火格子冷却水を循環流通させつつ冷却する火格子冷却水循環・冷却機構とから構成したごみ焼却炉の水冷式ストーカ装置に於いて、前記火格子冷却水循環・冷却機構は、火格子冷却水を循環流通させる火格子冷却部と火格子冷却部の火格子冷却水を冷水により冷却する火格子冷却水冷却部とを間接熱交換器を介して熱的に連結すると共に、火格子冷却水冷却部の冷水をごみ焼却炉の排ガス排出経路に設置されている排ガス冷却室に水を噴射する水噴射供給装置へ供給する構成とし、前記火格子冷却部は、火格子冷却水を貯留する火格子冷却水タンクと、火格子冷却水の循環ポンプと、火格子冷却水を各可動火格子及び固定火格子の火格子冷却水通路へ供給する給水側ヘッダと、各火格子冷却水通路から火格子冷却水を排水する排水側ヘッダと、排水側ヘッダからの火格子冷却水を冷却する間接熱交換器の火格子冷却水側熱交換エレメントとから成り、また、前記火格子冷却水冷却部は、冷水を貯留する冷水タンクと、冷水の送水ポンプと、間接熱交換器の冷水側熱交換エレメントと、冷水側熱交換エレメントの入口側に設けた冷水量調節弁と、排ガス冷却室への噴射水量に応じて冷水量調節弁を制御する流量制御器と、冷水側熱交換エレメントの出口側又は入口側に設けられ、間接熱交換器への冷水の流通制御を行う三方弁と、間接熱交換器の出口側の火格子冷却水の検出温度により三方弁を制御する温度制御器とから成ることに特徴がある。   According to the third aspect of the present invention, there is provided a water-cooled stoker in which a movable grate and a fixed grate each having a grate cooling water passage are combined in a stepped or inclined manner, and a grate cooling water to the water-cooled stoker. In a water-cooled stoker device for a waste incinerator configured to circulate and circulate a grate cooling water circulation / cooling mechanism, the grate cooling water circulation / cooling mechanism is a grate for circulating grate cooling water. The cooling unit and the grate cooling water cooling unit that cools the grate cooling water of the grate cooling unit with cold water are thermally connected via an indirect heat exchanger, and the cold water of the grate cooling water cooling unit is incinerated with garbage. It is configured to supply to a water injection supply device that injects water into an exhaust gas cooling chamber installed in the exhaust gas discharge path of the furnace, and the grate cooling unit includes a grate cooling water tank that stores grate cooling water, Circulation cooling water circulation A water supply side header that supplies grate cooling water to the grate cooling water passages of each movable grate and fixed grate, a drain side header that drains the grate cooling water from each grate cooling water passage, A grate cooling water side heat exchange element of an indirect heat exchanger that cools grate cooling water from the side header, and the grate cooling water cooling unit includes a cold water tank that stores cold water, and water supply of the cold water Flow rate that controls the chilled water amount control valve according to the amount of water injected into the pump, the chilled water side heat exchange element of the indirect heat exchanger, the chilled water amount control valve provided on the inlet side of the chilled water side heat exchange element, and the exhaust gas cooling chamber A controller, a three-way valve that is provided on the outlet side or inlet side of the chilled water side heat exchange element and controls the flow of chilled water to the indirect heat exchanger, and a detected temperature of grate cooling water on the outlet side of the indirect heat exchanger Temperature controller that controls the three-way valve by It is characterized by consisting of.

本発明の請求項4の発明は、請求項1に記載のごみ焼却炉の水冷式ストーカ装置に於いて、火格子冷却水タンク内の火格子冷却水を井水又は上水とし、井水又は上水を火格子冷却水循環ポンプにより圧送して水冷式ストーカに通した後、間接熱交換器により冷却して火格子冷却水タンクに戻し、また、冷却タンク内の冷水を井水又は雨水とし、井水又は雨水を冷水ポンプにより間接熱交換器に圧送してここで火格子冷却水の冷却に使用した後、排ガス冷却室の水噴射供給装置へ供給して排ガス冷却室の噴射水として利用するようにしたことに特徴がある。   According to a fourth aspect of the present invention, in the water-cooled stoker device for a waste incinerator according to the first aspect, the grate cooling water in the grate cooling water tank is well water or clean water, After the water is pumped by a grate cooling water circulation pump and passed through a water-cooled stoker, it is cooled by an indirect heat exchanger and returned to the grate cooling water tank, and the cold water in the cooling tank is made into well water or rain water, Well water or rainwater is pumped to an indirect heat exchanger by a chilled water pump and used for cooling grate cooling water, and then supplied to a water jet supply device in an exhaust gas cooling chamber to be used as jet water in the exhaust gas cooling chamber. It is characterized by doing so.

本発明の請求項5の発明は、請求項4に記載の発明に於いて、間接熱交換器に入る前の火格子冷却水を第2間接熱交換器に通してここで熱利用設備からの冷却水又は冷却空気により冷却するようにしたことに特徴がある。   The invention according to claim 5 of the present invention is the invention according to claim 4, wherein the grate cooling water before entering the indirect heat exchanger is passed through the second indirect heat exchanger, where It is characterized by being cooled by cooling water or cooling air.

本発明の請求項6の発明は、請求項3に記載のごみ焼却炉の水冷式ストーカ装置に於いて、火格子冷却水タンク内の火格子冷却水を井水又は上水とし、井水又は上水を火格子冷却水循環ポンプにより圧送して水冷式ストーカに通した後、間接熱交換器により冷却して火格子冷却水タンクに戻し、また、冷却タンク内の冷水を雨水とし、この雨水を送水ポンプにより間接熱交換器に圧送してここで火格子冷却水の冷却に使用した後、当該雨水を排ガス冷却室の水噴射供給装置へ供給して排ガス冷却室の噴射水として利用し、更に、排ガス冷却室への水噴射流量に応じて冷水量調節弁を制御して雨水の量を調整すると共に、間接熱交換器の出口側の火格子冷却水の検出温度に基づいて三方弁を制御して間接熱交換器への雨水の流通制御を行うようにしたことに特徴がある。   The invention according to claim 6 of the present invention is the water-cooled stoker device for a refuse incinerator according to claim 3, wherein the grate cooling water in the grate cooling water tank is well water or clean water, The water is pumped by a grate cooling water circulation pump and passed through a water-cooled stalker, then cooled by an indirect heat exchanger and returned to the grate cooling water tank, and the cooling water in the cooling tank is used as rainwater. After being pumped to the indirect heat exchanger by a water pump and used for cooling the grate cooling water, the rainwater is supplied to the water jet supply device of the exhaust gas cooling chamber and used as the jet water of the exhaust gas cooling chamber. Controls the amount of rainwater by controlling the cold water amount control valve according to the water injection flow rate to the exhaust gas cooling chamber, and controls the three-way valve based on the detected temperature of the grate cooling water on the outlet side of the indirect heat exchanger To control the flow of rainwater to the indirect heat exchanger It is characterized in the that.

本発明は、水冷式ストーカ装置へ火格子冷却水を循環流通させる火格子冷却部と火格子冷却部の火格子冷却水を冷水により冷却する火格子冷却水冷却部とを間接熱交換器を介して熱的に連結し、火格子冷却水冷却部の冷却水を間接熱交換器で火格子冷却水の冷却に使用した後、排ガス冷却室の水噴射供給装置へ供給して排ガス冷却室の噴射水として利用するようにしているため、上述した従来技術のように火格子冷却水の冷却に使用した冷水を冷却塔で冷却する必要もなく、火格子冷却水の冷却部の冷却塔を削減することができ、設備の簡略化を図れると共に、設備費の削減を図れる。
また、本発明は、冷却塔を削減できたことによって、火格子冷却水の冷却部の冷水に薬剤を注入する必要がなくなり、薬剤の注入装置が不要になって設備費をより削減することができると共に、薬剤も不要となってランニングコストの削減も図れる。
更に、本発明は、冷却塔を使用しないため、冷却塔に用いる充填材の座屈のリスクを回避することができる。
そのうえ、本発明は、間接熱交換器に入る前の火格子冷却水を第2間接熱交換器に通してここで熱利用設備からの冷却水、冷却空気、熱媒油又は低沸点媒体により冷却するようにしているため、熱エネルギーの有効利用を図れる。
加えて、本発明は、冷水として井水又は雨水を使用しているため、冷水に上水を使用した従来技術に比較してコスト削減を図れる。
The present invention relates to a grate cooling unit that circulates and distributes grate cooling water to a water-cooled stoker device and a grate cooling water cooling unit that cools grate cooling water of the grate cooling unit with cold water via an indirect heat exchanger. The cooling water in the grate cooling water cooling section is used to cool the grate cooling water with an indirect heat exchanger, and then supplied to the water jet supply device in the exhaust gas cooling chamber to inject the exhaust gas cooling chamber. Since it is used as water, it is not necessary to cool the cooling water used for cooling the grate cooling water with the cooling tower as in the prior art described above, and the number of cooling towers in the cooling part of the grate cooling water is reduced. Therefore, the equipment can be simplified and the equipment cost can be reduced.
In addition, since the present invention has reduced the number of cooling towers, it is no longer necessary to inject a medicine into the cold water of the grate cooling water cooling unit, and the equipment for injecting the medicine becomes unnecessary, thereby further reducing the equipment cost. In addition, it is possible to reduce running costs by eliminating the need for chemicals.
Furthermore, since the present invention does not use a cooling tower, the risk of buckling of the filler used in the cooling tower can be avoided.
Moreover, the present invention passes the grate cooling water before entering the indirect heat exchanger through the second indirect heat exchanger where it is cooled by cooling water from the heat utilization equipment, cooling air, heat transfer oil or low boiling point medium. Therefore, effective use of thermal energy can be achieved.
In addition, since well water or rainwater is used as cold water, the present invention can achieve cost reduction as compared with the prior art using clean water as cold water.

本発明の第1の実施形態に係るごみ焼却炉の水冷式ストーカ装置の概略系統図である。1 is a schematic system diagram of a water-cooled stoker device for a waste incinerator according to a first embodiment of the present invention. 本発明の第2の実施形態に係るごみ焼却炉の水冷式ストーカ装置の概略系統図である。It is a schematic system diagram of the water-cooled stoker device for the waste incinerator according to the second embodiment of the present invention. 本発明の第3の実施形態に係るごみ焼却炉の水冷式ストーカ装置の概略系統図である。It is a schematic system diagram of the water-cooled stoker device for the refuse incinerator according to the third embodiment of the present invention. 従来の水冷式ストーカ装置の一例を示す概略系統図である。It is a schematic system diagram which shows an example of the conventional water-cooled stoker device. 同じく従来の水冷式ストーカ装置の他の例を示す概略系統図である。It is a schematic system diagram which similarly shows the other example of the conventional water-cooled stoker apparatus.

以下、本発明の実施形態を図面に基づいて詳細に説明する。
図1は本発明の第1の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aの概略系統図を示し、当該ごみ焼却炉Dの水冷式ストーカ装置Aは、火格子冷却水通路(図示省略)をそれぞれ形成した可動火格子1と固定火格子2とを階段状又は傾斜状に組み合せて成る水冷式ストーカBと、水冷式ストーカBへ火格子冷却水Wを循環流通させつつ冷却する火格子冷却水循環・冷却機構Cとから構成されている。
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 shows a schematic system diagram of a water-cooled stoker device A of a waste incinerator D according to a first embodiment of the present invention. The water-cooled stoker device A of the waste incinerator D has a grate cooling water passage (illustrated). A water-cooled stoker B formed by combining the movable grate 1 and the fixed grate 2 formed in a stepped or inclined manner, and a fire that cools the grate cooling water W through the water-cooled stoker B in a circulating manner. It comprises a lattice cooling water circulation / cooling mechanism C.

即ち、前記水冷式ストーカBは、冷却水通路(図示省略)を形成した複数基の水冷式火格子本体3を並列状に組み合せ、隣接する水冷式火格子本体3の冷却水通路同士を連結して連通状の火格子冷却水通路(図示省略)を形成して成る可動火格子1と固定火格子2とを複数基交互に階段状又は傾斜状に組み合せることにより構成されており、各可動火格子1の作動により都市ごみ等の廃棄物が矢印方向へ移動して行くようになっている。
この水冷式ストーカBは、従来公知のものと同様構造に構成されているため、ここではその詳細な説明を省略する。
尚、水冷式ストーカBの形式及び構造等は、火格子冷却水通路を備えておれば、如何なるものであっても良い。
That is, the water-cooled stoker B combines a plurality of water-cooled grate bodies 3 having cooling water passages (not shown) in parallel and connects the cooling water passages of adjacent water-cooled grate bodies 3 together. Are constructed by combining a plurality of movable grate 1 and fixed grate 2 formed by forming a continuous grate cooling water passage (not shown) in a staircase shape or an inclined shape. Waste such as municipal waste moves in the direction of the arrow by the operation of the grate 1.
Since this water-cooled stalker B has the same structure as a conventionally known one, detailed description thereof is omitted here.
The type and structure of the water-cooled stoker B may be any as long as it has a grate cooling water passage.

一方、火格子冷却水循環・冷却機構Cは、火格子冷却水Wを循環流通させる火格子冷却部C1と火格子冷却部C1の火格子冷却水Wを冷水Woにより冷却する火格子冷却水冷却部C2とを間接熱交換器4を介して熱的に連結すると共に、間接熱交換器4で使用した火格子冷却水冷却部C2の冷水Woをごみ焼却炉Dの排ガス排出経路に設置されている排ガス冷却室Eに水を噴射する水噴射供給装置Fへ供給する構成としている。   On the other hand, the grate cooling water circulation / cooling mechanism C includes a grate cooling unit C1 that circulates and distributes the grate cooling water W and a grate cooling water cooling unit that cools the grate cooling water W of the grate cooling unit C1 with the cold water Wo. C2 is thermally coupled with the indirect heat exchanger 4 and the cold water Wo of the grate cooling water cooling unit C2 used in the indirect heat exchanger 4 is installed in the exhaust gas discharge path of the garbage incinerator D. It is set as the structure supplied to the water injection supply apparatus F which injects water into the exhaust gas cooling chamber E.

尚、排ガス冷却室Eは、ごみ焼却炉Dの排ガス排出経路に必ず設置されており、ごみ焼却炉Dから排出されて廃熱ボイラ等により熱回収された排ガスを排ガス冷却室E内に導き、ここで水噴射供給装置Fにより排ガス冷却室E内に水を噴射して排ガスの温度を排ガス冷却室Eの下流側に設けたバグフィルタ等の排ガス処理設備に適した温度にまで減温するものである。   The exhaust gas cooling chamber E is always installed in the exhaust gas discharge path of the waste incinerator D, and the exhaust gas discharged from the waste incinerator D and heat recovered by a waste heat boiler or the like is guided into the exhaust gas cooling chamber E, Here, water is injected into the exhaust gas cooling chamber E by the water injection supply device F to reduce the temperature of the exhaust gas to a temperature suitable for exhaust gas treatment equipment such as a bag filter provided on the downstream side of the exhaust gas cooling chamber E. It is.

また、排ガス冷却室Eの水噴射供給装置Fは、火格子冷却水冷却部C2からの冷水Woと雨水又は井水とを貯留する水噴射タンク5と、水噴射タンク5内の冷水Woを圧送する水噴射ポンプ6と、水噴射ポンプ6の下流側に設けた流量計7と、流量計7の下流側に設けた水噴射制御弁8と、排ガス冷却室E内に冷水Woを噴射する水噴射ノズル9と、排ガス冷却室Eの出口側のガス温度を検出する排ガス温度検出器10と、排ガス温度検出器10の検出温度により水噴射制御弁8を制御する温度制御器11と、前記各機器同士を連結する配管12とから成り、排ガス冷却室Eへの冷水Woの噴射量を、排ガス温度検出器10からの検出温度に基づき温度制御器11を介して水噴射制御弁8の開度を調整することにより制御し、排ガス冷却室Eの出口側の排ガス温度を所定の温度(バグフィルタ等の排ガス処理設備に適した温度)に保つようにしたものである。   The water injection supply device F in the exhaust gas cooling chamber E pumps the cold water Wo from the grate cooling water cooling unit C2 and the water injection tank 5 that stores rainwater or well water, and the cold water Wo in the water injection tank 5 by pressure. Water jet pump 6, a flow meter 7 provided downstream of the water jet pump 6, a water injection control valve 8 provided downstream of the flow meter 7, and water for injecting cold water Wo into the exhaust gas cooling chamber E An injection nozzle 9, an exhaust gas temperature detector 10 for detecting the gas temperature on the outlet side of the exhaust gas cooling chamber E, a temperature controller 11 for controlling the water injection control valve 8 based on the detected temperature of the exhaust gas temperature detector 10, It comprises a pipe 12 that connects the devices, and the amount of cold water Wo injected into the exhaust gas cooling chamber E is determined based on the detected temperature from the exhaust gas temperature detector 10 via the temperature controller 11. The exhaust gas cooling chamber E is controlled by adjusting It is obtained to keep the exhaust gas temperature on the outlet side to a predetermined temperature (a temperature suitable for the exhaust gas treatment equipment such as bag filter).

前記火格子冷却水循環・冷却機構Cの火格子冷却部C1は、火格子冷却水Wを貯留する火格子冷却水タンク13と、火格子冷却水Wの循環ポンプ14と、火格子冷却水Wを各可動火格子1及び固定火格子2の火格子冷却水通路へ供給する給水側ヘッダ16と、各火格子冷却水通路から火格子冷却水Wを排水する排水側ヘッダ17と、排水側ヘッダ17からの火格子冷却水Wを冷却する間接熱交換器4の火格子冷却水側熱交換エレメント4aと、前記各機器同士を連結する配管21とから成り、火格子冷却水Wを循環流通させるようになっている。   The grate cooling unit C1 of the grate cooling water circulation / cooling mechanism C includes a grate cooling water tank 13 for storing the grate cooling water W, a circulation pump 14 for the grate cooling water W, and a grate cooling water W. A water supply side header 16 that supplies the grate cooling water passages of the movable grate 1 and the fixed grate 2, a drain side header 17 that drains the grate cooling water W from each grate cooling water passage, and a drain side header 17. The grate cooling water side heat exchange element 4a of the indirect heat exchanger 4 that cools the grate cooling water W from the pipe and the piping 21 that connects the devices to each other so as to circulate and circulate the grate cooling water W. It has become.

前記火格子冷却水タンク13は、開放型のタンクに形成されており、その内部には、火格子冷却水Wとして井水又は上水が貯留されている。この実施形態では、火格子冷却水タンク13には、井水が貯留されている。
また、火格子冷却水タンク13内の液面が設定値以下になった場合には、井水又は上水が火格子冷却水Wとして補給される。
The grate cooling water tank 13 is formed as an open tank, in which well water or clean water is stored as grate cooling water W. In this embodiment, well water is stored in the grate cooling water tank 13.
Further, when the liquid level in the grate cooling water tank 13 becomes a set value or less, well water or clean water is supplied as the grate cooling water W.

火格子冷却水タンク13内の火格子冷却水Wは、循環ポンプ14により圧送され、給水側ヘッダ16を経て水冷式ストーカBの各可動火格子1及び固定火格子2の火格子冷却水通路を通過し、水冷式ストーカBを冷却して約35℃昇温(この温度は炉内の燃焼状態により変動)されて排水側ヘッダ17へ排出され、間接熱交換器4で冷水Woにより約20℃に間接冷却された後、火格子冷却水タンク13内へ戻される。   The grate cooling water W in the grate cooling water tank 13 is pumped by the circulation pump 14, passes through the water supply side header 16, and passes through the grate cooling water passages of the movable grate 1 and the fixed grate 2 of the water-cooled stoker B. The water-cooled stoker B is cooled and heated to about 35 ° C. (this temperature fluctuates depending on the combustion state in the furnace) and discharged to the drain side header 17, and about 20 ° C. by the cold water Wo in the indirect heat exchanger 4. After being indirectly cooled, the grate cooling water tank 13 is returned.

尚、火格子冷却水側熱交換エレメント4aと循環ポンプ14の吸水口側の間の火格子冷却水系は、ほぼ大気圧と同圧に保持されている。その結果、火格子冷却水タンク13への火格子冷却水Wの補給は、極めて簡単に行なえる。   Note that the grate cooling water system between the grate cooling water side heat exchange element 4a and the water inlet side of the circulation pump 14 is maintained at substantially the same pressure as the atmospheric pressure. As a result, the replenishment of the grate cooling water W to the grate cooling water tank 13 can be performed very easily.

更に、間接熱交換器4に於ける火格子冷却水Wの冷却は、後述するように間接熱交換器4の火格子冷却水Wの出口側に設けた温度検出器25aにより火格子冷却水Wの温度を検出し、この検出温度に基づいて温度制御器25を介して冷水量調節弁24の開度を調整し、間接熱交換器4への冷水Wo量を調整することにより制御されている。
具体的には、間接熱交換器4から火格子冷却水タンク13へ戻す火格子冷却水Wの温度を約20℃(例えば、Woで用いている井水又は雨水の温度約15℃として+5℃位高くなる温度)に保持するようにしている。
Further, the grate cooling water W in the indirect heat exchanger 4 is cooled by a temperature detector 25a provided on the outlet side of the grate cooling water W of the indirect heat exchanger 4 as described later. , And the amount of cold water Wo to the indirect heat exchanger 4 is adjusted by adjusting the opening degree of the cold water amount adjustment valve 24 via the temperature controller 25 based on the detected temperature. .
Specifically, the temperature of the grate cooling water W returned from the indirect heat exchanger 4 to the grate cooling water tank 13 is about 20 ° C. (for example, the temperature of well water or rain water used in Wo is about 15 ° C. and + 5 ° C. Temperature).

一方、前記火格子冷却水循環・冷却機構Cの火格子冷却水冷却部C2は、冷水Woを貯留する冷水タンク22と、冷水Woの送水ポンプ23と、間接熱交換器4の冷水側熱交換エレメント4bと、冷水側熱交換エレメント4bの入口側(又は出口側)に設けた冷水量調節弁24と、間接熱交換器4の出口側の火格子冷却水Wの検出温度により冷水量調節弁24を制御する温度制御器25と、前記各機器同士を連結する配管26とから成り、冷水Woを間接熱交換器4で火格子冷却水Wの冷却に使用した後、当該冷水Woをごみ焼却炉Dの排ガス排出経路に必ず設置されている排ガス冷却室Eの水噴射供給装置Fへ供給し、前記冷水Woを排ガス冷却室Eの噴射水として利用するようにしている。   On the other hand, the grate cooling water cooling unit C2 of the grate cooling water circulation / cooling mechanism C includes a chilled water tank 22 for storing the chilled water Wo, a water supply pump 23 for the chilled water Wo, and a chilled water side heat exchange element of the indirect heat exchanger 4. 4b, a chilled water amount adjusting valve 24 provided on the inlet side (or outlet side) of the chilled water side heat exchange element 4b, and a chilled water amount adjusting valve 24 according to the detected temperature of the grate cooling water W on the outlet side of the indirect heat exchanger 4. The temperature controller 25 for controlling the water and the pipe 26 for connecting the devices to each other. After the cold water Wo is used for cooling the grate cooling water W by the indirect heat exchanger 4, the cold water Wo is used as a waste incinerator. The cooling water Wo is supplied to the water jet supply device F of the exhaust gas cooling chamber E that is always installed in the exhaust gas discharge path of D, and the cold water Wo is used as the jet water of the exhaust gas cooling chamber E.

前記冷水タンク22は、開放型のタンクに形成されており、その内部には、冷水Woとして井水又は雨水が貯留されている。
また、冷水タンク22内の液面が設定値以下になると、冷水Woとして井水を使用している場合には、井水が井水ポンプ(図示省略)等により冷水Woとして補給される。
尚、冷水タンク22内の冷水Woの一部は、分岐配管26aを介してごみ焼却プラント内で補給水、加湿水、散水等として使用される。
The cold water tank 22 is formed as an open tank, in which well water or rain water is stored as cold water Wo.
Further, when the liquid level in the cold water tank 22 is equal to or lower than the set value, when well water is used as the cold water Wo, the well is replenished as cold water Wo by a well water pump (not shown) or the like.
A part of the cold water Wo in the cold water tank 22 is used as make-up water, humidified water, sprinkling water, etc. in the waste incineration plant via the branch pipe 26a.

冷水タンク22内の冷水Woは、送水ポンプ23により圧送され、冷水量調節弁24を経て間接熱交換器4に入り、ここで火格子冷却水Wを冷却した後、水噴射供給装置Fの水噴射タンク5内に入る。   The cold water Wo in the cold water tank 22 is pumped by the water pump 23 and enters the indirect heat exchanger 4 through the cold water amount adjustment valve 24, where the grate cooling water W is cooled, and then the water in the water injection supply device F Enter into the injection tank 5.

このとき、間接熱交換器4へ流通させる冷水Woの量は、間接熱交換後の火格子冷却水Wの温度が一定になるように調整されている。
即ち、間接熱交換器4への冷水Wo量の調整は、間接熱交換器4の火格子冷却水Wの出口側に設けた温度検出器25aにより火格子冷却水Wの温度を検出し、この検出温度に基づいて温度制御器25で冷水量調節弁24の開度を調整することにより行なわれている。
例えば、火格子冷却水Wに約15℃の井水を使用した場合には、間接熱交換後の火格子冷却水Wの温度が約20℃(+5℃位)になるように、冷水Woの量が冷水量調節弁24により調整されている。
At this time, the amount of the cold water Wo circulated to the indirect heat exchanger 4 is adjusted so that the temperature of the grate cooling water W after the indirect heat exchange becomes constant.
That is, the amount of the cold water Wo to the indirect heat exchanger 4 is adjusted by detecting the temperature of the grate cooling water W by the temperature detector 25a provided on the outlet side of the grate cooling water W of the indirect heat exchanger 4. This is done by adjusting the opening degree of the cold water amount adjusting valve 24 by the temperature controller 25 based on the detected temperature.
For example, when well water of about 15 ° C. is used as the grate cooling water W, the temperature of the grate cooling water W after indirect heat exchange is about 20 ° C. (about + 5 ° C.). The amount is adjusted by the cold water amount adjusting valve 24.

尚、この実施形態では、冷水量調節弁24の取り付け位置を冷水側熱交換エレメント4bの入口側としているが、他の実施形態では、冷水量調節弁24を冷水側熱交換エレメント4bの出口側に取り付けるようにしても良い。
また、間接熱交換器4としては、火格子冷却水Wと冷水Woとが非混合の状態で熱交換を行うものであれば、プレート式、管形式等に拘わらず、如何なる構造の熱交換器であっても良い。
In this embodiment, the mounting position of the chilled water amount adjusting valve 24 is set to the inlet side of the chilled water side heat exchange element 4b. However, in other embodiments, the chilled water amount adjusting valve 24 is set to the outlet side of the chilled water side heat exchanging element 4b. You may make it attach to.
The indirect heat exchanger 4 may have any structure regardless of whether it is a plate type or a tube type, as long as it performs heat exchange in a state where the grate cooling water W and the cold water Wo are not mixed. It may be.

ところで、前記間接熱交換器4の伝熱面積は、下記の条件で決められている(数値は何れも一例である)。
・ 火格子冷却水Wの水冷式ストーカBを出た温度、つまり間接熱交換器4の入口側の温 度Thin(20℃+水冷火格子での振れ幅込みの温度上昇分60℃)=80℃
・ 間接熱交換器4の出口水温Thout=20℃
・ 火格子冷却水量Wh(t/h)
・ 間接熱交換器4の入口の冷水温度Tcin=井水又は雨水の水温(15℃)
・ 間接熱交換器4の出口の冷水温度Tcoutは、一般的な渦巻きポンプがタンクと同 等レベルで設置してあっても、キャビテーションを起こさない温度以下(例えば、 50℃以下)
・ 間接熱交換器4への冷水量Wc(t/h)が排ガス冷却室Eへの設計上の水噴射量 (Ww)以上にならないようにした量(例えば、Wc=Ww×0.9)
ここで、×0.9としているのは、冷水が水噴射タンク5から溢れないようにするた め。
つまり、
火格子冷却水側の間接熱交換器4での交換熱量:Qh=Wh×(Thin−Thout)
火格子冷却水の冷却側に於ける間接熱交換器4での熱交換量:Qc=Wc×(Tcout−Tcin)
間接熱交換器4の伝熱面積:S=Qh/U/ΔTm
ここで、Uは熱交換器の総括熱伝達係数、ΔTmは熱交換器の対数平均温度差である。
また、Qh=Qcとなるので、冷水温度Tcoutが50℃以下になるように間接熱交換器4の伝熱面積Sを求める。
このようにして、間接熱交換器4の伝熱面積が決まる。
By the way, the heat transfer area of the indirect heat exchanger 4 is determined under the following conditions (all numerical values are examples).
・ Temperature of the grate cooling water W coming out of the water-cooled stoker B, that is, the temperature Thin at the inlet side of the indirect heat exchanger 4 (20 ° C. + 60 ° C. of the temperature increase included in the water-cooled grate) = 80 ℃
-Inlet heat exchanger 4 outlet water temperature Thout = 20 ° C
・ Grate cooling water volume Wh (t / h)
-Cold water temperature Tcin at the inlet of the indirect heat exchanger 4 = temperature of well water or rain water (15 ° C)
・ The chilled water temperature Tcout at the outlet of the indirect heat exchanger 4 is below the temperature that does not cause cavitation even if a general centrifugal pump is installed at the same level as the tank (for example, 50 ° C or less).
An amount that prevents the amount of cold water Wc (t / h) to the indirect heat exchanger 4 from exceeding the designed water injection amount (Ww) to the exhaust gas cooling chamber E (for example, Wc = Ww × 0.9)
Here, x0.9 is set to prevent cold water from overflowing from the water jet tank 5.
That means
Exchange heat quantity in the indirect heat exchanger 4 on the grate cooling water side: Qh = Wh × (Thin−Thout)
Heat exchange amount in indirect heat exchanger 4 on the cooling side of the grate cooling water: Qc = Wc × (Tcout−Tcin)
Heat transfer area of indirect heat exchanger 4: S = Qh / U / ΔTm
Here, U is the overall heat transfer coefficient of the heat exchanger, and ΔTm is the logarithmic average temperature difference of the heat exchanger.
Since Qh = Qc, the heat transfer area S of the indirect heat exchanger 4 is determined so that the cold water temperature Tcout is 50 ° C. or less.
In this way, the heat transfer area of the indirect heat exchanger 4 is determined.

上記のように間接熱交換器4の伝熱面積を決めておけば、水噴射供給装置Fの水噴射ポンプ6がキャビテーションを起こすことはない。また、冷水量Wcと排ガス冷却室Eへの設計上の水噴射量Wwに差が生じ、水噴射タンク5の水位が変動するが、水噴射タンク5自体に別途、レベル制御機能(例えば、ボールタップ式、接点式on、off制御等)を設けておれば、問題はない。   If the heat transfer area of the indirect heat exchanger 4 is determined as described above, the water injection pump 6 of the water injection supply device F does not cause cavitation. Further, there is a difference between the cold water amount Wc and the designed water injection amount Ww to the exhaust gas cooling chamber E, and the water level of the water injection tank 5 fluctuates. However, the water injection tank 5 itself has a level control function (for example, a ball tap). If a formula, contact type on, off control, etc.) are provided, there is no problem.

このように、上述したごみ焼却炉Dの水冷式ストーカ装置Aに於いては、火格子冷却水冷却部C2の冷水Woを間接熱交換器4で火格子冷却水Wの冷却に使用した後、排ガス冷却室Eの水噴射供給装置Fへ供給して排ガス冷却室Eの噴射水として利用するようにしているため、冒頭で述べた従来の水冷式ストーカ装置のように冷却塔を必要とすることがなく、設備の簡略化及び設備費の削減を図れる。
また、このごみ焼却炉Dの水冷式ストーカ装置Aに於いては、冷却塔を削減できたことによって、薬剤の注入装置及び薬剤が不要になって設備費をより削減することができると共に、ランニングコストの削減も図れる。
更に、このごみ焼却炉Dの水冷式ストーカ装置Aに於いては、冷却水として井水又は雨水を使用しているため、冷水Woに上水を使用した従来の冷却式ストーカ装置に比較してコスト削減を図れる。
Thus, in the above-described water-cooled stoker device A of the waste incinerator D, after using the cold water Wo of the grate cooling water cooling section C2 for cooling the grate cooling water W by the indirect heat exchanger 4, Since it is supplied to the water injection supply device F of the exhaust gas cooling chamber E and used as the injection water of the exhaust gas cooling chamber E, a cooling tower is required like the conventional water-cooled stoker device described at the beginning. It is possible to simplify equipment and reduce equipment costs.
In addition, in the water-cooled stoker device A of the waste incinerator D, since the cooling tower can be reduced, the chemical injection device and the chemical become unnecessary, and the equipment cost can be further reduced. Costs can be reduced.
Furthermore, in the water-cooled stoker device A of the waste incinerator D, since well water or rain water is used as cooling water, compared with a conventional cooling stoker device using clean water as cold water Wo. Cost reduction can be achieved.

図2は本発明の第2の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aの概略系統図を示し、当該ごみ焼却炉Dの水冷式ストーカ装置Aは、火格子冷却水通路をそれぞれ形成した可動火格子1と固定火格子2とを階段状又は傾斜状に組み合せて成る水冷式ストーカBと、水冷式ストーカBへ火格子冷却水Wを循環流通させつつ冷却する火格子冷却水循環・冷却機構Cとから構成されており、前記火格子冷却水循環・冷却機構Cが熱利用設備27及び第2間接熱交換器28を備えていると共に、前記熱利用設備27と火格子冷却部C1の火格子冷却水系とを、間接熱交換器4と排水側ヘッダ17との間に設けた第2間接熱交換器28を介して熱的に連結したものである。   FIG. 2 shows a schematic system diagram of a water-cooled stoker device A of a waste incinerator D according to the second embodiment of the present invention, and the water-cooled stoker device A of the waste incinerator D has a grate cooling water passage. A water-cooled stoker B, which is a combination of the movable grate 1 and the fixed grate 2 formed in a stepped or inclined manner, and a grate cooling water circulation that cools the water-cooled stoker B while circulating the grate cooling water W. The grate cooling water circulation / cooling mechanism C includes a heat utilization facility 27 and a second indirect heat exchanger 28, and includes the heat utilization facility 27 and the grate cooling section C1. The grate cooling water system is thermally connected via a second indirect heat exchanger 28 provided between the indirect heat exchanger 4 and the drain side header 17.

即ち、前記ごみ焼却炉Dの水冷式ストーカ装置Aは、間接熱交換器4に入る前の火格子冷却水Wを第2間接熱交換器28に通し、ここで熱利用設備27からの冷却水又は冷却空気により間接冷却してから間接熱交換器4へ導くようにすると共に、第2間接熱交換器28で加熱された冷却水、冷却空気、熱媒油又は低沸点媒体を熱利用設備27へ導き、ここで熱利用設備27の熱源として利用するようにしたものである。
また、熱利用設備27としては、ごみ焼却炉Dに付随する機器(例えば、ボイラの給水を加熱するエコノマイザやごみ焼却炉Dへの燃焼用空気を予熱する空気予熱器等)やごみ焼却炉Dに付随しない機器(例えば、融雪機等)が使用されている。
That is, the water-cooled stoker device A of the waste incinerator D passes the grate cooling water W before entering the indirect heat exchanger 4 through the second indirect heat exchanger 28, where the cooling water from the heat utilization equipment 27 is passed. Alternatively, the cooling water is indirectly cooled and then guided to the indirect heat exchanger 4, and the cooling water, the cooling air, the heat medium oil, or the low boiling point medium heated by the second indirect heat exchanger 28 is used as the heat utilization equipment 27. This is used as a heat source of the heat utilization equipment 27 here.
Further, as the heat utilization equipment 27, equipment associated with the waste incinerator D (for example, an economizer that heats boiler feed water, an air preheater that preheats combustion air to the waste incinerator D, etc.) or a waste incinerator D Equipment that does not accompany the snow (for example, a snow melting machine) is used.

尚、前記ごみ焼却炉Dの水冷式ストーカ装置Aに於いては、熱利用設備27及び第2間接熱交換器28以外の設備及び機器(水冷式ストーカB、火格子冷却水循環・冷却機構C、火格子冷却部C1、火格子冷却水冷却部C2、間接熱交換器4、排ガス冷却室E、水噴射供給装置F等)は、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同じ構造に構成されており、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同じ部位・部材には同一の参照番号を付し、その詳細な説明を省略する。   In the water-cooled stoker device A of the waste incinerator D, facilities and equipment other than the heat utilization equipment 27 and the second indirect heat exchanger 28 (water-cooled stoker B, grate cooling water circulation / cooling mechanism C, The grate cooling unit C1, the grate cooling water cooling unit C2, the indirect heat exchanger 4, the exhaust gas cooling chamber E, the water injection supply device F, etc.) are the same as the water-cooled stoker device A of the waste incinerator D shown in FIG. The same parts and members as those of the water-cooled stoker apparatus A of the waste incinerator D shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof is omitted.

上述した第2の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aは、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同様の作用効果を奏することができる。
しかも、第2の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aは、間接熱交換器4に入る前の火格子冷却水Wを第2間接熱交換器28に通してここで熱利用設備27からの冷却水、冷却空気、熱媒油又は低沸点媒体により冷却するようにしているため、熱エネルギーの有効利用を図れる。
The water-cooled stoker device A of the waste incinerator D according to the second embodiment described above can achieve the same operational effects as the water-cooled stoker device A of the waste incinerator D shown in FIG.
In addition, the water-cooled stoker device A of the waste incinerator D according to the second embodiment uses the grate cooling water W before entering the indirect heat exchanger 4 through the second indirect heat exchanger 28 and uses the heat here. Since the cooling is performed by the cooling water, the cooling air, the heat medium oil, or the low boiling point medium from the facility 27, the heat energy can be effectively used.

図3は本発明の第3の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aの概略系統図を示し、当該ごみ焼却炉Dの水冷式ストーカ装置Aは、火格子冷却水通路をそれぞれ形成した可動火格子1と固定火格子2とを階段状又は傾斜状に組み合せて成る水冷式ストーカBと、水冷式ストーカBへ火格子冷却水Wを循環流通させつつ冷却する火格子冷却水循環・冷却機構Cとから構成されており、火格子冷却水循環・冷却機構Cの火格子冷却水冷却部C2に改良を加え、火格子冷却水冷却部C2の冷水タンク22への冷水Woの供給が雨水しか使用できないときに使用するものである。
尚、冷水タンク22への供給が雨水しか使用できないときの例として、例えば、ごみ処理施設内への降水については、放流できず施設内処理をする必要があり、積極的に雨水を使用しないと、処理しきれない場合等がある。
FIG. 3 shows a schematic system diagram of a water-cooled stoker device A of a waste incinerator D according to the third embodiment of the present invention, and the water-cooled stoker device A of the waste incinerator D has a grate cooling water passage. A water-cooled stoker B, which is a combination of the movable grate 1 and the fixed grate 2 formed in a stepped or inclined manner, and a grate cooling water circulation that cools the water-cooled stoker B while circulating the grate cooling water W. The cooling mechanism C is configured to improve the grate cooling water cooling unit C2 of the grate cooling water circulation / cooling mechanism C, and supply of the cold water Wo to the cold water tank 22 of the grate cooling water cooling unit C2 is rainwater. It is used only when it can only be used.
In addition, as an example when only the rainwater can be used for the supply to the cold water tank 22, for example, the precipitation in the waste treatment facility cannot be discharged and needs to be treated in the facility. In some cases, it cannot be processed.

即ち、前記火格子冷却水循環・冷却機構Cの火格子冷却水冷却部C2は、冷水Woを貯留する冷水タンク22と、冷水Woの送水ポンプ23と、間接熱交換器4の冷水側熱交換エレメント4bと、冷水側熱交換エレメント4bの入口側に設けた冷水量調節弁24と、排ガス冷却室Eへの噴射水量に応じて冷水量調節弁24を制御する流量制御器29と、冷水側熱交換エレメント4bの出口側に設けられ、間接熱交換器4への冷水Woの流通制御を行う三方弁30と、間接熱交換器4の出口側の火格子冷却水Wの検出温度により三方弁30を制御する温度制御器25とから成り、流量計7からの流量に応じて流量制御器29により冷水量調節弁24を制御して排ガス冷却室Eへの水噴射量に応じた冷水Woの量を確保し、また、三方弁30を間接熱交換器4の出口側の火格子冷却水Wの検出温度(温度検出器25aからの検出温度)に基づいて温度制御器25により制御し、間接熱交換器4への冷水Woの流通制御を行うようにしたものである。   That is, the grate cooling water cooling unit C2 of the grate cooling water circulation / cooling mechanism C includes a chilled water tank 22 for storing the chilled water Wo, a water supply pump 23 for the chilled water Wo, and a chilled water side heat exchange element of the indirect heat exchanger 4. 4b, a chilled water amount adjusting valve 24 provided on the inlet side of the chilled water side heat exchange element 4b, a flow rate controller 29 for controlling the chilled water amount adjusting valve 24 according to the amount of water injected into the exhaust gas cooling chamber E, and a chilled water side heat A three-way valve 30 that is provided on the outlet side of the exchange element 4b and controls the flow of the cold water Wo to the indirect heat exchanger 4, and a three-way valve 30 based on the detected temperature of the grate cooling water W on the outlet side of the indirect heat exchanger 4. The amount of cold water Wo according to the amount of water injected into the exhaust gas cooling chamber E by controlling the cold water amount adjusting valve 24 by the flow rate controller 29 according to the flow rate from the flow meter 7. Secure the three-way valve 30 Based on the detected temperature of the grate cooling water W on the outlet side of the heat exchanger 4 (the detected temperature from the temperature detector 25a), the temperature controller 25 controls the flow control of the cold water Wo to the indirect heat exchanger 4. It is what I do.

尚、この実施形態では、三方弁30は、冷水側熱交換エレメント4bの出口側に設けたが、他の実施形態では、三方弁30を冷水側熱交換エレメント4bの入口側に設けても良い。
また、三方弁30を冷水側熱交換エレメント4bの出口側に設ける場合、三方弁30には、二つの管路から一つの管に流体を混合して流せる混合形の三方弁30を使用し、更に、三方弁30を冷水側熱交換エレメント4bの入口側に設ける場合、三方弁30には、一つの管路から二つの管路へ流体を所定の比率で分散して流せる分割形の三方弁30を使用する。
In this embodiment, the three-way valve 30 is provided on the outlet side of the cold water side heat exchange element 4b. However, in another embodiment, the three way valve 30 may be provided on the inlet side of the cold water side heat exchange element 4b. .
When the three-way valve 30 is provided on the outlet side of the cold water side heat exchange element 4b, the three-way valve 30 uses a mixed three-way valve 30 that can mix and flow fluid from two pipes to one pipe, Further, when the three-way valve 30 is provided on the inlet side of the cold water side heat exchange element 4b, the three-way valve 30 is a split three-way valve that can distribute and flow fluid from one pipe to two pipes at a predetermined ratio. 30 is used.

前記ごみ焼却炉Dの水冷式ストーカ装置Aに於いては、三方弁30及び流量制御器29以外の設備及び機器(水冷式ストーカB、火格子冷却水循環・冷却機構C、火格子冷却部C1、火格子冷却水冷却部C2、間接熱交換器4、排ガス冷却室E、水噴射供給装置F等)は、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同じ構造に構成されており、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同じ部位・部材には同一の参照番号を付し、その詳細な説明を省略する。   In the water-cooled stoker device A of the waste incinerator D, equipment and equipment other than the three-way valve 30 and the flow rate controller 29 (water-cooled stoker B, grate cooling water circulation / cooling mechanism C, grate cooling unit C1, The grate cooling water cooling section C2, the indirect heat exchanger 4, the exhaust gas cooling chamber E, the water injection supply device F, etc.) are configured in the same structure as the water-cooled stoker device A of the waste incinerator D shown in FIG. The same parts and members as those of the water-cooled stoker device A of the waste incinerator D shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof is omitted.

上述した第3の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aも、図1に示すごみ焼却炉Dの水冷式ストーカ装置Aと同様の作用効果を奏することができる。   The water-cooled stoker device A of the waste incinerator D according to the third embodiment described above can also exhibit the same operational effects as the water-cooled stoker device A of the waste incinerator D shown in FIG.

尚、上述した第3の実施形態に係るごみ焼却炉Dの水冷式ストーカ装置Aにおいて、図3に一点鎖線で示す如く、火格子冷却水循環・冷却機構Cに熱利用設備27及び第2間接熱交換器28を追加し、前記熱利用設備27と火格子冷却部C1の火格子冷却水系とを、間接熱交換器4と排水側ヘッダ17との間に設けた第2間接熱交換器28を介して熱的に連結するようにしても良い。   In the water-cooled stalker apparatus A of the refuse incinerator D according to the third embodiment described above, the heat utilization equipment 27 and the second indirect heat are added to the grate cooling water circulation / cooling mechanism C as shown by a one-dot chain line in FIG. An exchanger 28 is added, and a second indirect heat exchanger 28 in which the heat utilization equipment 27 and the grate cooling water system of the grate cooling unit C1 are provided between the indirect heat exchanger 4 and the drain side header 17 is provided. It may be configured to be thermally connected through the vias.

Aは水冷式ストーカ装置、Bは水冷式ストーカ、Cは火格子冷却水循環・冷却機構、C1は火格子冷却部、C2は火格子冷却水冷却部、Dはごみ焼却炉、Eは排ガス冷却室、Fは水噴射供給装置、Wは火格子冷却水、Woは冷水、1可動火格子、2は固定火格子、3は水冷式火格子本体、4は間接熱交換器、4aは火格子冷却水側熱交換エレメント、4bは冷水側熱交換エレメント、5は水噴射タンク、6は水噴射ポンプ、7は流量計、8は水噴射制御弁、9は水噴射ノズル、10は排ガス温度検出器、11は温度制御器、12は配管、13は火格子冷却水タンク、14は循環ポンプ、16は給水側ヘッダ、17は排水側ヘッダ、21は配管、22は冷水タンク、23は送水ポンプ、24は冷水量調節弁、25は温度制御器、25aは温度検出器、26は配管、26aは分岐配管、27は熱利用設備、28は第2間接熱交換器、29は流量制御器、30は三方弁。   A is a water-cooled stoker device, B is a water-cooled stoker, C is a grate cooling water circulation / cooling mechanism, C1 is a grate cooling unit, C2 is a grate cooling water cooling unit, D is a waste incinerator, and E is an exhaust gas cooling chamber , F is a water jet supply device, W is a grate cooling water, Wo is cold water, 1 movable grate, 2 is a fixed grate, 3 is a water-cooled grate body, 4 is an indirect heat exchanger, 4a is a grate cooling Water side heat exchange element, 4b is a cold water side heat exchange element, 5 is a water injection tank, 6 is a water injection pump, 7 is a flow meter, 8 is a water injection control valve, 9 is a water injection nozzle, and 10 is an exhaust gas temperature detector. , 11 is a temperature controller, 12 is piping, 13 is a grate cooling water tank, 14 is a circulation pump, 16 is a water supply side header, 17 is a drainage side header, 21 is piping, 22 is a cold water tank, 23 is a water pump, 24 is a cold water amount control valve, 25 is a temperature controller, and 25a is a temperature detector. Vessel, 26 pipe, 26a the branch pipe, 27 heat utilization equipment, second indirect heat exchanger 28, 29 flow controller, 30 is a three-way valve.

Claims (6)

火格子冷却水通路をそれぞれ形成した可動火格子と固定火格子とを階段状又は傾斜状に組み合せて成る水冷式ストーカと、水冷式ストーカへ火格子冷却水を循環流通させつつ冷却する火格子冷却水循環・冷却機構とから構成したごみ焼却炉の水冷式ストーカ装置に於いて、前記火格子冷却水循環・冷却機構は、火格子冷却水を循環流通させる火格子冷却部と火格子冷却部の火格子冷却水を冷水により冷却する火格子冷却水冷却部とを間接熱交換器を介して熱的に連結すると共に、火格子冷却水冷却部の冷水をごみ焼却炉の排ガス排出経路に設置されている排ガス冷却室に水を噴射する水噴射供給装置へ供給する構成とし、前記火格子冷却部は、火格子冷却水を貯留する火格子冷却水タンクと、火格子冷却水の循環ポンプと、火格子冷却水を各可動火格子及び固定火格子の火格子冷却水通路へ供給する給水側ヘッダと、各火格子冷却水通路から火格子冷却水を排水する排水側ヘッダと、排水側ヘッダからの火格子冷却水を冷却する間接熱交換器の火格子冷却水側熱交換エレメントとから成り、また、前記火格子冷却水冷却部は、冷水を貯留する冷水タンクと、冷水の送水ポンプと、間接熱交換器の冷水側熱交換エレメントと、冷水側熱交換エレメントの入口側又は出口側に設けた冷水量調節弁と、間接熱交換器の出口側の火格子冷却水の検出温度により冷水量調節弁を制御する温度制御器とから成ることを特徴とするごみ焼却炉の水冷式ストーカ装置。   A water-cooled stoker that is a combination of a movable grate and a fixed grate each formed with a grate cooling water passage, and a grate cooling that cools the grate cooling water while circulating the grate cooling water to the water-cooled stoker. In a water-cooled stoker device for a waste incinerator comprising a water circulation / cooling mechanism, the grate cooling water circulation / cooling mechanism includes a grate cooling unit that circulates and distributes grate cooling water and a grate of a grate cooling unit. A grate cooling water cooling unit that cools the cooling water with cold water is thermally connected to the grate cooling water cooling unit via an indirect heat exchanger, and the grate cooling water cooling unit is installed in the exhaust gas discharge path of the waste incinerator. The grate cooling unit is configured to supply water to a water injection supply device that injects water into the exhaust gas cooling chamber, and the grate cooling unit includes a grate cooling water tank that stores grate cooling water, a grate cooling water circulation pump, and a grate Cooling water for each Water supply side headers that supply the grate cooling water passages of the dynamic grate and fixed grate, drain side headers that drain the grate cooling water from each grate cooling water passage, and grate cooling water from the drain side header The grate cooling water side heat exchange element of the indirect heat exchanger to be cooled, and the grate cooling water cooling section includes a cold water tank for storing cold water, a water feed pump for cold water, and cold water for the indirect heat exchanger. The temperature at which the chilled water amount adjusting valve is controlled by the detected temperature of the grate cooling water at the outlet side of the indirect heat exchanger, the chilled water amount adjusting valve provided on the inlet side or outlet side of the chilled water side heat exchanging element, and the outlet side of the indirect heat exchanger A water-cooled stoker device for a waste incinerator characterized by comprising a controller. 火格子冷却水循環・冷却機構は、熱利用設備及び第2間接熱交換器を備えており、前記熱利用設備と火格子冷却部の火格子冷却水系とを、間接熱交換器と排水側ヘッダとの間に設けた第2間接熱交換器を介して熱的に連結したことを特徴とする請求項1に記載のごみ焼却炉の水冷式ストーカ装置。   The grate cooling water circulation / cooling mechanism includes a heat utilization facility and a second indirect heat exchanger, and the heat utilization facility and the grate cooling water system of the grate cooling section are connected to the indirect heat exchanger, the drain side header, The water-cooled stoker device for a refuse incinerator according to claim 1, wherein the water-cooled stoker device is thermally connected via a second indirect heat exchanger provided between the two. 火格子冷却水通路をそれぞれ形成した可動火格子と固定火格子とを階段状又は傾斜状に組み合せて成る水冷式ストーカと、水冷式ストーカへ火格子冷却水を循環流通させつつ冷却する火格子冷却水循環・冷却機構とから構成したごみ焼却炉の水冷式ストーカ装置に於いて、前記火格子冷却水循環・冷却機構は、火格子冷却水を循環流通させる火格子冷却部と火格子冷却部の火格子冷却水を冷水により冷却する火格子冷却水冷却部とを間接熱交換器を介して熱的に連結すると共に、火格子冷却水冷却部の冷水をごみ焼却炉の排ガス排出経路に設置されている排ガス冷却室に水を噴射する水噴射供給装置へ供給する構成とし、前記火格子冷却部は、火格子冷却水を貯留する火格子冷却水タンクと、火格子冷却水の循環ポンプと、火格子冷却水を各可動火格子及び固定火格子の火格子冷却水通路へ供給する給水側ヘッダと、各火格子冷却水通路から火格子冷却水を排水する排水側ヘッダと、排水側ヘッダからの火格子冷却水を冷却する間接熱交換器の火格子冷却水側熱交換エレメントとから成り、また、前記火格子冷却水冷却部は、冷水を貯留する冷水タンクと、冷水の送水ポンプと、間接熱交換器の冷水側熱交換エレメントと、冷水側熱交換エレメントの入口側に設けた冷水量調節弁と、排ガス冷却室への噴射水量に応じて冷水量調節弁を制御する流量制御器と、冷水側熱交換エレメントの出口側又は入口側に設けられ、間接熱交換器への冷水の流通制御を行う三方弁と、間接熱交換器の出口側の火格子冷却水の検出温度により三方弁を制御する温度制御器とから成ることを特徴とするごみ焼却炉の水冷式ストーカ装置。   A water-cooled stoker that is a combination of a movable grate and a fixed grate each formed with a grate cooling water passage, and a grate cooling that cools the grate cooling water while circulating the grate cooling water to the water-cooled stoker. In a water-cooled stoker device for a waste incinerator comprising a water circulation / cooling mechanism, the grate cooling water circulation / cooling mechanism includes a grate cooling unit that circulates and distributes grate cooling water and a grate of a grate cooling unit. A grate cooling water cooling unit that cools the cooling water with cold water is thermally connected to the grate cooling water cooling unit via an indirect heat exchanger, and the grate cooling water cooling unit is installed in the exhaust gas discharge path of the waste incinerator. The grate cooling unit is configured to supply water to a water injection supply device that injects water into the exhaust gas cooling chamber, and the grate cooling unit includes a grate cooling water tank that stores grate cooling water, a grate cooling water circulation pump, and a grate Cooling water for each Water supply side headers that supply the grate cooling water passages of the dynamic grate and fixed grate, drain side headers that drain the grate cooling water from each grate cooling water passage, and grate cooling water from the drain side header The grate cooling water side heat exchange element of the indirect heat exchanger to be cooled, and the grate cooling water cooling section includes a cold water tank for storing cold water, a water feed pump for cold water, and cold water for the indirect heat exchanger. Side heat exchange element, chilled water amount adjustment valve provided on the inlet side of the chilled water side heat exchange element, a flow rate controller for controlling the chilled water amount adjustment valve according to the amount of water injected into the exhaust gas cooling chamber, and the chilled water side heat exchange element A three-way valve that controls the flow of cold water to the indirect heat exchanger and a temperature controller that controls the three-way valve based on the detected temperature of grate cooling water on the outlet side of the indirect heat exchanger Characterized by comprising Water-cooled stoker device only incinerator. 請求項1に記載のごみ焼却炉の水冷式ストーカ装置に於いて、火格子冷却水タンク内の火格子冷却水を井水又は上水とし、井水又は上水を火格子冷却水循環ポンプにより圧送して水冷式ストーカに通した後、間接熱交換器により冷却して火格子冷却水タンクに戻し、また、冷却タンク内の冷水を井水又は雨水とし、井水又は雨水を冷水ポンプにより間接熱交換器に圧送してここで火格子冷却水の冷却に使用した後、排ガス冷却室の水噴射供給装置へ供給して排ガス冷却室の噴射水として利用するようにしたことを特徴とするごみ焼却炉の水冷式ストーカ装置の運転方法。   2. A water-cooled stoker device for a waste incinerator according to claim 1, wherein the grate cooling water in the grate cooling water tank is well water or clean water, and the well water or clean water is pumped by a grate cooling water circulation pump. After passing through a water-cooled stoker, it is cooled by an indirect heat exchanger and returned to the grate cooling water tank, and the cold water in the cooling tank is made into well water or rain water, and the well water or rain water is indirectly heated by a cold water pump. Waste incineration characterized by being fed to the exchanger and used here for cooling the grate cooling water, then supplied to the water jet supply device of the exhaust gas cooling chamber and used as the jet water of the exhaust gas cooling chamber Operation method of water-cooled stoker equipment for furnace. 間接熱交換器に入る前の火格子冷却水を第2間接熱交換器に通してここで熱利用設備からの冷却水又は冷却空気により冷却するようにしたことを特徴とする請求項4に記載のごみ焼却炉の水冷式ストーカ装置の運転方法。   5. The grate cooling water before entering the indirect heat exchanger is passed through the second indirect heat exchanger, where it is cooled by cooling water or cooling air from the heat utilization equipment. To operate a water-cooled stoker device in a waste incinerator. 請求項3に記載のごみ焼却炉の水冷式ストーカ装置に於いて、火格子冷却水タンク内の火格子冷却水を井水又は上水とし、井水又は上水を火格子冷却水循環ポンプにより圧送して水冷式ストーカに通した後、間接熱交換器により冷却して火格子冷却水タンクに戻し、また、冷却タンク内の冷水を雨水とし、この雨水を送水ポンプにより間接熱交換器に圧送してここで火格子冷却水の冷却に使用した後、当該雨水を排ガス冷却室の水噴射供給装置へ供給して排ガス冷却室の噴射水として利用し、更に、排ガス冷却室への水噴射流量に応じて冷水量調節弁を制御して雨水の量を調整すると共に、間接熱交換器の出口側の火格子冷却水の検出温度に基づいて三方弁を制御して間接熱交換器への雨水の流通制御を行うようにしたことを特徴とするごみ焼却炉の水冷式ストーカ装置の運転方法。   4. A water-cooled stoker device for a refuse incinerator according to claim 3, wherein the grate cooling water in the grate cooling water tank is well water or clean water, and the well water or clean water is pumped by a grate cooling water circulation pump. After passing through a water-cooled stoker, it is cooled by an indirect heat exchanger and returned to the grate cooling water tank, and the cold water in the cooling tank is made rainwater, and this rainwater is pumped to the indirect heat exchanger by a water pump. After using the grate cooling water here, the rainwater is supplied to the water injection supply device of the exhaust gas cooling chamber and used as the injection water of the exhaust gas cooling chamber, and the water injection flow rate to the exhaust gas cooling chamber is further increased. Accordingly, the amount of rainwater is adjusted by controlling the cold water amount control valve, and the rainwater to the indirect heat exchanger is controlled by controlling the three-way valve based on the detected temperature of the grate cooling water on the outlet side of the indirect heat exchanger. Garbage characterized by distribution control How the operation of the water-cooled stoker device 却炉.
JP2014078325A 2014-04-07 2014-04-07 Water-cooled stoker device for waste incinerator and operation method thereof Expired - Fee Related JP6288841B2 (en)

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JPH1038234A (en) * 1996-07-24 1998-02-13 Nagasaki Pref Gov Thermal decomposition and incineration unit
JP2001343112A (en) * 2000-05-31 2001-12-14 Nkk Corp Waste incinerator
JP3876133B2 (en) * 2001-06-21 2007-01-31 株式会社タクマ Water-cooled stoker device for waste incinerator and its operation method
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