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JP5954704B2 - Closed system flue gas treatment system - Google Patents

Closed system flue gas treatment system Download PDF

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JP5954704B2
JP5954704B2 JP2012096126A JP2012096126A JP5954704B2 JP 5954704 B2 JP5954704 B2 JP 5954704B2 JP 2012096126 A JP2012096126 A JP 2012096126A JP 2012096126 A JP2012096126 A JP 2012096126A JP 5954704 B2 JP5954704 B2 JP 5954704B2
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exhaust gas
water
incineration ash
supplied
ejector
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JP2013224831A (en
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吉田 博久
博久 吉田
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Tokyo Metropolitan University
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Description

本発明は、閉鎖系排煙処理システムに関する。特に、本発明は、放射性物質を含有する廃棄物を処理する閉鎖系排煙処理システムに関する。   The present invention relates to a closed system flue gas treatment system. In particular, the present invention relates to a closed-system smoke treatment system for treating waste containing radioactive materials.

従来、焼却炉からの排煙を集塵器で除塵し、湿式洗煙法によって除塵排ガスを洗浄する廃棄物の焼却方法であって、湿式洗煙法により発生する洗煙排水を凝集、濃縮して洗煙処理汚泥とし、焼却炉に洗煙処理汚泥を返送することによって汚泥中のダイオキシン類を加熱分解させ、また、重金属類を集塵器に焼却炉を介して排煙と共に返送することで捕集灰として取り出す廃棄物等の焼却方法が知られている(例えば、特許文献1参照。)。特許文献1に記載の廃棄物等の焼却方法によれば、廃棄物の焼却に際し、洗煙処理汚泥中のダイオキシン類や重金属類を特別な装置を用いることなく分解することができ、また、重金属類を1箇所に捕集することができる。   Conventionally, it is a waste incineration method that removes the flue gas from the incinerator with a dust collector and cleans the exhaust gas from the dust by the wet smoke cleaning method. By converting the sludge into sludge and returning it to the incinerator, the dioxins in the sludge are thermally decomposed, and heavy metals are returned to the dust collector along with the flue gas through the incinerator. A method for incineration of waste or the like to be taken out as collected ash is known (for example, see Patent Document 1). According to the method for incinerating wastes and the like described in Patent Document 1, dioxins and heavy metals in smoke-washed sludge can be decomposed without using a special device when incinerating wastes. Can be collected in one place.

特開2004−325010号公報JP 2004-325010 A

しかし、特許文献1に記載されている廃棄物等の焼却方法においては、焼却炉等から環境中への放射性物質の流出が防止できない。また、特許文献1に記載されている廃棄物等の焼却方法においては、放射性物質を含む廃材を焼却処理した場合に焼却炉内で濃縮される高濃度放射性物質の取扱いをすることができない。   However, in the method for incineration of wastes and the like described in Patent Document 1, it is not possible to prevent outflow of radioactive substances from the incinerator or the like into the environment. Moreover, in the incineration method of waste etc. described in patent document 1, when the waste material containing a radioactive substance is incinerated, the high concentration radioactive substance concentrated in an incinerator cannot be handled.

したがって、本発明の目的は、放射性物質を含む物質を燃焼処理した場合に環境中への放射性物質の流出を防止でき、また、廃材の焼却後に発生する高濃度放射性物質を適切に管理できる閉鎖系排煙処理システムを提供することにある。   Accordingly, an object of the present invention is to provide a closed system that can prevent outflow of radioactive material into the environment when a material containing radioactive material is burned, and can appropriately manage high-concentration radioactive material generated after incineration of waste materials. The object is to provide a flue gas treatment system.

本発明は、上記目的を達成するため、放射性物質を含む廃材の燃焼に伴い発生する燃焼ガス及び煙を含む排気ガスと廃材の燃焼により生じる焼却灰とを排出する燃焼部と、燃焼部から排出される排気ガスが移送される排気ガス移送路と、排気ガス移送路を移送してきた排気ガスが導入される吸引口と、排気ガスに接触させる水を当該水の導入部分における流速より早い流速で内部に供給し、内部に負の静圧を発生させる水供給口と、排気ガスと水とが混合した混合液が吐出される吐出口とを有するエジェクターと、吐出口から排出される混合液を水中に導入すると共に混合液と水とを混合する湿式サイクロンを有し、混合液と水とが混合された処理水を貯える水槽と、燃焼ガス及び煙に起因する固形物質を処理水から分離し、固形物質が取り除かれた処理済水をエジェクターに供給する水処理部と、燃焼部から排出される焼却灰を吸引し、焼却灰と吸引により生じる排出ガスとを分離し、焼却灰を回収容器に回収し、排出ガスをエジェクターの吸引口に向けて供給する焼却灰処理部とを備える閉鎖系排煙処理システムが提供される。
In order to achieve the above object, the present invention provides a combustion section for discharging exhaust gas containing combustion gas and smoke generated by combustion of waste materials containing radioactive materials and incineration ash generated by combustion of waste materials, and discharging from the combustion section. The exhaust gas transfer path through which the exhaust gas is transferred, the suction port into which the exhaust gas transferred through the exhaust gas transfer path is introduced, and the water to be brought into contact with the exhaust gas at a flow rate faster than the flow rate at the water introduction portion. An ejector having a water supply port for supplying inside and generating a negative static pressure inside, a discharge port for discharging a mixed liquid in which exhaust gas and water are mixed, and a mixed liquid discharged from the discharge port It has a wet cyclone that introduces into the water and mixes the mixed liquid and water, and separates the water tank that stores the treated water mixed with the mixed liquid and water from the treated water and the solid substances resulting from the combustion gas and smoke. , Solid matter takes The water treatment unit that supplies the treated water to the ejector and the incineration ash discharged from the combustion unit are sucked, the incineration ash and the exhaust gas generated by the suction are separated, and the incineration ash is collected in a collection container and discharged There is provided a closed-system flue gas treatment system including an incineration ash treatment unit that supplies gas toward a suction port of an ejector .

また、上記閉鎖系排煙処理システムにおいて、焼却灰処理部が、焼却灰処理部の後段の管を介し、エジェクターの吸引口に向けて排出ガスを供給し、水槽が、処理水を覆う蓋と、水槽の内部と水槽の外部とを連結する連結部とを有することもできる。
Further, in the above closed system flue gas treatment system, the incineration ash treatment unit supplies exhaust gas to the suction port of the ejector through the tube at the rear stage of the incineration ash treatment unit, and the water tank has a lid that covers the treated water. It can also have the connection part which connects the inside of a water tank, and the exterior of a water tank.

また、上記閉鎖系排煙処理システムにおいて、焼却灰処理部が、回収容器の入口を熱圧着で閉じることで、回収容器に回収された焼却灰を真空パックすることもできる。 In the above closed system flue gas treatment system, incineration ash processing unit, an inlet of the collection container at Rukoto closed with thermocompression bonding was recovered in the recovery container ash can also be vacuum-packed.

また、上記閉鎖系排煙処理システムにおいて、エジェクターの吸引口と排気ガス移送路との間に、水処理部からの処理済水が供給される処理済水供給口と、焼却灰処理部からの排出ガスが供給される排出ガス供給口と、排気ガス移送路から移送される排気ガスが供給される排気ガス供給口とを有する中間導入部を更に備え、吸引口に、中間導入部から処理済水、排出ガス、及び排気ガスが供給されることもできる。   Further, in the above closed system flue gas treatment system, a treated water supply port through which treated water from the water treatment unit is supplied between the suction port of the ejector and the exhaust gas transfer path, and an incineration ash treatment unit An intermediate introduction part having an exhaust gas supply port to which exhaust gas is supplied and an exhaust gas supply port to which exhaust gas transferred from the exhaust gas transfer path is supplied is further provided, and the suction port has been processed from the intermediate introduction part Water, exhaust gas and exhaust gas can also be supplied.

また、上記閉鎖系排煙処理システムにおいて、連結部が、水槽から微細な粒子が外部に放出することを防止するミストフィルタを含むこともできる。   Further, in the above closed system flue gas treatment system, the connecting portion may include a mist filter that prevents fine particles from being discharged from the water tank to the outside.

また、上記閉鎖系排煙処理システムにおいて、焼却灰処理部が、焼却灰と排出ガスとをサイクロンで分離することもできる。   Further, in the closed system flue gas treatment system, the incineration ash treatment unit can separate the incineration ash and the exhaust gas with a cyclone.

本発明に係る閉鎖系排煙処理システムによれば、放射性物質を含む物質を燃焼処理した場合に環境中への放射性物質の流出を防止でき、また、廃材の焼却後に発生する高濃度放射性物質を適切に管理できる閉鎖系排煙処理システムを提供できる。   According to the closed system flue gas treatment system according to the present invention, it is possible to prevent outflow of radioactive material into the environment when a material containing radioactive material is burned, and high-concentration radioactive material generated after incineration of waste materials. A closed flue gas treatment system that can be appropriately managed can be provided.

本発明の第1の実施の形態に係る閉鎖系排煙処理システムの概要図である。1 is a schematic diagram of a closed system flue gas treatment system according to a first embodiment of the present invention. 本発明の第2の実施の形態に係る閉鎖系排煙処理システムの概要図である。It is a schematic diagram of the closed system flue gas processing system which concerns on the 2nd Embodiment of this invention.

[第1の実施の形態]
図1は、本発明の第1の実施の形態に係る閉鎖系排煙処理システムの概要を示す。
[First Embodiment]
FIG. 1 shows an outline of a closed system flue gas treatment system according to a first embodiment of the present invention.

(閉鎖系排煙処理システム1の概要)
第1の実施の形態に係る閉鎖系排煙処理システム1は、放射性ヨウ素や放射性セシウム等の放射性物質を含む廃材の燃焼に伴い発生する燃焼ガス、煙、及び焼却灰等から放射性物質が環境中に放出されることを防止しつつ、燃焼ガス、煙、及び焼却灰を安全に分離して処理する。閉鎖系排煙処理システム1が処理する廃材は、例えば、放射性物質を含む樹木、木材等の木質系材料である。
(Outline of closed system flue gas treatment system 1)
The closed system flue gas treatment system 1 according to the first embodiment is configured so that radioactive substances are generated in the environment from combustion gas, smoke, incineration ash, and the like generated by burning waste materials containing radioactive substances such as radioactive iodine and radioactive cesium. Combustion gas, smoke, and incineration ash are safely separated and processed while preventing them from being released into the atmosphere. The waste material processed by the closed-system smoke treatment system 1 is, for example, a woody material such as a tree or wood containing a radioactive substance.

(閉鎖系排煙処理システム1の構成の概要)
閉鎖系排煙処理システム1は、放射性物質を含む廃材を燃焼する燃焼部10と、燃焼部10からの排気ガスを燃焼部10の外部に移送する排気ガス移送路12と、排気ガス移送路12の出口に接続され、排気ガスと水とを混合するエジェクター14と、エジェクター14から吐出される排気ガスと水とが混合した混合液を水中に導入し、処理水として蓄える水槽16と、処理水に含まれる固形物質と水とを分離する水処理部18と、少なくとも水槽16に貯えられている処理水の一部をエジェクター14に供給する水ポンプ32と、燃焼部10から排出される焼却灰を回収容器210に自動的に密封する焼却灰処理部20と、焼却灰処理部20の後段に設置され、焼却灰処理部20内の回収容器210内に向けて焼却灰を吸引する排気ポンプ30とを備える。
(Outline of configuration of closed system flue gas treatment system 1)
The closed system flue gas treatment system 1 includes a combustion unit 10 that burns a waste material containing a radioactive substance, an exhaust gas transfer channel 12 that transfers exhaust gas from the combustion unit 10 to the outside of the combustion unit 10, and an exhaust gas transfer channel 12. An ejector 14 that mixes exhaust gas and water, a water tank 16 that introduces into the water a mixture of exhaust gas and water discharged from the ejector 14, and stores the treated water as treated water; The water treatment part 18 which isolate | separates the solid substance contained in water and water, the water pump 32 which supplies at least one part of the treated water stored in the water tank 16 to the ejector 14, and the incineration ash discharged | emitted from the combustion part 10 Incineration ash processing unit 20 that automatically seals the incineration ash to the recovery container 210 and an exhaust pump that is installed downstream of the incineration ash processing unit 20 and sucks the incineration ash toward the recovery container 210 in the incineration ash processing unit 20 0 and a.

(燃焼部10)
燃焼部10は、放射性物質を含む廃材を燃焼する。そして燃焼部10は、廃材の燃焼に伴い発生する燃焼ガス及び煙を含む排気ガスと廃材の燃焼により生じる焼却灰とを排出する。ここで燃焼部10には、燃焼部10から排出される排気ガスを移送する排気ガス移送路12が接続されている。排気ガス移送路12は、エジェクター14に向けて排気ガスを移送する。一方、焼却灰は、エクストローダ220を用いて焼却灰処理部20に一定量ずつ供給される。なお、燃焼部10は、廃棄物を焼却する設備であれば、固定炉等の様々な形式の焼却炉を用いることができる。
(Combustion unit 10)
The combustion unit 10 burns a waste material containing a radioactive substance. And the combustion part 10 discharges | emits the exhaust gas containing combustion gas and smoke which generate | occur | produce with combustion of waste materials, and the incineration ash which arises by combustion of waste materials. Here, an exhaust gas transfer path 12 that transfers exhaust gas discharged from the combustion unit 10 is connected to the combustion unit 10. The exhaust gas transfer path 12 transfers the exhaust gas toward the ejector 14. On the other hand, the incineration ash is supplied to the incineration ash processing unit 20 by a certain amount using the extloader 220. In addition, if the combustion part 10 is an installation which incinerates a waste, various types of incinerators, such as a fixed furnace, can be used.

(エジェクター14)
エジェクター14は、流体及び/又は固体が導入又は排出される少なくとも三つの口を有する。具体的にエジェクター14は、流体である水が供給される第一の口と、流体及び/又は固体を吸引する第二の口と、第一の口に供給された水及び第二の口が吸引した流体及び/又は固体を吐出する第三の口とを有する。第一の口は、外部から導入された水を導入部分における当該水の流速より早い流速でエジェクター14内部に供給する。例えば、第一の口は、一方の端から他方の端に向けて徐々に断面径が狭まる形状を有する経路を後段に含む。
(Ejector 14)
The ejector 14 has at least three ports through which fluid and / or solids are introduced or discharged. Specifically, the ejector 14 includes a first port to which water that is a fluid is supplied, a second port that sucks fluid and / or solids, and water and a second port that are supplied to the first port. And a third port for discharging the sucked fluid and / or solid. The first port supplies water introduced from the outside into the ejector 14 at a flow rate faster than the flow rate of the water in the introduction portion. For example, the first port includes a path having a shape in which the cross-sectional diameter gradually decreases from one end toward the other end.

そして、第一の口から所定の流速を超える流速でエジェクター14内部に導入された水により、エジェクター14内部には負の静圧が発生する。第二の口は、発生した負の静圧を利用して流体及び/又は固体を吸引し、第三の口は、第一の口から供給された水と第二の口が吸引した流体及び/又は固体とを吐出する。エジェクター14は、耐蝕性、耐熱性、機械的特性等に優れた材料を用いて構成することができ、例えば、SUS等の金属材料を用いて構成することができる。   And the negative static pressure generate | occur | produces in the inside of the ejector 14 with the water introduce | transduced into the inside of the ejector 14 with the flow velocity exceeding predetermined | prescribed flow velocity from the 1st opening | mouth. The second port uses the generated negative static pressure to suck fluid and / or solid, and the third port uses water supplied from the first port and fluid sucked by the second port and And / or discharging solids. The ejector 14 can be configured using a material excellent in corrosion resistance, heat resistance, mechanical characteristics, and the like, and can be configured using a metal material such as SUS, for example.

より具体的にエジェクター14は、排気ガス移送路12を移送してきた排気ガスが導入される吸引口14aと、排気ガスに接触させる水であってエジェクター14内部に負の静圧を発生させる水が供給される水供給口14bと、排気ガスと水とが混合した混合液が吐出される吐出口14cとを有する。混合液は吐出口14cから水槽16に供給される。   More specifically, the ejector 14 includes a suction port 14a into which exhaust gas transferred through the exhaust gas transfer path 12 is introduced, and water that is brought into contact with the exhaust gas and generates negative static pressure inside the ejector 14. It has a water supply port 14b to be supplied and a discharge port 14c from which a mixed liquid in which exhaust gas and water are mixed is discharged. The mixed liquid is supplied to the water tank 16 from the discharge port 14c.

(水槽16)
水槽16は、吐出口14cから吐出される混合液が水中に導入され、混合液と水とが混合して生じる処理水168を蓄える。具体的に水槽16は、吐出口14cからの混合液を水槽16内に導入すると共に混合液と水とを水中で混合する混合液導入部160を有し、混合液導入部160が混合液と水とを混合して処理水168にする。ここで、混合液導入部160としては、混合液中に含まれる固形物質を混合液から水槽16中に離脱させるだけでなく、混合液と水槽16の水とを混合する湿式サイクロンを用いることができる。混合液導入部160は、混合液を吐出口14cから水槽16中にそのまま導入する場合に比べて混合液と水との接触時間を長くできる。また、水槽16は、処理水168の上方を覆う蓋162と、水槽16の内部と水槽16の外部とを連結する大気の流通経路としての連結部164とを有する。そして、連結部164は、水槽16の内部と水槽16の外部との間に水槽16から微細な粒子が外部に放出することを防止するミストフィルタ166を有する。
(Water tank 16)
The water tank 16 stores treated water 168 produced by mixing the liquid mixture and water into which the liquid mixture discharged from the discharge port 14c is introduced. Specifically, the water tank 16 has a liquid mixture introduction section 160 that introduces the liquid mixture from the discharge port 14 c into the water tank 16 and mixes the liquid mixture and water in water, and the liquid mixture introduction section 160 includes the liquid mixture and the liquid mixture. Mix with water to make treated water 168. Here, as the mixed liquid introducing section 160, not only the solid substance contained in the mixed liquid is separated from the mixed liquid into the water tank 16, but also a wet cyclone that mixes the mixed liquid and the water in the water tank 16 is used. it can. The mixed liquid introducing unit 160 can increase the contact time between the mixed liquid and water as compared with the case where the mixed liquid is introduced into the water tank 16 as it is from the discharge port 14c. In addition, the water tank 16 includes a lid 162 that covers the upper side of the treated water 168, and a connecting portion 164 as an air circulation path that connects the inside of the water tank 16 and the outside of the water tank 16. And the connection part 164 has the mist filter 166 which prevents that a micro particle | grain is discharge | released outside from the water tank 16 between the inside of the water tank 16 and the exterior of the water tank 16. FIG.

(水処理部18)
水処理部18は、水槽16に貯えられている処理水168を吸い上げ、処理水168に含まれている固形物質を処理水168から分離する。ここで固形物質は、燃焼ガス及び煙に起因する放射性物質を含有するスス等である。そして水処理部18は、管182を介して固形物質が取り除かれた処理済水を水ポンプ32に供給する。水ポンプ32は、この処理済水をエジェクター14の水供給口14bに供給する。また水処理部18は、処理水168が導入される一方の端部と処理済水が排出される他方の端部との間にフィルター180を有する。水処理部18は、このフィルター180を用いて処理水168に含まれる固形物質を捕集する。フィルター180としては、例えば、濾紙を用いることができる。
(Water treatment unit 18)
The water treatment unit 18 sucks up the treated water 168 stored in the water tank 16 and separates the solid substance contained in the treated water 168 from the treated water 168. Here, the solid substance is soot containing radioactive substances caused by combustion gas and smoke. Then, the water treatment unit 18 supplies treated water from which the solid substance has been removed via the pipe 182 to the water pump 32. The water pump 32 supplies the treated water to the water supply port 14b of the ejector 14. Further, the water treatment unit 18 has a filter 180 between one end where the treated water 168 is introduced and the other end where the treated water is discharged. The water treatment unit 18 collects the solid material contained in the treated water 168 using the filter 180. For example, filter paper can be used as the filter 180.

ここで水ポンプ32は、水槽16内の水若しくは処理水168の少なくとも一部を吸引する。また、水ポンプ32は、水処理部18から処理済水を吸引する。そして、水ポンプ32は、吸引した処理済水と吸引した水とをエジェクター14の水供給口14bに供給する。   Here, the water pump 32 sucks at least a part of the water in the water tank 16 or the treated water 168. Further, the water pump 32 sucks the treated water from the water treatment unit 18. The water pump 32 supplies the sucked treated water and the sucked water to the water supply port 14b of the ejector 14.

(焼却灰処理部20)
焼却灰処理部20は、エクストローダ220を用いて燃焼部10から排出される焼却灰を受け取る。そして、焼却灰処理部20は、減圧下で回収容器210に焼却灰を回収する。この場合において焼却灰処理部20は、回収容器210内を減圧状態にすることを目的として回収容器210内を吸引するときに生じる排出ガスと焼却灰とをサイクロン200を用いて分離する。
(Incineration ash treatment unit 20)
The incineration ash processing unit 20 receives the incineration ash discharged from the combustion unit 10 using the extloader 220. Then, the incineration ash processing unit 20 collects the incineration ash in the collection container 210 under reduced pressure. In this case, the incineration ash processing unit 20 uses the cyclone 200 to separate exhaust gas and incineration ash that are generated when the inside of the recovery container 210 is sucked for the purpose of reducing the pressure in the recovery container 210.

そして、焼却灰処理部20は、回収容器210に焼却灰を回収すると共に、焼却灰処理部20の後段に設けられる排気ポンプ30から管300を介してエジェクター14の吸引口14aに向けて排出ガスを供給する。また、焼却灰処理部20は、回収容器210の入口である開口を自動的に閉じて、回収容器210に回収された焼却灰を密封する。なお、焼却灰処理部20は、回収容器210から放射される放射線量を測定する放射線検出部を更に有することができる。この場合、焼却灰処理部20は、放射線量を測定する放射線検出部と、放射線検出部が予め定められた放射線量を検出した場合に発する信号に応じて作業者にアラームを発する報知部とを含む放射線検出ユニットを有することができる。   The incineration ash processing unit 20 collects the incineration ash in the recovery container 210 and exhausts gas from the exhaust pump 30 provided at the rear stage of the incineration ash processing unit 20 toward the suction port 14a of the ejector 14 through the pipe 300. Supply. Further, the incineration ash processing unit 20 automatically closes the opening that is the inlet of the recovery container 210 and seals the incineration ash recovered in the recovery container 210. Note that the incineration ash treatment unit 20 may further include a radiation detection unit that measures the amount of radiation emitted from the collection container 210. In this case, the incineration ash processing unit 20 includes a radiation detection unit that measures the radiation dose, and a notification unit that issues an alarm to the worker in response to a signal that is emitted when the radiation detection unit detects a predetermined radiation dose. A radiation detection unit can be included.

例えば、焼却灰処理部20は、回収容器210を保持する容器保持部と、エクストローダ220からの焼却灰を回収容器210内に導入する導入部(例えば、サイクロン装置)と、回収容器210を密封する密封部とを有する。また、回収容器210は、例えば、ポリエチレン等からなる回収パックである。焼却灰処理部20は、容器保持部に保持されている回収パック内に導入される焼却灰が予め定められた量に達するごとに、回収パックの口を密封部に熱圧着させる。これにより焼却灰処理部20は、回収パックを真空パックする。   For example, the incineration ash processing unit 20 seals the collection container 210, a container holding unit that holds the collection container 210, an introduction unit (for example, a cyclone device) that introduces the incineration ash from the extloader 220 into the collection container 210, and the recovery container 210. And a sealing portion. The collection container 210 is a collection pack made of, for example, polyethylene. The incineration ash processing unit 20 thermocompresses the opening of the recovery pack to the sealing unit every time the incineration ash introduced into the recovery pack held in the container holding unit reaches a predetermined amount. Thereby, the incineration ash processing unit 20 vacuum-packs the collection pack.

(第1の実施の形態の効果)
第1の実施の形態に係る閉鎖系排煙処理システム1は、放射性物質を含む廃材の燃焼により発生する排気ガスをエジェクター14において水と混合させて混合液にし、この混合液を水槽16の水に混合させて処理水168にした後、処理水168に含まれる放射性物質を含む固形物質を水処理部18において捕集する。そして、固形物質が取り除かれた処理済水は再びエジェクター14に戻される。更に、焼却灰は焼却灰処理部20において回収容器210に回収され、回収に伴い生じる排出ガスは排気ポンプ30によってエジェクター14に戻される。
(Effects of the first embodiment)
In the closed-system flue gas treatment system 1 according to the first embodiment, exhaust gas generated by combustion of waste materials containing radioactive substances is mixed with water in an ejector 14 to form a mixed solution. The solid material containing the radioactive material contained in the treated water 168 is collected in the water treatment unit 18. Then, the treated water from which the solid substance has been removed is returned to the ejector 14 again. Further, the incineration ash is collected in the collection container 210 in the incineration ash processing unit 20, and the exhaust gas generated by the collection is returned to the ejector 14 by the exhaust pump 30.

したがって、本実施の形態に係る閉鎖系排煙処理システム1によれば、放射性物質を含む廃材の燃焼により発生する放射性物質を含む排気ガスや焼却灰を閉鎖系排煙処理システム1内で処理して管理できるので、放射性物質を含む排気ガスや焼却灰が環境中に放出されることを防止できる。すなわち、閉鎖系排煙処理システム1は、廃棄物の処理過程において環境中に排出される放射性物質を大幅に低減若しくはなくすことができ、排気ガスや焼却灰を安全に処理できる。また、閉鎖系排煙処理システム1は、閉鎖系排煙処理システム1内において処理済水を循環して再利用できるので、廃材の処理に伴って外部から新たに水を供給し続けることを抑制できる。   Therefore, according to the closed system flue gas treatment system 1 according to the present embodiment, exhaust gas and incineration ash containing radioactive substances generated by combustion of waste materials containing radioactive substances are treated in the closed system flue gas treatment system 1. As a result, it is possible to prevent exhaust gas containing radioactive materials and incineration ash from being released into the environment. That is, the closed system flue gas treatment system 1 can significantly reduce or eliminate radioactive substances discharged into the environment during the waste treatment process, and can safely treat exhaust gas and incineration ash. Further, since the closed-system smoke treatment system 1 can circulate and reuse the treated water in the closed-system smoke treatment system 1, it suppresses the continuous supply of new water from the outside as the waste material is treated. it can.

また、閉鎖系排煙処理システム1によれば、混合液導入部160が水槽16中に混合液をそのまま導入する場合に比べて混合液と水との接触時間を長くすることができるので、エジェクター14から供給されてくる混合液に含まれる排気ガスを水で効率的に洗浄することができる。   Further, according to the closed system flue gas treatment system 1, the contact time between the mixed liquid and water can be increased compared with the case where the mixed liquid introducing unit 160 introduces the mixed liquid into the water tank 16 as it is, so the ejector The exhaust gas contained in the mixed solution supplied from 14 can be efficiently washed with water.

更に閉鎖系排煙処理システム1によれば、放射性物質が濃縮された焼却灰を焼却灰処理部20において回収容器210に自動的に無人で密封できるので、作業者の内部被ばくを防止でき、また、放射性物質を含む廃材の燃焼により減量濃縮された放射性物質を含む焼却灰の全量を高濃度放射性廃棄物として容易に管理できる。   Furthermore, according to the closed system flue gas treatment system 1, the incineration ash enriched with radioactive substances can be automatically and unmannedly sealed in the recovery container 210 in the incineration ash treatment unit 20, thereby preventing the internal exposure of the worker, In addition, the entire amount of incinerated ash containing radioactive material that has been reduced and concentrated by combustion of waste materials containing radioactive material can be easily managed as high-concentration radioactive waste.

また、本実施の形態に係る閉鎖系排煙処理システム1は、排気ガス移送路12、エジェクター14、混合液導入部160を有する水槽16、水処理部18、及び焼却灰処理部20等を燃焼部10の周囲に設置することで構成できるので、燃焼部10のタイプによらず本実施の形態に係る閉鎖系排煙処理システム1を容易に構成できる。   Further, the closed system flue gas treatment system 1 according to the present embodiment combusts the exhaust gas transfer path 12, the ejector 14, the water tank 16 having the mixed liquid introduction unit 160, the water treatment unit 18, the incineration ash treatment unit 20, and the like. Since it can comprise by installing around the part 10, the closed system flue gas treatment system 1 which concerns on this Embodiment can be comprised easily irrespective of the type of the combustion part 10. FIG.

[第2の実施の形態]
図2は、本発明の第2の実施の形態に係る閉鎖系排煙処理システムの概要を示す。
[Second Embodiment]
FIG. 2 shows an outline of a closed system flue gas treatment system according to the second embodiment of the present invention.

第2の実施の形態に係る閉鎖系排煙処理システム1aは、排気ガス移送路12とエジェクター14との間に中間導入部40を更に備える点を除き、第1の実施の形態に係る閉鎖系排煙処理システム1と略同一の構成及び機能を備える。したがって、相違点を除き詳細な説明は省略する。   The closed system flue gas treatment system 1a according to the second embodiment is a closed system according to the first embodiment except that an intermediate introduction part 40 is further provided between the exhaust gas transfer path 12 and the ejector 14. It has substantially the same configuration and function as the flue gas treatment system 1. Therefore, a detailed description is omitted except for differences.

中間導入部40は、排気ガス移送路12とエジェクター14の吸引口14aとの間に設置される。中間導入部40は、水処理部18からの処理済水が管182aを介して供給される処理済水供給口40bと、焼却灰処理部20からの排出ガスが管300a供給される排出ガス供給口40cと、排気ガス移送路12を移送してくる排気ガスが供給される排気ガス供給口40aとを有する。そして、中間導入部40に供給された処理済水、排出ガス、及び排気ガスは中間導入部40内で合流し、出口40dからエジェクター14の吸引口14aにまとめて供給される。   The intermediate introduction part 40 is installed between the exhaust gas transfer path 12 and the suction port 14 a of the ejector 14. The intermediate introduction unit 40 includes a treated water supply port 40b through which treated water from the water treatment unit 18 is supplied via a pipe 182a, and an exhaust gas supply through which exhaust gas from the incineration ash treatment unit 20 is supplied to the pipe 300a. It has a port 40c and an exhaust gas supply port 40a to which the exhaust gas transferred through the exhaust gas transfer path 12 is supplied. Then, the treated water, the exhaust gas, and the exhaust gas supplied to the intermediate introduction unit 40 merge in the intermediate introduction unit 40 and are collectively supplied from the outlet 40d to the suction port 14a of the ejector 14.

なお、中間導入部40の内部と排気ガス供給口40aとの間、中間導入部40の内部と処理済水供給口40bとの間、及び中間導入部40の内部と排出ガス供給口40cとの間のそれぞれに、それぞれを流れる流体の流量を調節するバルブ(例えば、ボールバルブ)を設けることもできる。また、排気ガス供給口40aと排気ガス移送路12との間には、排気ガス移送路12の終端から排気ガス供給口40aの入口まで徐々に断面径が狭まる形状のリデューサーを挟むこともできる。   In addition, between the inside of the intermediate introduction part 40 and the exhaust gas supply port 40a, between the inside of the intermediate introduction part 40 and the treated water supply port 40b, and between the inside of the intermediate introduction part 40 and the exhaust gas supply port 40c. A valve (for example, a ball valve) for adjusting the flow rate of the fluid flowing through each of the fluids may be provided between the two. Further, a reducer having a shape in which the cross-sectional diameter gradually decreases from the end of the exhaust gas transfer path 12 to the inlet of the exhaust gas supply port 40a can be sandwiched between the exhaust gas supply port 40a and the exhaust gas transfer path 12.

(第2の実施の形態の効果)
第2の実施の形態に係る閉鎖系排煙処理システム1aによれば、水処理部18から排出される処理済水と焼却灰処理部20から排出される排出ガスとが中間導入部40において排気ガスと合流し、中間導入部40を介してエジェクター14の吸引口14aにまとめて供給されるので、放射性物質をより効率的に水槽16中に送ることができる。
(Effect of the second embodiment)
According to the closed system flue gas treatment system 1a according to the second embodiment, the treated water discharged from the water treatment unit 18 and the exhaust gas discharged from the incineration ash treatment unit 20 are exhausted in the intermediate introduction unit 40. Since it merges with the gas and is collectively supplied to the suction port 14a of the ejector 14 via the intermediate introduction part 40, the radioactive substance can be sent into the water tank 16 more efficiently.

以上、本発明の実施の形態を説明したが、上記に記載した実施の形態は特許請求の範囲に係る発明を限定するものではない。また、実施の形態の中で説明した特徴の組合せのすべてが発明の課題を解決するための手段に必須であるとは限らない。   While the embodiments of the present invention have been described above, the embodiments described above do not limit the invention according to the claims. In addition, not all the combinations of features described in the embodiments are essential to the means for solving the problems of the invention.

1、1a 閉鎖系排煙処理システム
10 燃焼部
12 排気ガス移送路
14 エジェクター
14a 吸引口
14b 水供給口
14c 吐出口
16 水槽
18 水処理部
20 焼却灰処理部
30 排気ポンプ
32 水ポンプ
40 中間導入部
40a 排気ガス供給口
40b 処理済水供給口
40c 排出ガス供給口
40d 出口
160 混合液導入部
162 蓋
164 連結部
166 ミストフィルタ
168 処理水
180 フィルター
182、182a 管
200 サイクロン
210 回収容器
220 エクストローダ
300、300a 管
DESCRIPTION OF SYMBOLS 1, 1a Closed system flue gas treatment system 10 Combustion part 12 Exhaust gas transfer path 14 Ejector 14a Suction port 14b Water supply port 14c Discharge port 16 Water tank 18 Water treatment part 20 Incineration ash treatment part 30 Exhaust pump 32 Water pump 40 Intermediate introduction part 40a Exhaust gas supply port 40b Treated water supply port 40c Exhaust gas supply port 40d Outlet 160 Mixed liquid introduction part 162 Lid 164 Connection part 166 Mist filter 168 Treated water 180 Filter 182, 182a Pipe 200 Cyclone 210 Recovery container 220 Extruder 300, 300a tube

Claims (6)

放射性物質を含む廃材の燃焼に伴い発生する燃焼ガス及び煙を含む排気ガスと前記廃材の燃焼により生じる焼却灰とを排出する燃焼部と、
前記燃焼部から排出される前記排気ガスが移送される排気ガス移送路と、
前記排気ガス移送路を移送してきた前記排気ガスが導入される吸引口と、前記排気ガスに接触させる水を当該水の導入部分における流速より早い流速で内部に供給し、前記内部に負の静圧を発生させる水供給口と、前記排気ガスと前記水とが混合した混合液が吐出される吐出口とを有するエジェクターと、
前記吐出口から排出される前記混合液を水中に導入すると共に前記混合液と水とを混合する湿式サイクロンを有し、前記混合液と前記水とが混合された処理水を貯える水槽と、
前記燃焼ガス及び前記煙に起因する固形物質を前記処理水から分離し、前記固形物質が取り除かれた処理済水を前記エジェクターに供給する水処理部と、
前記燃焼部から排出される前記焼却灰を吸引し、前記焼却灰と前記吸引により生じる排出ガスとを分離し、前記焼却灰を回収容器に回収し、前記排出ガスを前記エジェクターの前記吸引口に向けて供給する焼却灰処理部と
を備える閉鎖系排煙処理システム。
A combustion section for discharging exhaust gas containing combustion gas and smoke generated along with combustion of waste material containing radioactive material and incineration ash generated by combustion of the waste material;
An exhaust gas transfer path through which the exhaust gas discharged from the combustion section is transferred;
A suction port through which the exhaust gas transferred through the exhaust gas transfer path is introduced, and water to be brought into contact with the exhaust gas are supplied to the inside at a flow rate faster than the flow rate at the introduction portion of the water. An ejector having a water supply port for generating pressure, and a discharge port from which a mixed liquid in which the exhaust gas and the water are mixed is discharged;
A wet tank that introduces the mixed liquid discharged from the discharge port into the water and mixes the mixed liquid and water, and a water tank for storing treated water in which the mixed liquid and the water are mixed;
A water treatment unit for separating the solid material resulting from the combustion gas and the smoke from the treated water, and supplying treated water from which the solid material has been removed to the ejector;
The incineration ash discharged from the combustion section is sucked, the incineration ash and the exhaust gas generated by the suction are separated, the incineration ash is recovered in a recovery container, and the exhaust gas is supplied to the suction port of the ejector A closed-system flue gas treatment system comprising an incineration ash treatment unit that is supplied toward the factory.
前記焼却灰処理部が、前記焼却灰処理部の後段の管を介し、前記エジェクターの前記吸引口に向けて前記排出ガスを供給し、
記水槽が、前記処理水を覆う蓋と、前記水槽の内部と前記水槽の外部とを連結する連結部とを有する請求項1に記載の閉鎖系排煙処理システム。
The incineration ash treatment unit supplies the exhaust gas toward the suction port of the ejector via a tube at the rear stage of the incineration ash treatment unit,
Closed system flue gas treatment system according to claim 1 having pre Symbol aquarium, a lid covering the treated water, and a connecting portion for connecting the exterior of the internal and the water tank of the water tub.
前記焼却灰処理部が、前記回収容器の入口を熱圧着で閉じることで、前記回収容器に回収された前記焼却灰を真空パックする請求項2に記載の閉鎖系排煙処理システム。 The incineration ash processing unit, a closed system flue gas treatment system according to claim 2, the inlet of the collecting container Rukoto closed by thermal bonding, vacuum packed the ash collected in the said collection container. 前記エジェクターの前記吸引口と前記排気ガス移送路との間に、前記水処理部からの前記処理済水が供給される処理済水供給口と、前記焼却灰処理部からの前記排出ガスが供給される排出ガス供給口と、前記排気ガス移送路から移送される前記排気ガスが供給される排気ガス供給口とを有する中間導入部
を更に備え、
前記吸引口に、前記中間導入部から前記処理済水、前記排出ガス、及び前記排気ガスが供給される請求項3に記載の閉鎖系排煙処理システム。
Between the suction port of the ejector and the exhaust gas transfer path, the treated water supply port to which the treated water from the water treatment unit is supplied and the exhaust gas from the incineration ash treatment unit are supplied. An intermediate introduction part having an exhaust gas supply port to be supplied and an exhaust gas supply port to which the exhaust gas transferred from the exhaust gas transfer path is supplied,
The closed-system smoke treatment system according to claim 3, wherein the treated water, the exhaust gas, and the exhaust gas are supplied to the suction port from the intermediate introduction unit.
前記連結部が、前記水槽から微細な粒子が外部に放出することを防止するミストフィルタを含む請求項4に記載の閉鎖系排煙処理システム。   The closed system flue gas treatment system according to claim 4, wherein the connecting portion includes a mist filter that prevents fine particles from being discharged to the outside from the water tank. 前記焼却灰処理部が、前記焼却灰と前記排出ガスとをサイクロンで分離する請求項5に記載の閉鎖系排煙処理システム。
The closed-system smoke treatment system according to claim 5, wherein the incineration ash treatment unit separates the incineration ash and the exhaust gas with a cyclone.
JP2012096126A 2012-04-19 2012-04-19 Closed system flue gas treatment system Expired - Fee Related JP5954704B2 (en)

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