JP2013086087A5 - - Google Patents
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- JP2013086087A5 JP2013086087A5 JP2011232502A JP2011232502A JP2013086087A5 JP 2013086087 A5 JP2013086087 A5 JP 2013086087A5 JP 2011232502 A JP2011232502 A JP 2011232502A JP 2011232502 A JP2011232502 A JP 2011232502A JP 2013086087 A5 JP2013086087 A5 JP 2013086087A5
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- exhaust gas
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上記目的を達成するため、本発明は、燃焼排ガス処理装置であって、燃焼排ガス中のダストを集塵する電気集塵機と、該電気集塵機を通過した排ガス中のNOx又は/及びダイオキシン類を分解除去すると共に、該排ガス中の金属水銀を酸化する触媒装置と、該触媒装置を通過した排ガス中の水溶性成分、ダスト及び水分を捕集する湿式集塵機とを備えることを特徴とする。 In order to achieve the above object, the present invention is a flue gas treatment apparatus, which is an electric dust collector that collects dust in flue gas and NOx and / or dioxins in the flue gas that has passed through the electric dust collector and characterized removed by be Rutotomoni, catalyst and medium system you oxidizing the metal mercury in exhaust gas, a water-soluble components in the exhaust gas which has passed through the 該触 medium apparatus, further comprising a wet dust collector for collecting dust and moisture To do.
そして、本発明によれば、電気集塵機を用いることで集塵機の維持費を低く抑えることができる。また、バグフィルタを用いた場合、燃焼排ガスに含まれている塩化水素がバグフィルタのろ過層で吸着されて下流側に行き着かないが、電気集塵機を用いることで、燃焼排ガスに含まれている塩化水素を触媒装置に導入することができるため、触媒装置で排ガス中のNOx又は/及びダイオキシン類を分解除去するだけでなく、触媒存在下で塩化水素を用いることにより、排ガスに含まれる金属水銀を、捕捉・除去が容易な塩化水銀に変換することができ、水銀、NOx、ダイオキシン類等の有害物質を効率よく低コストで除去することができる。 And according to this invention, the maintenance cost of a dust collector can be restrained low by using an electric dust collector. In addition, when a bag filter is used, hydrogen chloride contained in the combustion exhaust gas is adsorbed by the filter layer of the bag filter and does not reach the downstream side, but it is contained in the combustion exhaust gas by using an electric dust collector. it is possible to introduce a medium apparatus tactile hydrogen chloride, not only to decompose and remove the NOx and / or dioxins in the exhaust gas in the catalytic unit, by using hydrogen chloride in medium presence touch, contained in the exhaust gas Metal mercury can be converted into mercury chloride that can be easily captured and removed, and harmful substances such as mercury, NOx, and dioxins can be efficiently and inexpensively removed.
上記燃焼排ガス処理装置において、前記触媒装置で使用される触媒を、チタン・バナジウム系触媒とすることができる。 In the combustion exhaust gas treatment apparatus, a catalyst used in the previous Kisawa medium device may be a titanium-vanadium catalyst.
上記燃焼排ガス処理装置に、前記触媒装置を通過した排ガスに酸化剤を添加する酸化剤添加装置を設けることで、触媒装置で酸化しきれなかった金属水銀の酸化を補うことができる。 In the combustion exhaust gas treatment apparatus, before Kisawa medium device by the provision of the oxidizing agent addition device for adding an oxidizing agent to the exhaust gas which has passed through, it is possible to compensate for oxidation has not been oxidized in catalytic device metallic mercury.
上記燃焼排ガス処理装置において、前記燃焼排ガスをセメントキルン排ガスとすることができ、セメントキルン排ガス中の水銀、NOx、ダイオキシン類等の有害物質を効率よく低コストで除去することが可能となる。
また、前記触媒装置を、前記電気集塵機を通過した排ガス中のNOx又は/及びダイオキシン類を分解除去する第1触媒装置と、該第1触媒装置を通過した排ガス中に残存するダイオキシン類を分解除去すると共に、金属水銀を酸化する第2触媒装置とすることができる。
さらに、前記第1触媒装置を通過した排ガスに塩化水素を添加する塩化水素添加装置を設けることができる。これによって、燃焼排ガスに含まれていた塩化水素が脱硝剤のアンモニアと反応して塩化アンモニウムが生成され、第2触媒装置に導入される塩化水素の量が充分でない場合に容易に対応することができる。
In the above-described combustion exhaust gas treatment device, the combustion exhaust gas can be used as cement kiln exhaust gas, and harmful substances such as mercury, NOx, dioxins and the like in the cement kiln exhaust gas can be efficiently removed at low cost.
Further, the catalyst device includes a first catalyst device that decomposes and removes NOx and / or dioxins in the exhaust gas that has passed through the electrostatic precipitator, and decomposes and removes dioxins remaining in the exhaust gas that has passed through the first catalyst device. In addition, a second catalytic device that oxidizes metallic mercury can be obtained.
Furthermore, a hydrogen chloride addition device for adding hydrogen chloride to the exhaust gas that has passed through the first catalyst device can be provided. As a result, hydrogen chloride contained in the combustion exhaust gas reacts with ammonia of the denitration agent to produce ammonium chloride, which can easily cope with the case where the amount of hydrogen chloride introduced into the second catalytic device is not sufficient. it can.
また、本発明は、燃焼排ガス処理方法であって、燃焼排ガス中のダストを集塵し、該ダスト集塵後の排ガス中のNOx又は/及びダイオキシン類を触媒を用いて分解除去すると共に、該排ガス中の金属水銀を触媒を用いて酸化し、該金属水銀酸化後の排ガス中の水溶性成分、ダスト及び水分を湿式集塵することを特徴とする。 Further, the present invention provides a flue gas treatment method, and the dust collecting dust in the combustion exhaust gas, Rutotomoni to be partial de-using a catalyst of NOx and / or dioxins in exhaust gas after the dust collector The metal mercury in the exhaust gas is oxidized using a catalyst, and water-soluble components, dust, and moisture in the exhaust gas after the metal mercury oxidation are wet collected.
Claims (17)
該電気集塵機を通過した排ガス中のNOx又は/及びダイオキシン類を分解除去すると共に、該排ガス中の金属水銀を酸化する触媒装置と、
該触媒装置を通過した排ガス中の水溶性成分、ダスト及び水分を捕集する湿式集塵機とを備えることを特徴とする燃焼排ガス処理装置。 An electric dust collector that collects dust in the combustion exhaust gas,
Electric dust collector to be removed by partial release the NOx and / or dioxins in the exhaust gas that has passed through Rutotomoni, catalyst and medium system you oxidizing the metal mercury in exhaust gas,
Water-soluble components in the exhaust gas which has passed through the 該触 medium device, a combustion exhaust gas treatment apparatus, characterized in that it comprises a wet dust collector for collecting dust and moisture.
該固液分離機で分離されたろ液中の水銀を吸着する水銀除去装置とを備えることを特徴とする請求項1乃至5のいずれかに記載の燃焼排ガス処理装置。 A solid-liquid separator for solid-liquid separation of the slurry discharged from the wet dust collector;
A combustion exhaust gas treatment device according to any one of claims 1 to 5 , further comprising a mercury removal device that adsorbs mercury in the filtrate separated by the solid-liquid separator.
該第1触媒装置を通過した排ガス中に残存するダイオキシン類を分解除去すると共に、金属水銀を酸化する第2触媒装置であることを特徴とする請求項1乃至7のいずれかに記載の燃焼排ガス処理装置。The combustion exhaust gas according to any one of claims 1 to 7, which is a second catalyst device that decomposes and removes dioxins remaining in the exhaust gas that has passed through the first catalyst device and oxidizes metallic mercury. Processing equipment.
該ダスト集塵後の排ガス中のNOx又は/及びダイオキシン類を触媒を用いて分解除去すると共に、該排ガス中の金属水銀を触媒を用いて酸化し、
該金属水銀酸化後の排ガス中の水溶性成分、ダスト及び水分を湿式集塵することを特徴とする燃焼排ガス処理方法。 Collecting dust in the flue gas,
The NOx and / or dioxins in exhaust gas after the dust collector Rutotomoni to be removed by partial release using a catalyst, the metal mercury in exhaust gas is oxidized using a catalyst,
A method for treating combustion exhaust gas, comprising wet-collecting water-soluble components, dust and moisture in the exhaust gas after oxidation of the metal mercury.
該固液分離で分離されたろ液中の水銀を吸着することを特徴とする請求項10乃至15のいずれかに記載の燃焼排ガス処理方法。 Solid-liquid separation of the slurry obtained by the wet dust collection,
The combustion exhaust gas treatment method according to any one of claims 10 to 15, wherein mercury in the filtrate separated by the solid-liquid separation is adsorbed.
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JP6236653B2 (en) * | 2013-05-16 | 2017-11-29 | 学校法人福岡大学 | Incineration ash stabilization method and apparatus |
JP2015058397A (en) * | 2013-09-19 | 2015-03-30 | 太平洋セメント株式会社 | Processing system and method of cement kiln waste gas |
JP6344850B2 (en) * | 2014-07-23 | 2018-06-20 | 太平洋セメント株式会社 | Cement kiln exhaust gas treatment apparatus and treatment method |
JP2016022439A (en) * | 2014-07-23 | 2016-02-08 | 太平洋セメント株式会社 | Cement kiln exhaust gas treatment apparatus and treatment method |
JP2017057122A (en) * | 2015-09-18 | 2017-03-23 | 太平洋セメント株式会社 | Apparatus and method for treating cement kiln exhaust gas |
JP2017060905A (en) * | 2015-09-24 | 2017-03-30 | 太平洋セメント株式会社 | Processing apparatus and method of cement kiln exhaust gas |
CN105664690B (en) * | 2016-04-13 | 2018-08-24 | 北京凯盛建材工程有限公司 | A kind of system that denitration being carried out to cement decomposing furnace using gas generator |
CN108579420A (en) * | 2018-05-21 | 2018-09-28 | 襄阳泽东化工集团有限公司 | Nitrate produces the processing system and treatment process of tail gas |
KR101935734B1 (en) | 2018-07-16 | 2019-01-04 | 이승호 | Boiler system using waste heat |
WO2023053218A1 (en) * | 2021-09-28 | 2023-04-06 | 三菱重工業株式会社 | Denitration device |
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JP4503378B2 (en) * | 2004-07-15 | 2010-07-14 | 株式会社Ihi | Method and apparatus for removing gaseous mercury in exhaust gas |
WO2006073083A1 (en) * | 2005-01-06 | 2006-07-13 | Taiheiyo Cement Corporation | Cement kiln firing waste gas treating apparatus and treating method |
JP4981318B2 (en) * | 2005-12-19 | 2012-07-18 | 三菱重工業株式会社 | Exhaust gas treatment apparatus and exhaust gas treatment method |
JP2009226298A (en) * | 2008-03-21 | 2009-10-08 | Ihi Corp | Method for treating exhaust gas and exhaust gas treatment apparatus |
JP5636577B2 (en) * | 2008-07-29 | 2014-12-10 | バブコック日立株式会社 | Method for purifying exhaust gas containing metallic mercury and oxidation catalyst for metallic mercury in exhaust gas |
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