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JP2016011759A - Exhaust gas combustion purification system - Google Patents

Exhaust gas combustion purification system Download PDF

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JP2016011759A
JP2016011759A JP2014132088A JP2014132088A JP2016011759A JP 2016011759 A JP2016011759 A JP 2016011759A JP 2014132088 A JP2014132088 A JP 2014132088A JP 2014132088 A JP2014132088 A JP 2014132088A JP 2016011759 A JP2016011759 A JP 2016011759A
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combustion chamber
combustion
exhaust gas
side wall
wall
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JP6258797B2 (en
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荒川 秩
Chitsu Arakawa
秩 荒川
敏雄 秋山
Toshio Akiyama
敏雄 秋山
祐司 及川
Yuji Oikawa
祐司 及川
健太 水野
Kenta Mizuno
健太 水野
一貴 長井
kazutaka Nagai
一貴 長井
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Japan Pionics Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide means capable of suppressing or preventing the crack, collapse, chipping or the like of a ceramic wall.SOLUTION: A combustion type purification device, with a ceramic wall 4' having air permeability on a side surface wall 4 of a combustion chamber 1, ejects oxygen-containing gas to the combustion chamber through the ceramic wall in order to prevent a solid particulate-like oxide from being accumulated on the side surface wall, and includes a spray nozzle 8 at a gas discharge port 7. In the combustion type purification device, the upper surface of the side surface wall of the combustion chamber is formed of the ceramic wall having air permeability, and the lower surface thereof is formed of a metal wall 4'' having air permeability.

Description

本発明は、半導体製造工程から排出される排ガスに含まれる有害成分を燃焼させて除去するための燃焼式浄化装置に関する。さらに詳細には、半導体製造工程から排出される有害成分を、火炎及び酸素の存在下、高温で接触させ、燃焼することにより無害な物質あるいは容易に無害化できる物質に変えるための燃焼式浄化装置に関するものである。   The present invention relates to a combustion type purification apparatus for burning and removing harmful components contained in exhaust gas discharged from a semiconductor manufacturing process. More specifically, a combustion type purification device for converting harmful components discharged from a semiconductor manufacturing process into harmless substances or substances that can be easily detoxified by bringing them into contact with each other at high temperatures in the presence of flame and oxygen and burning them. It is about.

近年の半導体工業の発展とともに、半導体製造工程においては非常に多種のガスが使用されるようになってきている。しかし、これらのガスは人体及び環境にとって有害な物質が多く、工場外へ排出するに先立って浄化することが必須のこととなっている。これらのガス(有害成分)を燃焼させることにより分解処理する燃焼式浄化方法は、排ガスの組成や物性によらず適用することができる便利な方法であり、特に高濃度、大流量の場合は乾式浄化方法や湿式浄化方法と比較して効率的である。   With the development of the semiconductor industry in recent years, a great variety of gases have been used in the semiconductor manufacturing process. However, many of these gases are harmful to the human body and the environment, and it is essential to purify them before they are discharged outside the factory. The combustion purification method that decomposes these gases (hazardous components) by burning them is a convenient method that can be applied regardless of the composition and physical properties of the exhaust gas, especially in the case of high concentrations and large flow rates. It is more efficient than purification methods and wet purification methods.

燃焼式浄化方法においては、有害成分を含む排ガスと、プロパン、LPG、LNG等の燃料ガス、空気または酸素、必要に応じて不活性ガスを、燃焼室において混合し、燃焼させ、有害成分を無害な酸化物あるいは容易に無害化できる物質に変換する処理が行なわれる。従来から使用されている一般的な燃焼式浄化装置は、有害成分を燃焼するための燃焼室と、処理対象の有害成分を含む排ガス、燃料ガス、空気等の酸素含有ガスを燃焼室へ導入するための各配管やノズルと、燃焼後のガスを燃焼室から排出するための配管等から構成されている。また、燃焼室のガス排出口近辺には、冷却水を噴出して高温度の排ガスを冷却するためのスプレーノズルが備えられている。   In the combustion purification method, exhaust gas containing harmful components, fuel gas such as propane, LPG, LNG, etc., air or oxygen, and inert gas as necessary are mixed in the combustion chamber and burned to harm the harmful components. The conversion to a simple oxide or a material that can be easily detoxified is performed. Conventional combustion purification apparatuses that have been used in the past introduce a combustion chamber for burning harmful components, and an oxygen-containing gas such as exhaust gas, fuel gas, air containing harmful components to be treated into the combustion chamber. Each pipe and nozzle for this, and the pipe | tube for discharging | emitting the gas after combustion from a combustion chamber, etc. are comprised. Further, a spray nozzle is provided near the gas discharge port of the combustion chamber to cool the exhaust gas at a high temperature by jetting cooling water.

このような構成の燃焼式浄化装置で、有害成分は燃焼され排出口より排気されて大気に放出されるか、あるいは次の処理装置へ送られる。しかし、処理対象の有害成分が、例えばシラン、ホスフィン、アルシン、ジボランのようなガスである場合は、燃焼により各々ケイ素、リン、ヒ素、ホウ素の固体粒子状酸化物(粉化物)が生成し、大部分は燃焼室内を通過し後工程で処理されるが、一部は燃焼室内の側面壁に堆積し、燃焼時間の経過とともにその付着面積、厚みが増加する。その結果、有害成分と、燃料ガス、空気、酸素等との均一な混合が妨げられて完全燃焼が阻害され、燃焼温度の低下、処理対象の有害成分の分解率の低下を生じるだけでなく、粉化物の堆積量が多い場合は失火する虞があった。   In the combustion type purification apparatus having such a configuration, harmful components are combusted and exhausted from the discharge port and released to the atmosphere or sent to the next processing apparatus. However, when the harmful component to be treated is a gas such as silane, phosphine, arsine, and diborane, solid particulate oxides (powder) of silicon, phosphorus, arsenic, and boron are generated by combustion, Most of them pass through the combustion chamber and are processed in the subsequent process, but some are deposited on the side wall in the combustion chamber, and the adhesion area and thickness increase with the passage of combustion time. As a result, uniform mixing of harmful components with fuel gas, air, oxygen, etc. is hindered and complete combustion is inhibited, resulting in a decrease in combustion temperature and a decomposition rate of harmful components to be treated. If the amount of powdered material accumulated is large, there was a risk of misfire.

そのため、特許文献1〜5のように、燃焼室の側面をセラミックや焼結金属等からなる通気性の材料とし、その外周に空気や不活性ガス等の圧力ガス流路を設けて、側面壁を介して該圧力ガスを燃焼室に噴出させることにより、固体粒子状酸化物が燃焼室の側面壁に堆積することを防止する燃焼式浄化装置が開発されている。
特開平10−54534号公報 特開平10−61934号公報 特開2005−98680号公報 特開2006−194544号公報
Therefore, as in Patent Documents 1 to 5, the side surface of the combustion chamber is made of a breathable material made of ceramic, sintered metal, or the like, and a pressure gas flow path such as air or inert gas is provided on the outer periphery thereof, and the side wall A combustion type purifying apparatus has been developed that prevents the solid particulate oxide from accumulating on the side wall of the combustion chamber by ejecting the pressure gas into the combustion chamber via the gas.
JP 10-54534 A JP-A-10-61934 JP 2005-98680 A JP 2006-194544 A

前記のような燃焼式浄化装置において、燃焼室の側面壁を通気性のセラミックとした場合、火炎に対する耐熱性、有害成分に対する耐腐食性が、金属等他の材料よりも優れた側面壁とすることができる。しかしながら、セラミックは脆いという欠点があり、火炎等の影響によりクラック(裂け目、割れ)が生じ、崩壊したり欠けたりすることにより、燃焼式浄化装置自体や後工程の装置に悪影響を及ぼすことがある。従って、本発明が解決しようとする課題は、燃焼室の側面壁として通気性のセラミックを用いた燃焼式浄化装置において、燃焼室の側面壁のクラック、崩壊、欠け等を抑制または防止できる手段等を提供することである。   In the combustion type purifying apparatus as described above, when the side wall of the combustion chamber is made of a breathable ceramic, the side wall is superior to other materials such as metal in terms of heat resistance against flames and corrosion resistance against harmful components. be able to. However, ceramics have the disadvantage of being brittle, and cracks (cracks, cracks) occur due to the influence of flames, etc., and they may have an adverse effect on the combustion purification device itself and subsequent devices by collapsing or chipping. . Therefore, the problem to be solved by the present invention is a means for suppressing or preventing cracks, collapse, chipping, etc. of the side wall of the combustion chamber in the combustion purification device using breathable ceramic as the side wall of the combustion chamber. Is to provide.

本発明者らは、これらの課題を解決すべく鋭意検討した結果、セラミック壁が火炎による高温化とプレーノズルから噴出される冷却水による低温化の影響を繰返して長期間受けた場合、クラック、崩壊、欠け等が生じやすくなること、また、特に冷却水に接触する可能性が高い側面壁の下部表面を、通気性のセラミック壁から通気性の金属壁に替えることにより、燃焼室の側面壁全体の耐熱性を損なうことなく、クラック、崩壊、欠け等を少なくできることを見出し、本発明の燃焼式浄化装置に到達した。   As a result of intensive studies to solve these problems, the present inventors have found that the ceramic wall is repeatedly affected by the high temperature caused by the flame and the low temperature caused by the cooling water ejected from the pre-nozzle for a long period of time. By replacing the lower surface of the side wall, which is particularly likely to come into contact with cooling water, from a breathable ceramic wall with a breathable metal wall, it is easy to cause collapse, chipping, etc. The inventors have found that cracks, collapse, chipping, and the like can be reduced without impairing the overall heat resistance, and have reached the combustion purification apparatus of the present invention.

すなわち本発明は、半導体製造工程から排出される排ガスに含まれる有害成分を燃焼する燃焼室、火炎を該燃焼室へ導入するノズル、排ガスを該燃焼室へ導入するノズル、該燃焼室の側面壁、該側面壁の外周に設けられた酸素含有ガス流路、該流路に酸素含有ガスを導入する酸素含有ガス導入口、及び燃焼処理後のガスの排出口にスプレーノズルを備えた燃焼式浄化装置であって、燃焼室の側面壁の上部表面が通気性のセラミック壁、燃焼室の側面壁の下部表面が通気性の金属壁であることを特徴とする排ガスの燃焼式浄化装置である。   That is, the present invention relates to a combustion chamber for burning harmful components contained in exhaust gas discharged from a semiconductor manufacturing process, a nozzle for introducing flame into the combustion chamber, a nozzle for introducing exhaust gas into the combustion chamber, and a side wall of the combustion chamber Combustion-type purification provided with an oxygen-containing gas channel provided on the outer periphery of the side wall, an oxygen-containing gas inlet for introducing oxygen-containing gas into the channel, and a spray nozzle at the gas outlet after the combustion treatment An exhaust gas combustion purification apparatus, wherein the upper surface of the side wall of the combustion chamber is a breathable ceramic wall and the lower surface of the side wall of the combustion chamber is a breathable metal wall.

本発明の排ガスの燃焼式浄化装置においては、耐熱性が要求される側面壁の上部表面は通気性のセラミック壁で構成されるが、側面壁の下部表面は耐クラック性に弱点を有するセラミックに替わり、耐クラック性に優れた金属壁で構成されるので、燃焼室の側面壁の耐熱性を損なうことなく、クラック、崩壊、欠け等を抑制または防止することができる。その結果、セラミック壁の破片の流出が抑制または防止され、燃焼式浄化装置や後工程の装置への悪影響を抑制または防止することができる。本発明は特に、装置の小型化のために燃焼処理後すぐにガスの冷却が必要な燃焼式浄化装置に効果を発揮する。   In the exhaust gas combustion purification apparatus of the present invention, the upper surface of the side wall, which requires heat resistance, is composed of a breathable ceramic wall, but the lower surface of the side wall is made of ceramic having a weak point in crack resistance. Instead, since the metal wall is excellent in crack resistance, cracks, collapse, chipping, etc. can be suppressed or prevented without impairing the heat resistance of the side wall of the combustion chamber. As a result, the outflow of debris from the ceramic wall is suppressed or prevented, and adverse effects on the combustion purification device and the subsequent device can be suppressed or prevented. The present invention is particularly effective for a combustion type purification apparatus that requires gas cooling immediately after the combustion process in order to reduce the size of the apparatus.

本発明は、半導体製造工程から排出される排ガスに含まれる有害成分を燃焼する燃焼室、火炎を該燃焼室へ導入するノズル、排ガスを該燃焼室へ導入するノズル、該燃焼室の側面壁、該側面壁の外周に設けられた酸素含有ガス流路、該流路に酸素含有ガスを導入する酸素含有ガス導入口、及び燃焼処理後のガスの排出口にスプレーノズルを備えた燃焼式浄化装置に適用される。   The present invention comprises a combustion chamber for burning harmful components contained in exhaust gas discharged from a semiconductor manufacturing process, a nozzle for introducing flame into the combustion chamber, a nozzle for introducing exhaust gas into the combustion chamber, a side wall of the combustion chamber, Combustion-type purification apparatus provided with an oxygen-containing gas channel provided on the outer periphery of the side wall, an oxygen-containing gas inlet for introducing an oxygen-containing gas into the channel, and a spray nozzle at the gas outlet after the combustion treatment Applies to

本発明の排ガスの燃焼式浄化装置で処理できる有害成分としては、アルシン、ホスフィン、シラン、ジシラン、ジクロロシラン、ジボラン、セレン化水素、ゲルマン等の水素化物ガス、三フッ化ホウ素、三塩化ホウ素、四フッ化珪素、四塩化珪素、四塩化チタン、塩化アルミニウム、四フッ化ゲルマニウム、六フッ化タングステン等の酸性ガス、アンモニア、モノメチルアミン、ジメチルアミン、トリメチルアミン、ヒドラジン等の塩基性ガス、パーフルオロカーボン、ヒドロフルオロカーボン等のハロゲン化炭素等を例示することができる。また、燃料ガスとしては、プロパンガス、天然ガス等を使用することができる。これらのガスは、必要に応じ窒素等の不活性ガスと共に用いられる。   As harmful components that can be treated by the exhaust gas combustion purification device of the present invention, arsenic, phosphine, silane, disilane, dichlorosilane, diborane, hydrogen selenide, germane and other hydride gases, boron trifluoride, boron trichloride, Acid gases such as silicon tetrafluoride, silicon tetrachloride, titanium tetrachloride, aluminum chloride, germanium tetrafluoride, tungsten hexafluoride, basic gases such as ammonia, monomethylamine, dimethylamine, trimethylamine, hydrazine, perfluorocarbon, Examples thereof include halogenated carbon such as hydrofluorocarbon. Moreover, propane gas, natural gas, etc. can be used as fuel gas. These gases are used together with an inert gas such as nitrogen as necessary.

以下、本発明の排ガスの燃焼式浄化装置を、図1〜図6に基づいて詳細に説明するが、本発明がこれらにより限定されるものではない。
尚、図1は、本発明の排ガスの燃焼式浄化装置の一例を示す縦断面の構成図である。図2は、図1におけるa−a’断面図である。図3は、本発明の排ガスの燃焼式浄化装置の図1以外の一例を示す縦断面の構成図である。図4は、図3におけるb−b’断面図である。図5は、本発明の排ガスの燃焼式浄化装置の燃焼室の側面壁の例を示す部分拡大断面図である。図6は、本発明の排ガスの燃焼式浄化装置に水槽及びスクラバーの設備を結合した浄化装置の例を示す縦断面の構成図である。
Hereinafter, the exhaust gas combustion purification apparatus of the present invention will be described in detail with reference to FIGS. 1 to 6, but the present invention is not limited thereto.
FIG. 1 is a longitudinal sectional view showing an example of an exhaust gas combustion purification device of the present invention. 2 is a cross-sectional view taken along the line aa ′ in FIG. FIG. 3 is a longitudinal sectional configuration diagram showing an example other than FIG. 1 of the exhaust gas combustion purification apparatus of the present invention. 4 is a cross-sectional view taken along the line bb ′ in FIG. FIG. 5 is a partially enlarged cross-sectional view showing an example of a side wall of a combustion chamber of the exhaust gas combustion purification apparatus of the present invention. FIG. 6 is a longitudinal sectional view showing an example of a purification device in which a water tank and a scrubber facility are combined with the exhaust gas combustion purification device of the present invention.

本発明の排ガスの燃焼式浄化装置は、図1〜図4に示すように、半導体製造工程から排出される排ガスに含まれる有害成分を燃焼する燃焼室1、火炎を該燃焼室へ導入するノズル2、排ガスを該燃焼室へ導入するノズル3、該燃焼室の側面壁4、該側面壁の外周に設けられた酸素含有ガス流路5、該流路5に酸素含有ガスを導入する酸素含有ガス導入口6、及び燃焼処理後のガスの排出口7にスプレーノズル8を備えた燃焼式浄化装置であって、燃焼室の側面壁の上部表面が通気性のセラミック壁4’、燃焼室の側面壁の下部表面が通気性の金属壁4”である排ガスの燃焼式浄化装置である。   As shown in FIGS. 1 to 4, an exhaust gas combustion purification device of the present invention includes a combustion chamber 1 for burning harmful components contained in exhaust gas discharged from a semiconductor manufacturing process, and a nozzle for introducing flame into the combustion chamber. 2. Nozzle 3 for introducing exhaust gas into the combustion chamber, side wall 4 of the combustion chamber, oxygen-containing gas channel 5 provided on the outer periphery of the side wall, oxygen-containing gas for introducing oxygen-containing gas into the channel 5 A combustion type purification apparatus provided with a spray nozzle 8 at a gas inlet 6 and a gas outlet 7 after combustion treatment, wherein the upper surface of the side wall of the combustion chamber is a breathable ceramic wall 4 ′, This is an exhaust gas combustion type purification apparatus in which the lower surface of the side wall is a breathable metal wall 4 ″.

本発明の排ガスの燃焼式浄化装置は、燃焼室1の側面に、円筒の通気性及び断熱性を有する側面壁4が設けられ、燃焼室1において排ガスが高温度の火炎に接触するとともに、側面壁4から供給される空気等の酸素含有ガスと接触して、排ガスに含まれる有害成分が燃焼(熱分解)される。その際、有害成分の種類によっては粉化物が生成するが、図1、図3において矢印で示すような酸素含有ガス(空気を含む)の流れにより、粉化物の側面壁4の表面への堆積を防止することができる。   In the combustion type purification apparatus for exhaust gas of the present invention, a cylindrical side wall 4 having air permeability and heat insulation is provided on the side surface of the combustion chamber 1, and the exhaust gas contacts the high temperature flame in the combustion chamber 1. In contact with an oxygen-containing gas such as air supplied from the wall 4, harmful components contained in the exhaust gas are burned (thermally decomposed). At that time, although a pulverized product is generated depending on the type of harmful component, the pulverized product is deposited on the surface of the side wall 4 by the flow of oxygen-containing gas (including air) as shown by arrows in FIGS. Can be prevented.

そして、本発明の排ガスの燃焼式浄化装置は、耐熱性が要求される燃焼室の側面壁の上部表面が通気性のセラミック壁で構成され、スプレーノズルから噴出される冷却水によりクラックの原因となる影響を受けやすい燃焼室の側面壁の下部表面が通気性の金属壁で構成される。セラミック壁の材質としては、アルミナ、シリカ、チタニア等を使用することができる。また、金属壁の材質としては、炭素鋼、クロム鋼、モリブデン鋼、マンガン鋼、ニッケル鋼、ステンレス鋼等を使用することができるが、これらの中でもステンレス鋼を使用することが好ましい。   In the exhaust gas combustion purification apparatus of the present invention, the upper surface of the side wall of the combustion chamber where heat resistance is required is constituted by a breathable ceramic wall, and the cause of cracks is caused by cooling water ejected from the spray nozzle. The lower surface of the side wall of the combustion chamber that is easily affected is made of a breathable metal wall. As the material of the ceramic wall, alumina, silica, titania or the like can be used. Moreover, as the material of the metal wall, carbon steel, chrome steel, molybdenum steel, manganese steel, nickel steel, stainless steel, etc. can be used, and among these, it is preferable to use stainless steel.

本発明の排ガスの燃焼式浄化装置においては、図1に示すように、燃焼室の側面壁4の上部全体が通気性のセラミック壁4’、燃焼室の側面壁4の下部全体が通気性の金属壁4”となるような構成のほか、上部表面のみがセラミック壁4’、下部表面のみが金属壁4”(図3)となるような構成とすることもできる。燃焼室の側面壁の下部表面を構成する通気性の金属壁4”の高さは、通常は燃焼室の側面壁4全体の高さの5〜30%、好ましくは側面壁4全体の高さの10〜25%である。本発明において、燃焼室の側面壁4は、通常は厚みが0.2〜50mmの円筒の形状、好ましくは厚みが5〜30mmの円筒の形状である。   In the exhaust gas combustion purifying apparatus of the present invention, as shown in FIG. 1, the entire upper portion of the side wall 4 of the combustion chamber is breathable ceramic wall 4 ', and the entire lower portion of the side wall 4 of the combustion chamber is breathable. In addition to a configuration in which the metal wall 4 ″ is formed, a configuration in which only the upper surface is the ceramic wall 4 ′ and only the lower surface is the metal wall 4 ″ (FIG. 3) can be employed. The height of the breathable metal wall 4 "constituting the lower surface of the side wall of the combustion chamber is usually 5-30% of the total height of the side wall 4 of the combustion chamber, preferably the height of the entire side wall 4 In the present invention, the side wall 4 of the combustion chamber is usually in the shape of a cylinder having a thickness of 0.2 to 50 mm, preferably in the shape of a cylinder having a thickness of 5 to 30 mm.

本発明において、燃焼室の側面壁4(4’及び4”)の表面の形態としては、例えば図5に示すような構成を挙げることができる。図5(1)(2)は針孔を有する壁の部分拡大断面図であり、その孔径(直径)は、通常は0.01〜3.0mm、好ましくは0.02〜1.0mmである。尚、孔9は円形に限られず、そのような場合の孔の大きさは、前記の孔径に相当する大きさである。孔の配列も縦横に規則的に配置したり、ランダムに配置したものを用いることができる。図5(3)は線状の間隙10を有する壁の部分拡大断面図であり、その間隙は、通常は0.005〜2.0mm、好ましくは0.01〜1.0mmである。図5(4)は格子窓状の間隙11を有する壁の部分拡大断面図であり、その間隙は正方形に換算した場合の一辺の長さとして、通常は0.01〜3.0mm、好ましくは0.02〜1.0mmである。また、燃焼室の側面壁4の表面の形態は、これらに限られるものではなく、例えばこれらのほかに、繊維状のセラミックまたは金属が積層された積層体、多数の粒子状のセラミックまたは金属が積層された積層体、細孔を有する多孔質セラミックまたは多孔質金属等の形態を挙げることができる。   In the present invention, as the form of the surface of the side wall 4 (4 ′ and 4 ″) of the combustion chamber, for example, a configuration as shown in FIG. 5 can be given. FIGS. The hole diameter (diameter) is usually 0.01 to 3.0 mm, preferably 0.02 to 1.0 mm, and the hole 9 is not limited to a circle. In such a case, the size of the holes is the size corresponding to the above-mentioned hole diameter, and the holes can be arranged regularly and vertically or randomly. Fig. 5 is a partially enlarged sectional view of a wall having a linear gap 10. The gap is usually 0.005 to 2.0 mm, preferably 0.01 to 1.0 mm. It is a partial expanded sectional view of the wall which has the window-shaped gap | interval 11, and the gap | interval is the case at the time of converting into a square The length of the side is usually 0.01 to 3.0 mm, preferably 0.02 to 1.0 mm, and the form of the surface of the side wall 4 of the combustion chamber is not limited to these, For example, in addition to these, forms such as a laminate in which fibrous ceramics or metals are laminated, a laminate in which a large number of particulate ceramics or metals are laminated, porous ceramics or porous metals having pores, etc. be able to.

尚、燃焼室の側面壁4の孔、間隙が前記の範囲より大きい場合は、燃焼室1への酸素含有ガスの流れが偏り、ガスの流量が多い部分と少ない部分が生じる虞があり、ガスの流量が少ない部分では粉化物が堆積する虞がある。また、前記の範囲より小さい場合は、短時間で孔、間隙が粉化物等により閉塞する虞がある。さらに、燃焼室の側面壁4の通気性部分は、いずれの形態においても、好ましくは空隙率あるいは気孔率が50〜90%程度となるようにされる。空隙率あるいは気孔率が50%未満の場合は、粉化物が壁面に堆積する虞があり、空隙率あるいは気孔率が90%を越える場合は、側面壁の強度が低下する虞がある。   If the holes and gaps in the side wall 4 of the combustion chamber are larger than the above ranges, the flow of oxygen-containing gas to the combustion chamber 1 is biased, and there may be a portion where the gas flow rate is high and a portion where the gas flow rate is high. There is a possibility that the powdered material accumulates in the portion where the flow rate of the gas is small. Moreover, when smaller than the said range, there exists a possibility that a hole and a gap | block may be obstruct | occluded by powdered material etc. in a short time. Furthermore, the air-permeable portion of the side wall 4 of the combustion chamber is preferably configured so that the porosity or porosity is about 50 to 90% in any form. When the porosity or porosity is less than 50%, there is a possibility that the powdered material is deposited on the wall surface, and when the porosity or porosity exceeds 90%, the strength of the side wall may be lowered.

本発明の排ガスの燃焼式浄化装置においては、通常は前記のような燃焼室の側面壁4の外周全体にわたり、酸素含有ガス流路5が設けられる。酸素含有ガス流路5の幅は、通常は5〜200mm、好ましくは10〜100mmである。有害成分を処理する際には燃焼室1の温度は500〜1200℃の高温になり、このような構成とすることにより、燃焼室1の熱が外部に拡散することを防止できる。尚、酸素含有ガス流路5の外壁は、燃焼室の側面壁4の形状と合ったものであり、通常は円筒形である。   In the exhaust gas combustion purification apparatus of the present invention, the oxygen-containing gas flow path 5 is usually provided over the entire outer periphery of the side wall 4 of the combustion chamber as described above. The width of the oxygen-containing gas channel 5 is usually 5 to 200 mm, preferably 10 to 100 mm. When processing harmful components, the temperature of the combustion chamber 1 becomes a high temperature of 500 to 1200 ° C. With such a configuration, the heat of the combustion chamber 1 can be prevented from diffusing to the outside. The outer wall of the oxygen-containing gas flow path 5 matches the shape of the side wall 4 of the combustion chamber and is usually cylindrical.

また、本発明において、酸素含有ガスを流路5に導入するための酸素含有ガス導入口6は、導入口6から導入された酸素含有ガスが、環状の酸素含有ガス流路5を旋回するような方向に設定される。酸素含有ガス導入口6は、通常は環の接線方向に対して±30度の角度の範囲内、好ましくは実質的に環の接線方向に酸素含有ガスが導入できるように設定される。このような構成とすることにより、酸素含有ガスを流路5内のいずれの個所においても、酸素含有ガスが滞留、偏流することを防止でき、酸素含有ガスを均一な流量及び温度で燃焼室1へ導入することが可能となる。   In the present invention, the oxygen-containing gas introduction port 6 for introducing the oxygen-containing gas into the flow path 5 is configured so that the oxygen-containing gas introduced from the introduction port 6 swirls through the annular oxygen-containing gas flow path 5. Is set to the correct direction. The oxygen-containing gas inlet 6 is usually set so that the oxygen-containing gas can be introduced within an angle range of ± 30 degrees with respect to the tangential direction of the ring, preferably substantially in the tangential direction of the ring. With such a configuration, the oxygen-containing gas can be prevented from staying and drifting at any location in the flow path 5, and the oxygen-containing gas can be prevented from flowing at a uniform flow rate and temperature. It becomes possible to introduce to.

また、酸素含有ガス流路5は、排ガスの導入方向(図1においては上下方向)に、複数個に区切り、各々の流路に導入する酸素含有ガスの流量等をコントロールすることも可能である。このような場合、酸素含有ガスの旋回方向は、互いに同じ方向となるように設定しても、互いに反対方向となるように設定してもよい。しかし、側面壁が酸素含有ガスを流路内の旋回方向を維持して燃焼室1へ導入できるような構成の場合は、隣接する流路内の酸素含有ガスの旋回方向を互いに反対方向となるように設定して、燃焼室内におけるガスの混合を容易にすることが好ましい。   Further, the oxygen-containing gas flow path 5 can be divided into a plurality of parts in the exhaust gas introduction direction (vertical direction in FIG. 1), and the flow rate of the oxygen-containing gas introduced into each flow path can be controlled. . In such a case, the swirling directions of the oxygen-containing gas may be set to be the same as each other or may be set to be opposite to each other. However, when the side wall is configured to be able to introduce the oxygen-containing gas into the combustion chamber 1 while maintaining the swirl direction in the flow path, the swirl directions of the oxygen-containing gas in the adjacent flow paths are opposite to each other. It is preferable to facilitate the mixing of the gas in the combustion chamber by setting as described above.

本発明の排ガスの燃焼式浄化装置においては、燃焼室1の直前で燃料と酸素含有ガスが混合され、燃焼するように設定される。燃料の燃焼の際には、火炎の先端が燃焼室1に入ってもよいし入らなくてもよい。また、図1に示すように、排ガスを燃焼室1へ導入するノズル3は、通常は、火炎を燃焼室1へ導入するノズル2の外周側に設置される。尚、本発明においては、酸素含有ガス流路5のほか、火炎を燃焼室1へ導入するノズル2の周辺にも、酸素含有ガスを燃焼室1へ導入するノズルを設けることができる。   In the exhaust gas combustion purifying apparatus of the present invention, the fuel and the oxygen-containing gas are mixed immediately before the combustion chamber 1 and burned. When the fuel is burned, the tip of the flame may or may not enter the combustion chamber 1. Further, as shown in FIG. 1, the nozzle 3 for introducing exhaust gas into the combustion chamber 1 is usually installed on the outer peripheral side of the nozzle 2 for introducing flame into the combustion chamber 1. In the present invention, in addition to the oxygen-containing gas flow path 5, a nozzle for introducing the oxygen-containing gas into the combustion chamber 1 can be provided around the nozzle 2 for introducing the flame into the combustion chamber 1.

本発明の排ガスの燃焼式浄化装置において、燃焼処理後のガスは、図1、図3に示すように、排出口7に設けられたスプレーノズル8から噴出する冷却水により冷却された後、大気に放出されるか、あるいは次の処理工程に送られる。その際、スプレーノズル8から噴出する冷却水が燃焼室の側面壁4の下部表面に接触する可能性がある。しかし、本発明においては、燃焼室の側面壁4の下部表面が通気性の金属壁で構成されているため、通気性のセラミック壁の場合のようなクラック等が発生する虞がない。   In the exhaust gas combustion purifying apparatus of the present invention, the gas after the combustion treatment is cooled by cooling water ejected from a spray nozzle 8 provided at the discharge port 7 as shown in FIGS. Or sent to the next processing step. At that time, the cooling water ejected from the spray nozzle 8 may come into contact with the lower surface of the side wall 4 of the combustion chamber. However, in the present invention, since the lower surface of the side wall 4 of the combustion chamber is made of a breathable metal wall, there is no risk of cracks and the like as in the case of a breathable ceramic wall.

半導体製造工程から排出された排ガスが、本発明の排ガスの燃焼式浄化装置により燃焼処理された後、次の処理工程に送られるような場合は、本発明においては、このような処理工程を実施するための設備を併せて装備することも可能である。図6の水槽17及びスクラバーの設備は、本発明の排ガスの燃焼式浄化装置により処理した排ガスについて、処理後のガスに含まれる粉化物の除去、及び新たに生成した有害成分(容易に無害化できる成分)の除去を行なうためのものであり、本発明においては必須の設備ではないが、これらの設備を備えることが好ましい。すなわち、本発明においては、燃焼室1の排出側に、粉化物の除去部及び/または酸性ガスの除去部を設けた排ガスの燃焼式浄化装置とすることが好ましい。   When the exhaust gas discharged from the semiconductor manufacturing process is combusted by the exhaust gas combustion purification device of the present invention and then sent to the next processing process, the present invention implements such a processing process. It is also possible to equip it with equipment to do this. The water tank 17 and scrubber equipment shown in FIG. 6 are provided for the exhaust gas treated by the exhaust gas combustion purification device of the present invention, for removing pulverized substances contained in the treated gas, and for newly generated harmful components (easily detoxified). Component), which is not essential equipment in the present invention, but it is preferable to provide these equipment. That is, in the present invention, it is preferable that the exhaust gas combustion type purification device is provided with a pulverized product removal unit and / or an acid gas removal unit on the discharge side of the combustion chamber 1.

例えば、本発明の排ガスの燃焼式浄化装置により、アルシン、ホスフィン、シラン、ジボラン等の水素化物を処理した場合は、燃焼により各々ヒ素、リン、ケイ素、ホウ素等の固体粒子状酸化物が生成する。また、三フッ化ホウ素、三塩化ホウ素、四フッ化珪素、四塩化珪素、C等のハロゲン化物を処理した場合は、新たに塩化水素、フッ化水素等の酸性ガス(容易に無害化できる成分)が生成する。図6の浄化装置においては、粉化物は主にスプレーノズル13からの散水、及び多孔板19における捕捉により除去することが可能である。また、本発明の排ガスの燃焼式浄化装置とスクラバー設備間の配管16は、粉化物が容易に水槽17へ洗い流されるようにスクラバー設備側に傾斜させることが好ましい。 For example, when a hydride such as arsine, phosphine, silane, or diborane is processed by the exhaust gas combustion purification device of the present invention, solid particulate oxides such as arsenic, phosphorus, silicon, and boron are generated by combustion. . In addition, when a halide such as boron trifluoride, boron trichloride, silicon tetrafluoride, silicon tetrachloride, or C 2 F 6 is treated, a new acidic gas such as hydrogen chloride or hydrogen fluoride (which is easily harmless) Component that can be converted into In the purification device of FIG. 6, the pulverized material can be removed mainly by watering from the spray nozzle 13 and trapping in the perforated plate 19. Moreover, it is preferable to incline the piping 16 between the combustion purification device for exhaust gas of the present invention and the scrubber equipment toward the scrubber equipment so that the pulverized material can be easily washed out to the water tank 17.

本発明の排ガスの燃焼式浄化装置に、水槽17及びスクラバーの設備を結合した図6に示すような浄化装置を用いた場合、塩化水素、フッ化水素等の酸性ガスは、主に充填材20により除去することが可能である。また、デミスター21により水分も併せて除去することができる。尚、図6において、12は冷却配管、14はフローメーター、15はポンプ、18は排水管、22は処理後のガスを外部へ排出する排出口を表わす。   When the purification apparatus as shown in FIG. 6 in which the equipment of the water tank 17 and the scrubber is combined with the exhaust gas combustion type purification apparatus of the present invention, acidic gases such as hydrogen chloride and hydrogen fluoride are mainly used as the filler 20. Can be removed. Further, the demister 21 can also remove moisture. In FIG. 6, 12 is a cooling pipe, 14 is a flow meter, 15 is a pump, 18 is a drain pipe, and 22 is a discharge port for discharging processed gas to the outside.

次に、本発明を実施例により具体的に説明するが、本発明がこれらにより限定されるものではない。   EXAMPLES Next, although an Example demonstrates this invention concretely, this invention is not limited by these.

[実施例1]
(燃焼式浄化装置の製作)
円筒形の燃焼室1(高さ500mm、直径200mm)、火炎を該燃焼室1へ導入するノズル2、排ガスを燃焼室1へ導入するノズル3、燃焼室1の側面壁4(厚さ15mm)、環状の酸素含有ガス流路5(幅20mm)、酸素含有ガス導入口6、及び燃焼後のガスを外部へ排出する排出口7にスプレーノズル8を有する図1、図2に示すような構成の浄化装置を製作した。尚、側面壁4は、直径10〜100μmに相当する微多孔を有する通気性のセラミック壁4’と通気性の金属壁4”からなり、通気性の金属壁4”の高さは、燃焼室の側面壁全体の高さの20%であった。また、スプレーノズル8は、燃焼処理後のガスの冷却を早く行なうことにより、燃焼式浄化装置の小型化を図るため、噴出する冷却水がセラミック壁4’に接触せず、通気性の金属壁4”の下部に接触するような位置に設置した。
[Example 1]
(Production of combustion type purification device)
Cylindrical combustion chamber 1 (height 500 mm, diameter 200 mm), nozzle 2 for introducing a flame into the combustion chamber 1, nozzle 3 for introducing exhaust gas into the combustion chamber 1, and side wall 4 of the combustion chamber 1 (thickness 15 mm) 1 and 2 having a spray nozzle 8 in the annular oxygen-containing gas flow path 5 (width 20 mm), the oxygen-containing gas inlet 6 and the outlet 7 for discharging the burned gas to the outside. A purification device was manufactured. The side wall 4 is composed of a breathable ceramic wall 4 ′ having a micropore corresponding to a diameter of 10 to 100 μm and a breathable metal wall 4 ″, and the height of the breathable metal wall 4 ″ is determined by the combustion chamber. It was 20% of the height of the entire side wall. Further, the spray nozzle 8 quickly cools the gas after the combustion treatment, so that the combustion purification device can be miniaturized, so that the sprayed cooling water does not come into contact with the ceramic wall 4 ′, and the breathable metal wall It installed in the position which touches the lower part of 4 ''.

前述のように製作した燃焼式浄化装置の右下部に、縦300mm、横300mm、高さ300mmの水槽17を設置し、さらに水槽17の上部には、多孔板19、ポリプロピレン樹脂を主材とする充填材20、及びデミスター21を有するスクラバーを設置した。また、燃焼式浄化装置の下部と水槽を傾斜した配管で接続し、充填材20の上部にはスプレーノズル13を設置し、水槽17の冷却水が循環するように、フローメーター14、ポンプ15等を接続して、図6に示すような浄化装置を完成した。   A water tank 17 having a length of 300 mm, a width of 300 mm, and a height of 300 mm is installed in the lower right portion of the combustion purification device manufactured as described above, and a porous plate 19 and polypropylene resin are mainly used in the upper part of the water tank 17. A scrubber having a filler 20 and a demister 21 was installed. In addition, the lower part of the combustion purification device and the water tank are connected by an inclined pipe, and the spray nozzle 13 is installed on the upper part of the filler 20, so that the cooling water in the water tank 17 circulates, the flow meter 14, the pump 15, etc. To complete the purification device as shown in FIG.

(燃焼式浄化装置の燃焼処理試験)
水槽に深さが150mmになるまで水を注入した後、ポンプ等を稼動してスプレーノズル8及び13から水を噴出させた。また、プロパン(流量15L/min)と空気(流量440L/min)を混合し燃焼させて、ノズルから燃焼室1に導入するとともに、空気を4個の酸素含有ガス導入口から37.5L/minずつ、合計150L/minの流量で側面壁を介して燃焼室1に導入した。次に、排ガスとしてのシラン(流量10L/min)を含む窒素ガス(流量490L/min)を、4個の各ノズルから125L/min、合計500L/minで燃焼室1に導入して燃焼処理を行なった。シランの燃焼処理を20時間行なった後、燃焼式浄化装置からセラミック壁4’と金属壁4”を取出して表面を検査したが、クラック等は検出することはできなかった。
(Combustion treatment test of combustion type purifier)
After water was poured into the water tank until the depth reached 150 mm, the pump was operated to eject water from the spray nozzles 8 and 13. Further, propane (flow rate 15 L / min) and air (flow rate 440 L / min) are mixed and combusted and introduced from the nozzle into the combustion chamber 1, and air is introduced from the four oxygen-containing gas inlets to 37.5 L / min. Each was introduced into the combustion chamber 1 through the side wall at a flow rate of 150 L / min in total. Next, nitrogen gas (flow rate: 490 L / min) containing silane (flow rate: 10 L / min) as exhaust gas is introduced into the combustion chamber 1 from each of the four nozzles at a rate of 125 L / min for a total of 500 L / min. I did it. After the silane combustion treatment for 20 hours, the ceramic wall 4 ′ and the metal wall 4 ″ were taken out from the combustion purification device and the surface was inspected. However, cracks and the like could not be detected.

[実施例2]
(浄化装置の製作)
実施例1の燃焼式浄化装置の製作において、燃焼室1の側面壁4を、図3、図4に示すような構成に替えたほかは実施例1と同様にして燃焼式浄化装置を製作した。また、実施例1と同様にしてスクラバーを設置して、図6に示すような浄化装置を完成した。この装置を用いて実施例1と同様にして燃焼式浄化装置の燃焼処理試験を行なった。その結果、セラミック壁4’と金属壁4”の表面から、クラック等を検出することはできなかった。
[Example 2]
(Production of purification equipment)
In the production of the combustion purification device of Example 1, the combustion purification device was produced in the same manner as in Example 1 except that the side wall 4 of the combustion chamber 1 was changed to the configuration shown in FIGS. . Further, a scrubber was installed in the same manner as in Example 1 to complete a purification device as shown in FIG. Using this apparatus, the combustion treatment test of the combustion purification apparatus was conducted in the same manner as in Example 1. As a result, cracks or the like could not be detected from the surfaces of the ceramic wall 4 ′ and the metal wall 4 ″.

以上のように、本発明の排ガスの燃焼式浄化装置は、実施例に示すように、燃焼室の側面壁の上部表面をセラミック壁、燃焼室の側面壁の下部表面を金属壁で構成するので、燃焼室の側面壁の耐熱性を損なうことなく、クラック等を抑制または防止することができる。   As described above, in the exhaust gas combustion purification apparatus of the present invention, as shown in the embodiment, the upper surface of the side wall of the combustion chamber is composed of the ceramic wall and the lower surface of the side wall of the combustion chamber is composed of the metal wall. Cracks and the like can be suppressed or prevented without impairing the heat resistance of the side wall of the combustion chamber.

本発明の排ガスの燃焼式浄化装置の一例を示す縦断面の構成図Configuration diagram of a longitudinal section showing an example of an exhaust gas combustion purification device of the present invention 図1におけるa−a’断面図A-a 'sectional view in FIG. 本発明の排ガスの燃焼式浄化装置の図1以外の一例を示す縦断面の構成図Configuration diagram of a longitudinal section showing an example other than FIG. 1 of the exhaust gas combustion purification device of the present invention 図3におけるb−b’断面図B-b 'sectional view in FIG. 本発明の排ガスの燃焼式浄化装置の側面壁の例を示す部分拡大断面図The partial expanded sectional view which shows the example of the side wall of the combustion type purification apparatus of the exhaust gas of this invention 本発明の排ガスの燃焼式浄化装置に水槽及びスクラバーの設備を結合した浄化装置の例を示す縦断面の構成図Configuration diagram of a longitudinal section showing an example of a purification device in which a water tank and a scrubber facility are combined with the exhaust gas combustion purification device of the present invention

1 燃焼室
2 火炎を燃焼室へ導入するノズル
3 排ガスを燃焼室へ導入するノズル
4 側面壁
4’通気性のセラミック壁
4”通気性の金属壁
5 酸素含有ガス流路
6 酸素含有ガス導入口
7 排出口
8 スプレーノズル
9 孔
10 線状の間隙
11 格子窓状の間隙
12 冷却配管
13 スプレーノズル
14 フローメーター
15 ポンプ
16 排ガスの燃焼式浄化装置とスクラバー設備間の配管
17 水槽
18 排水管
19 多孔板
20 充填材
21 デミスター
22 処理後のガスを外部へ排出する排出口
DESCRIPTION OF SYMBOLS 1 Combustion chamber 2 Nozzle which introduces flame into combustion chamber 3 Nozzle which introduces exhaust gas into combustion chamber 4 Side wall 4 'Breathable ceramic wall 4 "Breathable metal wall 5 Oxygen-containing gas flow path 6 Oxygen-containing gas inlet 7 Discharge port 8 Spray nozzle 9 Hole 10 Linear gap 11 Lattice window-like gap 12 Cooling pipe 13 Spray nozzle 14 Flow meter 15 Pump 16 Pipe between exhaust gas combustion purifier and scrubber equipment 17 Water tank 18 Drain pipe 19 Porous Plate 20 Filler 21 Demister 22 Exhaust port for discharging treated gas to the outside

Claims (5)

半導体製造工程から排出される排ガスに含まれる有害成分を燃焼する燃焼室、火炎を該燃焼室へ導入するノズル、排ガスを該燃焼室へ導入するノズル、該燃焼室の側面壁、該側面壁の外周に設けられた酸素含有ガス流路、該流路に酸素含有ガスを導入する酸素含有ガス導入口、及び燃焼処理後のガスの排出口にスプレーノズルを備えた燃焼式浄化装置であって、燃焼室の側面壁の上部表面が通気性のセラミック壁、燃焼室の側面壁の下部表面が通気性の金属壁であることを特徴とする排ガスの燃焼式浄化装置。   Combustion chamber for burning harmful components contained in exhaust gas discharged from a semiconductor manufacturing process, nozzle for introducing flame into the combustion chamber, nozzle for introducing exhaust gas into the combustion chamber, side wall of the combustion chamber, An oxygen-containing gas flow path provided on the outer periphery, an oxygen-containing gas introduction port for introducing an oxygen-containing gas into the flow path, and a combustion-type purification device provided with a spray nozzle at the gas discharge port after the combustion treatment, An exhaust gas combustion purification apparatus, wherein the upper surface of the side wall of the combustion chamber is a breathable ceramic wall, and the lower surface of the side wall of the combustion chamber is a breathable metal wall. 燃焼室の側面壁が、円筒の形状である請求項1に記載の排ガスの燃焼式浄化装置。   The combustion-type purification apparatus for exhaust gas according to claim 1, wherein the side wall of the combustion chamber has a cylindrical shape. 酸素含有ガス流路が、環状である請求項1に記載の排ガスの燃焼式浄化装置。   The exhaust gas combustion purification device according to claim 1, wherein the oxygen-containing gas flow path is annular. 燃焼室の側面壁の下部表面を構成する通気性の金属壁の高さが、燃焼室の側面壁全体の高さの5〜30%である請求項1に記載の排ガスの燃焼式浄化装置。   2. The exhaust gas combustion purification apparatus according to claim 1, wherein the height of the breathable metal wall constituting the lower surface of the side wall of the combustion chamber is 5 to 30% of the total height of the side wall of the combustion chamber. 燃焼室の排出側に、粉化物の除去部及び/または酸性ガスの除去部を設けた請求項1に記載の排ガスの燃焼式浄化装置。   The exhaust gas combustion purification apparatus according to claim 1, wherein a dust removal unit and / or an acid gas removal unit is provided on the discharge side of the combustion chamber.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101792586B1 (en) * 2017-03-02 2017-11-02 (주)조선내화이엔지 Semi Dry Reactor Device for incinerator
JP2020034179A (en) * 2018-08-27 2020-03-05 国立大学法人埼玉大学 Combustion furnace of harmful exhaust gas processing device using generation of magnetic fields
CN115183252A (en) * 2022-07-28 2022-10-14 上海协微环境科技有限公司 Tail gas treatment device

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08105618A (en) * 1994-07-25 1996-04-23 Alzeta Corp Combustion breakdown of harmful substance
JPH1054534A (en) * 1996-08-14 1998-02-24 Nippon Sanso Kk Combustion type exhaust gas treating device
JPH1061934A (en) * 1996-08-16 1998-03-06 Nippon Sanso Kk Combustion type exhaust gas treatment apparatus
US6153150A (en) * 1998-01-12 2000-11-28 Advanced Technology Materials, Inc. Apparatus and method for controlled decomposition oxidation of gaseous pollutants
JP2005098680A (en) * 2003-08-20 2005-04-14 Japan Pionics Co Ltd Harmful gas cleaning facility
JP2006194544A (en) * 2005-01-14 2006-07-27 Japan Pionics Co Ltd Noxious gas purifying apparatus
JP2007519878A (en) * 2003-12-19 2007-07-19 アプライド マテリアルズ インコーポレイテッド Apparatus and method for controllably burning gaseous pollutants
JP2008519959A (en) * 2004-11-12 2008-06-12 アプライド マテリアルズ インコーポレイテッド Reactor structure to reduce particle build-up during reduction processing
JP2011174695A (en) * 2005-10-31 2011-09-08 Applied Materials Inc Process abatement reactor

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08105618A (en) * 1994-07-25 1996-04-23 Alzeta Corp Combustion breakdown of harmful substance
JPH1054534A (en) * 1996-08-14 1998-02-24 Nippon Sanso Kk Combustion type exhaust gas treating device
JPH1061934A (en) * 1996-08-16 1998-03-06 Nippon Sanso Kk Combustion type exhaust gas treatment apparatus
US6153150A (en) * 1998-01-12 2000-11-28 Advanced Technology Materials, Inc. Apparatus and method for controlled decomposition oxidation of gaseous pollutants
JP2005098680A (en) * 2003-08-20 2005-04-14 Japan Pionics Co Ltd Harmful gas cleaning facility
JP2007519878A (en) * 2003-12-19 2007-07-19 アプライド マテリアルズ インコーポレイテッド Apparatus and method for controllably burning gaseous pollutants
JP2008519959A (en) * 2004-11-12 2008-06-12 アプライド マテリアルズ インコーポレイテッド Reactor structure to reduce particle build-up during reduction processing
JP2006194544A (en) * 2005-01-14 2006-07-27 Japan Pionics Co Ltd Noxious gas purifying apparatus
JP2011174695A (en) * 2005-10-31 2011-09-08 Applied Materials Inc Process abatement reactor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101792586B1 (en) * 2017-03-02 2017-11-02 (주)조선내화이엔지 Semi Dry Reactor Device for incinerator
JP2020034179A (en) * 2018-08-27 2020-03-05 国立大学法人埼玉大学 Combustion furnace of harmful exhaust gas processing device using generation of magnetic fields
JP7109311B2 (en) 2018-08-27 2022-07-29 国立大学法人埼玉大学 Combustion furnace for harmful exhaust gas treatment equipment using magnetic field generation
CN115183252A (en) * 2022-07-28 2022-10-14 上海协微环境科技有限公司 Tail gas treatment device

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