序号 | 专利名 | 申请号 | 申请日 | 公开(公告)号 | 公开(公告)日 | 发明人 |
---|---|---|---|---|---|---|
181 | Engine exhaust gas treatment apparatus | US53271155 | 1955-09-06 | US2878107A | 1959-03-17 | RUTH JOSEPH P |
182 | Apparatus for and method of water supply control for dust collectors | US18080250 | 1950-08-22 | US2645304A | 1953-07-14 | MCILVAINE ROBERT L |
183 | Machine for making air cleaner filter units | US13097237 | 1937-03-15 | US2154081A | 1939-04-11 | ANDERSON JOSEPH A; HUNT LOGAN G |
184 | Gas washing apparatus | US57628831 | 1931-11-20 | US1927486A | 1933-09-19 | BRASSERT HERMAN A; BARRETT FREDERICK W; GRILLI JOHN P |
185 | 除害装置 | JP2014231944 | 2014-11-14 | JP6370684B2 | 2018-08-08 | 山田 俊樹; アレクサンダー マイケル ポープ; アリスター ベネット; スティーブン バーロー; クリストファー ペーター ジョーンズ |
186 | 排気ガスの除塵方法及び除塵剤 | JP2017537977 | 2016-01-15 | JP2018501954A | 2018-01-25 | ウェイ シェンホワ; ガオ ダオロン; ゾウ メイホワ; フー チュン |
本発明は排気ガスの除塵方法及び除塵剤に関する。前記方法は、塵含有排気ガス(1)と有機除塵剤(4)とをそれぞれ除塵塔(3)に進入させるとともに、塔内で接触し、塵含有排気ガス(1)における少なくとも一部の水蒸気が凝縮し、有機除塵剤(4)及び凝縮水が塵含有排気ガス(1)中の固体粒子、酸性汚染物、有機汚染物及び/又は重金属化合物を吸着するステップと、得られた浄化ガスを放出するか、或いは後続プロセスに移行するステップとを含む。前記有機除塵剤は、無毒性高沸点有機溶媒組成物を含んでおり、食用油、シリコーンオイル、変性シリコーンオイル、液状アスファルト油、キリ油、液状パラフィン油、鉱物油、パーム油および廃食用油から選ばれる2種又は2種以上である。 | ||||||
187 | 空気浄化装置 | JP2012106706 | 2012-05-08 | JP5991849B2 | 2016-09-14 | 藤田 雅司; 山中 弘次; 土井 雄太; 山下 幸福 |
188 | 家畜小屋の排気浄化装置および排気浄化方法 | JP2015078385 | 2015-04-07 | JP2015221031A | 2015-12-10 | スフェン・キュネン |
【課題】洗浄液で濡らされることができ、かつ/または洗浄液を吸収することができるフィルタ本体を含む少なくとも1つの排気スクラバー;および洗浄液を保持する洗浄液容器を含む家畜小屋の排気浄化装置を提供する。 【解決手段】少なくとも1つの排気スクラバー10が移動装置上に配置され、該移動装置が、少なくとも1つの排気スクラバー10を洗浄液容器20中の洗浄液に完全または部分的に浸漬させるように、設計および配置する。 【選択図】図1 |
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189 | ガス浄化装置 | JP2014558259 | 2013-02-22 | JP2015509445A | 2015-03-30 | マラ,ヨハン |
本発明は、任意の相対湿度において高いガス浄化効率を有するガス浄化装置を提案する。この装置は、ガス流の通路(10)と;ガス流に対して透過性を示す親水性キャリア(12)であって、この親水性キャリア(12)の少なくとも一部が、ガス流の通路内に位置付けされており、且つガス流の通路でガスに接触するような試薬を収容するように構成されている、親水性キャリアと;キャリアに液体を分配するための分配装置(14)と;この分配装置に関連付けられた制御装置(16)であって、この制御装置(16)は、分配装置を制御して、溶解試薬の水溶液をキャリアに分配し、その後、ガスの湿度が第1の湿度閾値を下回る場合に、分配装置を制御して液体を分配し、ガスの湿度が第2の湿度閾値を上回る場合に、液体を分配するのを停止するように構成される、制御装置と;を有する。 | ||||||
190 | The composition for wet air scrubber and operation and cleaning method of a wet air scrubber with it | JP2012527976 | 2010-08-31 | JP2013503041A | 2013-01-31 | イー. シンプソン,ウイリアム; ダブリュ. ケネディー,キース; エー. グリンステッド,デイル; エフ. コフリン,マイケル; ジェー. ローチ,ケネス; リオン,スティーヴン; ジェー. ライレイ,メイナード; ダブリュ. クロスデイル,ガリィ |
A composition for use in air scrubbers, and particularly, cleaning air scrubbers is provided, along with methods for cleaning air scrubbers using the same. The composition includes at least one of components A, B, C, and D. Component A includes at least one surfactant and at least one enzyme. Component B includes at least one surfactant. Component C includes at least one pH control agent. Component D includes at least one defoamer. The compositions may be used to remove volatile organic compounds from air. | ||||||
191 | Wet exhaust gas purification device | JP2011106548 | 2011-05-11 | JP2012236143A | 2012-12-06 | HOSONO TAKAMICHI; YOSHIZAWA KATSUHIRO; TAKADA HIROTAKA; IWASAKI HIDEKAZU; NISHIMURA MOTOHIKO; HIGASHIDA MASANORI |
PROBLEM TO BE SOLVED: To provide a wet exhaust gas purification device that enables the simple removal of PM accumulated in a demister, enables the use of a low porosity, high collection efficiency demister, and exhibits high exhaust gas purification efficiency.SOLUTION: This wet exhaust gas purification device uses a heating means for heating a demister 50 (51) to heat it to a temperature (60°C) at which the viscosity of PM that is accumulated in the demister 50 (51) and that contains an oil component reaches a low viscosity, or a temperature (equal to or more than 600°C) at which the PM that contains an oil component self ignites. As a result, PM which has been softened into a liquid state and has begun to form drips can be washed away by wash water (at a normal temperature or heated). Alternatively, after the PM has been burned away, any residue can be completely removed. Thus, the wash time and volume of wash water required for the removal of the PM are negligible. After the removal of PM, the demister 50 (51) can be re-used in a state that is almost as good as new. | ||||||
192 | Method of mass transfer, regularly packing and mass transfer apparatus for small liquid load | JP2011279220 | 2011-12-21 | JP2012130911A | 2012-07-12 | WICKI WERNER; DUSS MARKUS; AUSNER ILJA |
PROBLEM TO BE SOLVED: To provide a method of mass transfer, a regularly packing for performing the method of mass transfer, and a mass transfer apparatus for performing the method of mass transfer.SOLUTION: The method of mass transfer includes the steps of supplying a first fluid and a second fluid into the mass transfer apparatus, wherein the mass transfer apparatus includes a vessel which has a head region, a base region and a mass transfer region, wherein the first fluid is brought into contact with the second fluid at least in the mass transfer region, wherein the mass transfer region is arranged between the head region and the base region and the mass transfer region includes the regularly packing which includes a plurality of neighboring layers of fabric which includes fiber strands of a non-metallic material. The mass transfer apparatus is operated at a fluid load of at most 3 m/m/h. The fabric of the regularly packing includes fiber strands of the non-metallic material which are formed as weft threads, wherein the weft threads have a yarn count of at least 100 g/1,000 m and the weft threads include at least 20 yarns/25.4 mm. | ||||||
193 | Outflow scrubbing and moisture removal system control has been improved | JP2011535680 | 2009-11-06 | JP2012508105A | 2012-04-05 | ダニエル オー クラーク; ジェイ ジュン; ジョージ エル ザ サード ダンセン; フィル チャンドラー; フランク フーシュダラン; アレン フォックス; ダン エス ブラウン; バリー ペイジ |
本明細書では改善された流出物処理装置が提供される。 幾つかの実施形態において、除去システムは、流出ストリームが貫通して流れる排出導管と、流出ストリームから非排出可能流出物を除去するために排出導管内に配置される複数の充填床と、流出ストリームから非排出可能流出物を除去するために流出処理剤を隣接する充填床間に提供する1つ又はそれ以上の噴霧ジェットと、最上充填床上で排出導管内に配置され、大きな液滴の流出処理剤を提供して、微細液滴を実質的に形成することなく最上充填床の上側表面から粒子状物質を湿潤させリンスするドリッパーと、を含むことができる。
【選択図】図2 |
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194 | Air filtering apparatus | JP2006044012 | 2006-02-21 | JP4878865B2 | 2012-02-15 | 紀雄 福島; 徹 荒川 |
In an air filtering apparatus including a gas-liquid contact member (5) disposed in a housing (2), an electrolytic water supply pipe (17) for dropping electrolytic water to the gas-liquid contact member and an air blowing fan (7) for blowing air to the gas-liquid contact member to which the electrolytic water infiltrates and blowing out the air to a room, a first sheet member (76) having water retentivity for distributing the electrolytic water dropped from the electrolytic water supply pipe to the gas-liquid contact member is disposed above the gas-liquid contact member, and the first sheet member is equipped with recess portions (76D) at which scale accumulates when hardness components in the electrolytic water precipitate as the scale, or cut-out portions (92) through which the electrolytic water is positively discharged when hardness components in the electrolytic water precipitate as scale and accumulates on the first sheet member. | ||||||
195 | Liquid delivery portion of the contact device | JP2001546755 | 1999-12-20 | JP4672948B2 | 2011-04-20 | カルティン、ラルス; ビャルノ、オッド、イー |
196 | Distribution of gas and liquid in the contact device | JP2001546770 | 1999-12-21 | JP4671572B2 | 2011-04-20 | カルティン、ラルス; ビャルノ、オッド、イー |
197 | Molded packing element | JP2000574323 | 1999-08-18 | JP3542776B2 | 2004-07-14 | ルコベナ,フランク |
198 | Molded packing element | JP2000574323 | 1999-08-18 | JP2003506198A | 2003-02-18 | ルコベナ,フランク |
(57)【要約】 円筒状本体部材の内部に複数の対称的に配置された細分割部分を有するパッキング要素が、非常に強く、大きな表面積を有する高温と腐食性媒体とに抵抗性のある構造を提供する。 | ||||||
199 | Column for refining solvent-containing gas and method therefor | JP2766797 | 1997-02-12 | JPH09225244A | 1997-09-02 | BUERUNAA ZUIIBUERESU; GIYUNTAA MIYURAA |
PROBLEM TO BE SOLVED: To treat gas with the fewest possible packing materials without impairment of refining efficiency by passing liquid in a counter current to the gas at an adjustable velocity from the bottom to peak of a column and determining the height of the column in accordance with specific equation at the time of treating the gas. SOLUTION: The column for removing or recovering the components below the half amt. of the gas from the gas has an inlet and outlet port for the gas, an inlet and outlet port for the scrubbing liquid and a fluid packed bed. The gas is passed in the counter current to the gas at the adjustable velocity from the bottom to the peak of the column. At this time, the height of the column is set at the required height in accordance with the height H=k 1.SZ.SH (where, k 1=1.5 to 2.5., SZ is expressed by equation 2 [ye is the molar fraction of the components in the gas in a gas inlet and ya in a gas outlet, y*e is the equil. molar fraction of the components in the liquid at the gas inlet temp. and y*a at the gas outlet temp.] SH is expressed by equation 3 (k 2=1.5 to 2.5.d is the size of the fluid, F is a fluid number, S is a Schmidt number). The column is optimized in such a manner. COPYRIGHT: (C)1997,JPO | ||||||
200 | Gas washing equipment | JP31911895 | 1995-12-07 | JPH08299748A | 1996-11-19 | GIYUNTAA HAA KISU |
PROBLEM TO BE SOLVED: To provide a gas washing equipment which is improved by a multi- stage gas washer so as to be far favorable than conventional equipments with respect to design, assembling, maintenance and safety and reliability of operation. SOLUTION: This gas washing equipment purifies exhaust gas generated by gasification of all wastes such as domestic and industrial wastes and/or synthetic gas. For this purpose, if necessary, the gas is subjected to several washing processes having various washing liquids at different temperatures. All these different processes are performed in a pressurized vessel which is single, small-sized, horizontal and provided with not a few washing steps (A)-(E) arranged mutually apart a space. The respective washing steps are mutually separated by partitions 4, 5, 6 which are vertical, disc-shaped and provided with passing holes of each a large surface area. Each washing step is provided with its own sump and inspection hole 8. COPYRIGHT: (C)1996,JPO |