子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 201 | Fine particle trap for vacuum gas discharge system | JP9752187 | 1987-04-22 | JPS63264118A | 1988-11-01 | MAEBA YOSHIYASU; TOYODA SATOSHI; NARUSE FUMIO |
| PURPOSE: To efficiently trap the fine particles in an introduced gas by consistuting the trap connected to a vacuum pump with a double cylindrical body consisting of a high temp. wall and a low temp. wall. CONSTITUTION: A vessel 1 consists of the double cylinder which has an inlet pipe 3 connected to a vacuum chamber 11 such as a film forming device and an outlet pipe 4 connected to the vacuum pump 2. The vessel 1 consists of an outer cylinder 6 and an inner cylinder 7, and a flow passage 5 is formed between both cylinders. A heater 8 for heating is wound around the outer wall of the outer cylinder 6. Cooling water is introduced/discharged through cooling water pipes 9 to/from the inside of the inner cylinder 7 to keep the inner cylinder 7 in low temp. Consequently, a temp. gradient is generated between both cylinders in the gas flowed in the passage 5 with the result that the fine particles in the gas are stuck to the inner cylinder 7 of low temp. by the movement due to thermophoresis. COPYRIGHT: (C)1988,JPO&Japio | ||||||
| 202 | Method and apparatus for treating dust generated as by-product in amorphous silicon film forming process | JP9665384 | 1984-05-16 | JPS60241918A | 1985-11-30 | YASUI KOU |
| PURPOSE: To shape dust which is difficult and dangerous to treat into a safe solid body with a simple method by mixing collected dust with a noncombustible liquid to obtain a slurry, distilling the slurry by heating to obtain solidified dust, and reutilizing the solidified dust. CONSTITUTION: When a raw gas consisting essentially of silane is decomposed by glow discharge to form an amorphous silicon film on the surface of a drum 1, the solidified silicon in the gas is deposited on the inner wall surface of a film-forming chamber 4, and the other dust is collected in a filtration-dust collection vessel 10 after passing through a discharge pipe S. After the film formation is finished, dust (a) is passed through a flow passage D, collected in a dust hopper 15, and dropped into a bucket 16 filled with a noncombustible liquid such as liquid freon which has affinity for silicon and can be distilled by heating. The dust is mixed with liquid freon to obtain a slurry a'. The bucket 16 is detached from the hopper 15, and heated to evaporate only freon which is cooled and recovered. The dust a' slurry is solidified into a mass a" which is discarded or reutilized as a semiconductor material for solid silicon hydride. COPYRIGHT: (C)1985,JPO&Japio | ||||||
| 203 | Exhaust gas treating equipment | JP4529384 | 1984-03-09 | JPS60190612A | 1985-09-28 | INOUE KOUTAROU |
| PURPOSE:To minimize water consumption through cyclic use of water by obtaining a compact structure in wet-type exhaust gas treating equipment in which water in use is vaporized into steam that is introduced into cooling equipment in order to bring it back into water and then chemicals are dissolved into thus returned water. CONSTITUTION:Exhaust gas is introduced into cylindrical rotary filter elements 11 and 11' in order to treat the gas by means of water-soluble chemicals which are applied to a filter part. Heat treating equipment 21 makes the treated dust- collecting solution, which is situated at the lower part of the exhaust gas treating equipment, vaporize into steam. And water produced through this vaporization is used for dissolved the chemicals. Cooling equipment 18 is used to bring the steam back into water. And as the quantity of the water increases, a cooling cylinder 29 rotates, taking a supporting lever 30 as a fulcrum, thereby shifting the water to a tank 41. For water supply, an automatic water supplying equipment 43 opens its valve by means of wind pressure only when the exhaust gas is introduced for treatment. | ||||||
| 204 | Liquid flowing sheet | JP1989482 | 1982-02-09 | JPS57207794A | 1982-12-20 | JIYORUJIYU JIYATSUKU POORU UJI |
| 205 | Method of treating exhaust gas obtained in blast furnace | JP3513781 | 1981-03-11 | JPS56139121A | 1981-10-30 | SEODOA UORUTAA NERUSON JIYUNIA; DEEBITSUDO BURUUSU KOOKURU; JIYOERU ZEBU UORUFU; RARII ARAN GIYANZERU |
| 206 | Method of purifying exhaust from lacquer atomizing chamber | JP15604280 | 1980-11-07 | JPS5695318A | 1981-08-01 | HAINTSU JIIBERUZU |
| In a process for purifying exhaust air from paint-spraying-booths by scrubbing the spray mist with a scrubbing medium, particularly water, the spray particles are emulsified in the scrubbing medium with the addition of an emulsifier, at least a part of the emulsion is subjected to ultrafiltration and the ultra-filtrate is re-used as scrubbing medium. Among substances which can be used as emulsifier, are paraffin-sulphonates, olefin- sulphonates, alkylbenzenesulphonates, polyhydric alcohols, and diethylene glycol. | ||||||
| 207 | JPS5530888B2 - | JP12448672 | 1972-12-13 | JPS5530888B2 | 1980-08-14 | |
| 208 | JPS5220438B1 - | JP5232062 | 1962-11-21 | JPS5220438B1 | 1977-06-03 | |
| 209 | Gasuno senjohoho | JP11217775 | 1975-09-18 | JPS5157073A | 1976-05-19 | FURITSUTSU TSUIMAAMAN; AASAA RENKU |
| 210 | JPS50122746A - | JP2893475 | 1975-03-10 | JPS50122746A | 1975-09-26 | |
| 211 | JPS4943632B1 - | JP8707768 | 1968-11-29 | JPS4943632B1 | 1974-11-22 | |
| 212 | スクラバ排水の処理方法及びスクラバ排水の処理装置 | JP2017506124 | 2016-01-28 | JP6330968B2 | 2018-05-30 | 花井 洋輔; 石川 菜美; 酒井 保藏 |
| 213 | 塗装設備 | JP2015033000 | 2015-02-23 | JP6310871B2 | 2018-04-11 | 瀧澤 幸也; 三輪 朋孝 |
| 214 | 尿素製造プラント | JP2015510203 | 2013-05-02 | JP6306571B2 | 2018-04-04 | ヨハネス・ヘンリクス・メンネン; ヨゼフ・ヒュベルト・メーセン |
| 215 | 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。 | ||||||
| 216 | チャンバを空にして該チャンバから取り出されたガスを浄化するための装置及び方法 | JP2014546495 | 2012-12-12 | JP6138144B2 | 2017-05-31 | ハイナー・ケスタース; ウーヴェ・ゴッチュリッヒ |
| 217 | 排ガススクラバー用の遠心分離機及びその運転方法 | JP2015152521 | 2015-07-31 | JP5829352B1 | 2015-12-09 | 佐野 裕二; 渡辺 雄輔; 桶谷 尚史 |
| 【課題】 簡単な構成で遠心分離機の分離室から排出する廃棄物中の固形成分濃度を高濃度に安定させ、廃棄物の排出量を削減することができると共に廃棄物としての保管スペースを削減することができる遠遠心分離機を提供する。 【解決手段】 本発明の分離板型遠心分離機は、複数のグループに分割された初期濁度と上記複数の初期濁度のグループそれぞれに対応する複数のΔNTUから作成された排出トリガーテーブルを格納するメモリ17Aと、排出トリガーテーブルの初期濁度とこの初期濁度に対応するΔNTUに基づいて分離室15内の固形成分Sを排出する排出基準値を求める中央演算処理装置17Bと、を有するコントローラ17を備えている。 【選択図】図1 |
||||||
| 218 | チャンバを空にして該チャンバから取り出されたガスを浄化するための装置及び方法 | JP2014546495 | 2012-12-12 | JP2015500944A | 2015-01-08 | ハイナー・ケスタース; ウーヴェ・ゴッチュリッヒ |
| 本発明は、チャンバ(14)を空にし、チャンバ(14)から取り出されたガスを、あらゆる異物から浄化するための装置に関する。その装置は、空にされるべきチャンバ(14)に接続された入口(17)を有する乾燥濃縮真空ポンプ(15)であって、出口(18)における変動状態にもかかわらず、入口圧力を一定レベルに維持するのに適切な乾燥濃縮真空ポンプ(15)を有する。乾燥濃縮真空ポンプ(15)の出口(18)に接続する中間ライン(19)と、流体リング真空ポンプ(20)であって、その入口が中間ライン(19)に接続されている流体リング真空ポンプ(20)とが、付加的に設けられている。本発明は、また、対応する方法に関する。本発明は、そのガスをあらゆる異物から確実かつ効果的に浄化することを可能にする。 | ||||||
| 219 | スクラバシステム及び方法 | JP2014531174 | 2012-09-12 | JP2014528827A | 2014-10-30 | イェンス・ピーダ・ハンセン |
| 本発明は、船舶の船用エンジンまたは船用ボイラーからの排ガス由来のSO2を除去する方法に関連する。上記船用エンジンまたは船用ボイラーからの排ガスは、第一スクラバセクション(2)内で海水によって冷却及び洗浄され、その後、第二スクラバセクション(4)内で、アルカリ化学物質(11)の添加を伴って循環する淡水で洗浄される。洗浄に使用される上記循環する淡水は、第一スクラバセクション(2)内で冷却用に使用される海水よりも温かい。上記温かい淡水は、冷たい海水と間接的に熱交換される。さらに本発明は、対応するスクラバシステムと関連する。 | ||||||
| 220 | Ammonia recovery unit and recovery methods | JP2009243169 | 2009-10-22 | JP5501730B2 | 2014-05-28 | 佐藤 文昭; 裕之 古市; 雄大 加藤; 一男 石田 |
| A method includes a first step of introducing an ammonia-containing wastewater to a CO 2 ·H 2 S stripper maintained to have a pressure higher than atmospheric pressure, and discharging CO 2 and H 2 S in a form of gas having a low moisture concentration from a tower top of the CO 2 ·H 2 S stripper while discharging an ammonia-containing solution from a tower bottom of the CO 2 ·H 2 S stripper; a second step of introducing the ammonia-containing solution obtained after the first step into an ammonia stripper which is maintained to have a lower pressure than that of the CO 2 ·H 2 S stripper, and thereby discharging a gas rich in ammonia containing a small amount of H 2 S and CO 2 from a tower top of the ammonia stripper while discharging water usable as industrial water from a tower bottom of the ammonia stripper; and a third step of introducing the ammonia rich gas obtained after the second step into a washing tower which is maintained to have a lower pressure than that of the ammonia stripper, and wherein the third step includes a washing step with a Na-containing base reagent thereby discharging a wastewater containing a Na compound from a tower bottom of the washing tower while discharging a substantially H 2 S-free purified gas rich in ammonia from a tower top of the washing tower. | ||||||
QQ群二维码
意见反馈
意见反馈