| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | Method and device for separating particle substance from gas | JP8700481 | 1981-06-08 | JPS57204251A | 1982-12-14 | JIYOSEFU JII UIRUSON SHINIA |
| 142 | Exhaust gas-purifier | JP4310581 | 1981-03-26 | JPS57159563A | 1982-10-01 | MURAKAMI TOSHIO |
| PURPOSE: To prolong the life of a catalyst in a denitrifying reactor or the like operated at high dust concentration, in an exhaust gas-purifier for a coal-burning boiler, by locating a secondary dust-collector at the upperstream side of the denitrifier. CONSTITUTION: A plurality of axial-flow straight-driving cyclones 9 are located in a flue 6 at the upperstream side of a denitrifying reactor 2, and a hopper 8 to collect dust separated by the cyclones 9 is located at the bottom of the flue 6. As a result, larger-particle size dust which has a substantial influence on the abrasion of a catalyst is preremoved by the secondary dust-collector composed of the arranged cyclones 9, so that the life of the catalyst is prolonged. Moreover, the height of the reactor 2 can be decreased by the arrangement of the secondary dust-collector. In adition, the fraction of electrically collected dust in the latter stage is not necessary, since the larger-particle size dust is preremoved. COPYRIGHT: (C)1982,JPO&Japio | ||||||
| 143 | JPS5717754U - | JP9427280 | 1980-07-03 | JPS5717754U | 1982-01-29 | |
| 144 | JPS5651971Y2 - | JP15990377 | 1977-11-29 | JPS5651971Y2 | 1981-12-04 | |
| 145 | Dust collector | JP15216278 | 1978-12-07 | JPS5579061A | 1980-06-14 | SUZUKI TAKESHI; MURAO MIKIO; TAKAGISHI MASAHARU; AIZAWA KIYOSHI |
| PURPOSE: To provide a small size equipment with enhanced dust collecting efficiency and reduced pressure loss by a mechanism wherein a cylindrical body forming a vortex chamber having circular sectional area and horizontal axial line is provided to a cyclon dust collector, and gas guided in the tangent direction is spirally passed in the direction of axial line. CONSTITUTION: Gas which contains powder is introduced from the inlet duct 1 into the vortex chamber 3 of the cylindrical body 2 in the direction of tangent. The gas revolves along the guide plate 10 without causing turbulent flow and is discharged from the outlet duct 5. The gas vortex causes pressure to be reduced around the opening zone 12 at the downstream of a vortex direction as compared with the opening zone 11 at the upstream of vortex direction. This causes part of vortex gas to be passed from the opening 11 through the spaces 14a, 14b between the collector guide plate 13 and the internal wall 8a of the hollow conical body 8 provided at the lower part of the cylinder 2. The gas further passes through the spaces 16a, 16b formed by the guide plate 13, the internal walls 8a, 8b, and 8c, and the vortex guide plate 10, then the gas is sucked in the opening 12. Centrifugal force causes powder in the gas to be located near the internal wall of the cylinder 2 at high concentration and falled through the space 14a, 14b to be separated. COPYRIGHT: (C)1980,JPO&Japio | ||||||
| 146 | JPS5418422B2 - | JP3015373 | 1973-03-16 | JPS5418422B2 | 1979-07-07 | |
| 147 | JPS5485478U - | JP15990377 | 1977-11-29 | JPS5485478U | 1979-06-16 | |
| 148 | JPS5414348B2 - | JP10230871 | 1971-12-18 | JPS5414348B2 | 1979-06-06 | |
| 149 | System for separating contaminants from liquid | JP2406076 | 1976-03-05 | JPS51113254A | 1976-10-06 | UORODEIMAIYAA DAIYACHIYUUKU; RIYUUBEN ENU PAAMU |
| 150 | JPS492155A - | JP3015373 | 1973-03-16 | JPS492155A | 1974-01-10 | |
| 151 | JPS4867855A - | JP10230871 | 1971-12-18 | JPS4867855A | 1973-09-17 | |
| 152 | ごみ分離システム | JP2018098718 | 2018-05-23 | JP6619842B2 | 2019-12-11 | 永田 壽也; 金 成秀 |
| 153 | エアクリーナ | JP2016174941 | 2016-09-07 | JP2017029982A | 2017-02-09 | クリスコ, ウィリアム, ジェイ.; ビショップ, ウェイン, アール., ダブリュー.; ジエセケ, スティーブン, スコット; フィナティー, キャロライン, ジェイ.; ネルソン, デイヴィッド, ダブリュー. |
| 【課題】改良されたエアクリーナの提供 【解決手段】複数の遠心分離装置13を有する予備クリーナ8を含む第1段を備え、予備クリーナの下流側のエアフィルタカートリッジ22を含む第2段を備え、エアクリーナカートリッジ22は流入面23とその反対側の流出面24とを有して直線上に流れる濾材構造物を備え、エアフィルタカートリッジ22は前記濾材構造物の周りの全周に伸びるシール部材28を備え、シール部材28は前記第1段と前記第2段との間にシールを形成する、エアクリーナ1。 【選択図】図2 |
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| 154 | サイクロン式セパレータモジュール | JP2014100612 | 2014-05-14 | JP5837136B2 | 2015-12-24 | 何 玉 佩 |
| 155 | サイクロン式セパレータモジュール | JP2014100612 | 2014-05-14 | JP2015217317A | 2015-12-07 | 何 玉 佩 |
| 【課題】限られたスペースに複数のサイクロン分離部を設けても簡単に配管可能で配置自由度を高くする。 【解決手段】サイクロン式気流が発生する分離チューブ3と、第1の接合口411と第3の接合口413との間に空間的に連通する第1の連通路43と、第2の接合口412と第3の接合口413との間に空間的に連通する第2の連通路44とが形成された接合弁4とを備えている。1つの分離チューブ3を選択的に1つの接合弁4により連結することで第1のろ過モジュールAを形成し、又は、2つの接合弁4により連結することで第2のろ過モジュールBを形成する。 【選択図】図3 |
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| 156 | Air cleaner | JP2013090793 | 2013-04-23 | JP2013208611A | 2013-10-10 | KRISKO WILLIAM J; BISHOP WAYNE R W; GIESEKE STEVEN SCOTT; FINNERTY CAROLYN J; NELSON DAVID W |
| PROBLEM TO BE SOLVED: To provide an improved fluid cleaner assembly.SOLUTION: A fluid cleaner assembly 1 includes a filter element 22, and a safety filter element 20. The fluid cleaner assembly generally includes a housing 2 having a cover 7 and a primary fluid cleaner section 9. The filter element generally includes a z-filter media construction arranged in a straight through configuration, and an axial seal gasket 28 positioned to extend continuously around at outer perimeter of the straight through flow construction. The fluid cleaner assembly can have a precleaner 8 positioned therein. There are provided methods of assembly and use. | ||||||
| 157 | Removal method and apparatus of the volatile components from the fumes flow | JP2001393817 | 2001-12-26 | JP4663935B2 | 2011-04-06 | デュダ ジャン−ピエール; ジョルジュ セルジュ |
| 158 | Boiling water reactor and steam separator | JP2009213089 | 2009-09-15 | JP2011064481A | 2011-03-31 | YAMADA YUJI |
| PROBLEM TO BE SOLVED: To provide a boiling water reactor that reduces the difference between the water level at a position of the central axis of a reactor pressure vessel and that on the periphery of it by suppressing the lowering of the strength of a shroud head. SOLUTION: In the boiling water reactor 1, steam separators 6 are laid out inside a cylindrical steam dryer skirt 19 above the shroud head 5 in the reactor pressure vessel 2. Stand pipes 7 of the steam separators 6 are mounted on the shroud head 5. The cross-sectional shapes of the stand pipes 7 are streamline, and pre-heads 16, the tips of the streamlines, are laid out toward the central axis of the reactor pressure vessel 2. The cross-sectional shapes of the stand pipes 7 are streamlined and the tips of the streamlines are oriented to the central axis of the reactor pressure vessel 2, so that the geometrical loss of the stand pipes 7 can be reduced, thereby reducing the difference between the water level 24 in the vicinity of the central axis of the reactor pressure vessel 2 and the water level 25 at a position on the inside surface of the steam dryer skirt 19. COPYRIGHT: (C)2011,JPO&INPIT | ||||||
| 159 | Self-priming solid-liquid separation device | JP2010026493 | 2010-02-09 | JP4621802B1 | 2011-01-26 | 洋次 唐沢; 浩二 坂本; 洋二 森; 康一 芳賀 |
| The present invention is to provide a solid-liquid separator with self-priming pump with which wear of a self-priming liquid pump connected to a cyclone mechanism can be prevented and a solid-liquid mixture can be purified at a low cost without requiring a special arrangement (special material or special structure) for the pump. In the solid-liquid separator which is connected with self-priming pump, used to separate sludge in the liquid by cyclone mechanism arranged in separation portion, wherein, the separation portion is directly or indirectly connected to a suction system of the self-priming liquid pump that is an upstream side of the pump portion, the separation portion has a first and second cyclone mechanisms, said first cyclone mechanism is disposed in said second cyclone mechanism in coaxial, the liquid including sludge is introduced firstly into the first cyclone mechanism, and second, the liquid separated by the first cyclone mechanism is introduced into the second cyclone mechanism, the under space of the both cyclone mechanism, a tank is disposed, and the sludge separated from the liquid is collected to the tank. | ||||||
| 160 | Hydro-cyclone apparatus, and, hydrocyclone equipment | JP2009550658 | 2007-11-28 | JP2010519028A | 2010-06-03 | ホルガー ブラム |
| その上方前側（０）での液体供給のための上方開口、及び、その下方前側（Ｕ）での清浄水排水のための開口を有する、分離チューブ（Ｔ）と、分離チューブ（Ｔ）の下方端に懸濁液を集めるための、少なくとも１つの接線方向のチューブ部（Ｏ）と、清浄水排水に液圧接続されるとともに、分離チューブ（Ｔ）の中央部に配置されるフィルタエレメント（Ｆ）と、を備えるハイドロサイクロン装置。 分離チューブ（Ｔ）内の、液体高給のための上方開口（Ｏ）と、フィルタエレメント（Ｆ）との間にある回転エレメント（Ｒ）は、分離チューブに対して軸方向の中央部に設けられ、回転支持され、そのフィルタエレメントが可変可能な回転スピードでの駆動に適合する。 ハイドロサイクロン設備は、液圧接続された上記複数のハイドロサイクロン装置を備える。
【選択図】図１ |
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