| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 161 | Gas-liquid separator, and the gas-liquid separator an exhaust gas purifying apparatus using, or air cleaning apparatus, or air disinfection purification device | JP2004292005 | 2004-10-04 | JP4412601B2 | 2010-02-10 | 大志 小林; 敏樹 小林 |
PROBLEM TO BE SOLVED: To provide a gas-liquid separator without enlarging the size and with simple constitution, which can effectively separate PM (particulate matter) in the exhaust gas or dust of toxic fine particles in gas like air, surely separate and collect even liquid attached to the gas-liquid separator containing a part of toxic substance, difficult to collect in the past, and prevent flowing out to the outside. SOLUTION: An outer cylinder member 21 having a small diameter cylinder 23 imparting rotational force to an object gas-liquid mixture to be cleaned and flowed flowing in, is provided on the downstream side of a flowing-in port 22 formed on one end. Cylindrical bodies 27, 28 are adjacently disposed each other on the downstream side of the outer cylinder member. A communicating tube 30 with a smaller diameter than the cylindrical bodies is interposed between the cylindrical bodies to communicate them. A liquid receiver 32 is installed under the cylindrical bodies, and a gas outlet port 33 is provided at the most down stream side of the cylindrical bodies. COPYRIGHT: (C)2006,JPO&NCIPI |
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| 162 | Multi-cell cyclone | JP2002249528 | 2002-08-28 | JP4342778B2 | 2009-10-14 | コペック エドバルト; ドボラチェク クレメンス; ハーン ジェンス; グライフ フォルカー; ハルトマン マリオン |
| 163 | Gas-liquid separator, exhaust gas cleaning apparatus using the same, or air cleaning apparatus or air sterilizing and cleaning apparatus | JP2004292005 | 2004-10-04 | JP2006102618A | 2006-04-20 | KOBAYASHI TOSHIKI; KOBAYASHI HIROSHI |
| <P>PROBLEM TO BE SOLVED: To provide a gas-liquid separator without enlarging the size and with simple constitution, which can effectively separate PM (particulate matter) in the exhaust gas or dust of toxic fine particles in gas like air, surely separate and collect even liquid attached to the gas-liquid separator containing a part of toxic substance, difficult to collect in the past, and prevent flowing out to the outside. <P>SOLUTION: An outer cylinder member 21 having a small diameter cylinder 23 imparting rotational force to an object gas-liquid mixture to be cleaned and flowed flowing in, is provided on the downstream side of a flowing-in port 22 formed on one end. Cylindrical bodies 27, 28 are adjacently disposed each other on the downstream side of the outer cylinder member. A communicating tube 30 with a smaller diameter than the cylindrical bodies is interposed between the cylindrical bodies to communicate them. A liquid receiver 32 is installed under the cylindrical bodies, and a gas outlet port 33 is provided at the most down stream side of the cylindrical bodies. <P>COPYRIGHT: (C)2006,JPO&NCIPI | ||||||
| 164 | Material dewatering device | JP2004501076 | 2003-04-29 | JP2005523815A | 2005-08-11 | シーラック，クリストファー・フレデリック・ニーラン |
| 本願発明は空圧式脱水装置（１）を提供することを目的とする。 装置（１）は主に中心のファン（３）に接続されたサイクロン室（２）を備える。 渦流れ離脱区画に夫々追従された種々の渦流れ形成ステーション（６）が、サイクロン室（２）内に設けられる。 しっかりとした求心渦が形成されてから、水分がサイクロン室から溜め（４２）内に出されるように離脱される。 | ||||||
| 165 | Recirculating steam generator with a removable cyclone separator | JP17970694 | 1994-07-08 | JP3574183B2 | 2004-10-06 | クリストフ・プーシン; ベノワ・ギラウド |
| 166 | Coolant cleaning device | JP2003115005 | 2003-03-10 | JP2004268244A | 2004-09-30 | YAMAZAKI MINORU; HONDA TAKAMITSU; KAMEI HIROTO |
| PROBLEM TO BE SOLVED: To provide a coolant cleaning device of adopting a novel method for staying no chip in a bottom part of all coolant tanks for constituting the coolant cleaning device in the coolant cleaning device for processing a coolant including chips of a magnetic substance flowed out of an industrial machine such as a machine tool, and adjusting oil temperature of the coolant. SOLUTION: This coolant cleaning device is equipped with a magnetic separator 11, a bottomed cylindrical primary circular coolant tank 13 for generating a vortex flow 35 in the coolant, and an oil temperature automatic adjuster 19, and is equipped with a bottomed cylindrical secondary circular coolant tank 15 for generating a vortex flow 42 in the coolant, respective coolant sucking means for sucking the coolant in the respective circular coolant tanks, and a coolant pump 16, and is equipped with a primary clean tank 17 communicated with the primary circular coolant tank 13, and a coolant pump 22, and is provided with a secondary clean tank 23 communicated with the secondary circular coolant tank 15. COPYRIGHT: (C)2004,JPO&NCIPI | ||||||
| 167 | Steam separator | JP2003034489 | 2003-02-13 | JP2004245656A | 2004-09-02 | NISHIDA KOJI |
| PROBLEM TO BE SOLVED: To provide a steam separator which can reduce carryover even if steam quality is large and has a simple structure. SOLUTION: The separator is characterized in that droplets which are generated through the collision of steam with the water surface around the steam separator 1 are eliminated even if the steam quality is large to reduce the carryover by setting up numerous flow channel holes 20 in a second-stage inner cylinder 14 and a second-stage outer cylinder 15 constituting a steam separation section 4 on a second stage from the lower part of the steam separator 1, filling demister 21 between the second-stage inner cylinder 14 and the second-stage outer cylinder 15 and separating vapor and liquid in the demister section 21. COPYRIGHT: (C)2004,JPO&NCIPI | ||||||
| 168 | Gas-liquid separator | JP2001391043 | 2001-12-25 | JP2003190725A | 2003-07-08 | SAKAKIBARA YASUFUMI; UENO HARUHIKO |
| <P>PROBLEM TO BE SOLVED: To provide a gas-liquid separator reduced in pressure loss. <P>SOLUTION: In the gas-liquid separator A, a cylindrical introducing cylinder 2 capable of permitting a two-phase gas-liquid fluid before gas-liquid separation to pass while revolving the same and a cylindrical lead-out cylinder 3 capable of permitting the gas phase after gas-liquid separation to pass are coaxially provided to both ends in the axial direction of a cylindrical outer cylinder 1 and a discharge cylinder 4 capable of discharging the liquid phase after gas- liquid separation is provided in the vicinity of the end surface, position in the axial direction on the side of the introducing cylinder 2 of the outer cylinder 1. The outflow opening 2a of the introducing cylinder 2 and the lead-out port 3a of the lead-out cylinder 3 are respectively protruded into the outer cylinder 1 in the axial direction thereof by Lin and Lout so as to be opposed to each other in a state axially separated by a predetermined distance L. Since the two-phase gas-liquid fluid passing through the gas-liquid separator A while revolving flows linearly in one direction, the flow direction thereof is not changed suddenly and the pressure loss generated in the gas-liquid separator A is reduced as compared with a cyclone type revolving gas-liquid separator. <P>COPYRIGHT: (C)2003,JPO | ||||||
| 169 | Filter apparatus | JP4021193 | 1993-03-01 | JP3386170B2 | 2003-03-17 | マンデル ミナー アイバー; ヨハネス クリスチャン プリンスロー ウィリアム; デ ビリエール ピエール |
| 170 | Multistage gas/solid separator | JP33641696 | 1996-12-02 | JPH09201506A | 1997-08-05 | ROBAATO FURANKU TAMERA |
| PROBLEM TO BE SOLVED: To efficiently separate contaminated solid substances from a gas flow by removing a high density phase tangentially from each zone and a low density phase from the second zone. SOLUTION: A gas/solid mixture is introduced tangentially into the first stage of an apparatus 10, and high density substances are moved outside by centrifugal force to advance to a separation zone 21. Besides, low density substances advance to intermediate transfer apparatuses 18, 20. Since the zone 21 of the apparatus has a large diameter, the solid which advanced to the part 21 is reduced of its velocity and removed from a solid outlet 12, and a considerable amount of the solid is removed from a gas flow. Gas containing residual contaminated solid which advances in the apparatus 10 advances in the same direction when it flows in the intermediate transfer pipes 18, 20 and is discharged tangentially from the pipe 20 through a tangential opening 23. Heavy solid substances are moved outside by centrifugal force to advance to a separation zone 27 so that solid can be removed from a solid outlet. Besides, low density gas moves nearly in the middle of the apparatus and flows in a gas outlet conduit tube 26. COPYRIGHT: (C)1997,JPO | ||||||
| 171 | Liquid distributor and solid-liquid separator provided with the same | JP909196 | 1996-01-23 | JPH09192416A | 1997-07-29 | KAWAJIRI HITOSHI; KOJIMA MASAYUKI; YAMAMOTO HIROBUMI |
| PROBLEM TO BE SOLVED: To equalize filtration velocity of a solid-liquid separator as much as possible over the whole filter medium bed area. SOLUTION: Feed water to be treated is caused to flow into a cylindrical vessel 40 from an inflow pipe 42 arranged in the tangential direction thereof near the lower end thereof to generate a turning flow in the cylindrical vessel 40, and the turning flow is caused to flow out from plural discharge pipes 44 installed in the tangential direction of the peripheral surface of the cylindrical vessel 40 at the same height position thereof to constitute a distributor 3. Therefore, liquid flowing into the cylindrical vessel 40 is equally distributed and caused to flow out. The distributors 32 are applied to a solid-liquid separator, allowing the flow velocity distribution of feed water to be treated in the whole floating filter medium bed area to be equalized compared to the conventional distributors. COPYRIGHT: (C)1997,JPO | ||||||
| 172 | Modular steam-water separator | JP50596 | 1996-01-17 | JPH081361U | 1996-09-03 | ジョン・デビッド・イコルス |
| (57)【要約】 【目的】 圧力低下が小さいモジュール型遠心気水分離器を提供する。 【構成】 モジュール型遠心気水分離器は、環状上昇管（36）、上昇管内をそれと同軸に延びるハブ（38）、ハブと上昇管との間に取り付けられた複数の翼（50）、外径が上昇管の内径より小さく、上昇管の出口端部に隣接してそれと同軸に取り付けられたオリフィスリング（4
2）、及び内径が上昇管の外径より大きい、上昇管を囲むようにそれと同軸に取り付けた環状降水管（44）からなる。 翼の前縁（48）及び前端表面（52）は、実質的に上昇管の入口端部に隣接して気体−液体の混合物の流れ方向に平行な平面内に配設されている。 翼の後縁（50） 及び後端表面（54）は、ハブの軸心に垂直な平面に対してほぼ３７°の角度をなす平面内に配設されている。 ハブの軸心に垂直な平面で見た一つの翼の前縁の突出部とそれに隣接する翼の後縁の突出部は約２２．５°の角度をなす |
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| 173 | JPH0549324B2 - | JP6685284 | 1984-04-05 | JPH0549324B2 | 1993-07-26 | SUTEFUANUSU PAARUDEKOOPERU; YOHAN YAN BARENDO PETSUKU |
| 174 | Mechanical dust collector | JP34310891 | 1991-12-25 | JPH05168978A | 1993-07-02 | YOSHIDA NARIOMI; SUMIYOSHI YASUO |
| PURPOSE: To obtain a mechanical dust collector having higher reliability by restraining abnormal differential pressure between a crude gas chamber and a purified gas chamber. CONSTITUTION: In a mechanical dust collector wherein a crude gas chamber 21 is separated from a purified gas chamber 22 and a folded plate 5 having a plurality of gas outlet holes and a cyclone cell wherein a purified gas outlet port is provided in a gas outlet port are provided, there are provided a plurality of open/closure means (cover 4, receiving frame 2, etc.) provided on the plate 5 and a drive means (arm 6, rotation axis 11, etc.) which is linked to the open/ closure means. COPYRIGHT: (C)1993,JPO&Japio | ||||||
| 175 | Chiyubu holding structure of the multi-cyclone | JP10969891 | 1991-11-08 | JPH0539659U | 1993-05-28 | 直人 宇津木 |
| (57)【要約】 【目的】 マルチサイクロンにおける合成樹脂製入口チューブが、鋼板製端板の取付け穴周囲を環状つばと本体とで挟持し圧着した状態で取付けられているものが、気温による寒暖の変化や稼働による振動等で、圧着部に緩みが生じた場合でも、チューブが回動しようとするのを確実に抑止する。 【構成】 端板チューブ取付け穴個々の半径方向外側へ、所定の幅と奥行きを持つ切欠き部を任意箇所設け、
押し型によるチューブの環状つば成形時に、つば裏面の部分が前記切欠き部へ押し込まれて突出し、嵌合する突起片となることを特徴とした構造。 |
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| 176 | JPH0357827B2 - | JP2764584 | 1984-02-16 | JPH0357827B2 | 1991-09-03 | NOMYAMA SATORU; ASAI KAZUAKI |
| 177 | JPH0236623Y2 - | JP9867884 | 1984-06-29 | JPH0236623Y2 | 1990-10-04 | |
| 178 | JPH02501901A - | JP50093288 | 1987-12-22 | JPH02501901A | 1990-06-28 | |
| 179 | JPS6335798Y2 - | JP305585 | 1985-01-14 | JPS6335798Y2 | 1988-09-22 | |
| 180 | JPS6261346B2 - | JP5176979 | 1979-04-26 | JPS6261346B2 | 1987-12-21 | TEJIMA KYOMI; TSUBOI TOSHIO; KAJITANI YUKIMASA |
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