| 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 | PULP DECONTAMINATION APPARATUS AND METHOD OF USE | EP97930035 | 1997-06-18 | EP0910475A4 | 2000-06-28 | LAWSON J ALAN |
| The present invention provides an apparatus and method for decontaminating aqueous paper pulp, the apparatus comprising a decontaminating cell (12). The decontaminating cell (12) has an upper light contaminate collection hood (30) and/or a lower heavy contaminate collection trough (40). Paper pulp is provided to the cell (12) under a pulp head sufficient to purge the contaminates therefrom. | ||||||
| 182 | AUTOMATED, QUANTITATIVE FILTRATION OF LIQUIDS | EP98920237.9 | 1998-05-05 | EP1007849A1 | 2000-06-14 | SCHICK, Karl, G. |
| A system for automated filtration (24) of liquids for quantitative collection of desired filtrates or permeates (33) has a processor-controlled pump unit (25), which controls the rate of flow. The processor-controlled pump operates on data from pressure sensors (35, 36, 40) and a scale (37, 38) to control flow velocity and/or filter back pressure within the pressure. | ||||||
| 183 | Vorrichtung zum Nassklassieren | EP95103504.7 | 1995-03-10 | EP0672455A1 | 1995-09-20 | Bühler, Gerhard, Dipl.-Ing. |
Die Erfindung betrifft eine Vorrichtung zum Naßklassieren eines in einer Flüssigkeit suspendierten Feststoffgemisches in Grobgut und Feingut. Sie enthält einen in einem Gehäuse (2) um eine zentrale Drehachse antreibbaren Klassierrotor (1) mit wenigstens einem darin ausgebildeten Trennkanal (6,7). Damit auch bei höherviskosen Aufgabegutsuspensionen eine optimale Klassierung in Grobgut und Feingut gewährleistet werden kann, erstreckt sich jeder Trennkanal (6,7) etwa spiralförmig von einem exzentrisch angeordneten Aufgabegut-Zuführkanal (8,9) bis zu einer Grobgut-Austragsöffnung (10,11) am Außenumfang des Klassierrotors, wobei ein Fertiggut-Umlenkkanal (12,13) etwa radial vom Trennkanal zu einem zentralen Feingut-Abführkanal (14) verläuft. |
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| 184 | Separator | EP88311819.2 | 1988-12-14 | EP0321204A2 | 1989-06-21 | Lamb, Timothy John |
There is provided a method for separating a first, relatively dense and hard component of a fluid mixture from a second, less dense and relatively soft component of the mixture, the method comprising: Also disclosed is an apparatus for separating a first, relatively dense and hard component of a fluid mixture from a second, less dense and relatively soft component of the mixture. |
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| 185 | 土壌浄化システム及び土壌浄化方法 | JP2017093399 | 2017-04-18 | JP2018176154A | 2018-11-15 | 山▲崎▼ 公信 |
| 【課題】汚染土壌をキレート剤を用いて浄化する土壌浄化施設において、キレート剤の保有量及び使用量を低減するとともに、キレート剤回収のための設備の敷地面積を低減することを可能にする手段を提供する。 【解決手段】土壌浄化システムは、汚染土壌を礫と砂と土とに分級する土壌分級部と、分離された砂及び土をキレート洗浄液で浄化する砂・土浄化部2とを有する。砂・土浄化部2は、砂洗浄部14と、土洗浄部15と、キレート剤再生部16と、砂すすぎ部17と、土すすぎ部18と、キレート剤回収部19とを有する。砂洗浄部14及び土洗浄部15は、それぞれ、砂及び土をキレート洗浄液で洗浄する。キレート剤再生部16は、キレート洗浄液を再生して砂洗浄部14及び土洗浄部15に返送する。キレート剤回収部19は、砂すすぎ部17及び土すすぎ部18から排出された洗浄廃水からキレート剤を回収する。 【選択図】図3 |
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| 186 | Sand washing device | JP2004302386 | 2004-10-18 | JP2006110502A | 2006-04-27 | SAITO YASUHIRO |
| <P>PROBLEM TO BE SOLVED: To provide a space-saving sand washing device which can continuously and efficiently obtain washing effect, is free from the limit of an installation location, and can be easily carried by an operator. <P>SOLUTION: The sand washing device 1 comprises a sand washing pipe 2, a pressurizing means 3 connected to one end of the sand washing pipe 2, and a separating means 4 connected to the other end of the sand washing pipe 2, and is used by pressurizing dirty sand 34 to be washed and a washing liquid 35 to supply them to one end of the sand washing pipe 2. Friction between grains of sand is generate by making the pressurized sand 34 to be washed and washing liquid 35 flow along a pipe body 21 and a screw body 23 fixed on the inside of the pipe body 21 and forming a spiral passage along with it and the inner wall 21c of the pipe body, which washes the grains of sand by rubbing and washing effect. <P>COPYRIGHT: (C)2006,JPO&NCIPI | ||||||
| 187 | Apparatus and method of use remove the pulp contaminants | JP50321598 | 1997-06-18 | JP2000512898A | 2000-10-03 | ローソン、ジェイ．アラン |
| (57)【要約】 本発明は紙パルプ液の汚染物質除去方法および装置を提供し、本装置は汚染物質除去セル（１２）を含む。 汚染物質除去セル（１２）は上部軽汚染物質回収フード（３０）および／または下部重汚染物質回収トラフ（４０）を有している。 紙パルプ液はセル（１２）から汚染物質をパージするのに十分なパルプヘッドでセル（１２）に供給される。 | ||||||
| 188 | Classifier | JP53071096 | 1996-04-10 | JPH11503361A | 1999-03-26 | ガルク ヨアヒム |
| (57)【要約】 本発明は、遠心分級機原理で働く分級機であって、ケーシング（１）と、該ケーシング内に回転可能に配置されたロータ（２）と、該ロータ（２）の外周部及びケーシング（１）によって形成された、固体及び流体供給のための外側の通路（７）とを有しており、前記ロータ（２）が、２つのロータディスク（５，６）とこれらのロータディスク間に配置された羽根（４）とから成っている形式のものに関する。 分級に不都合を影響を与える渦流を減少させるために、本発明によれば、ロータディスクの直径は、ロータディスクの外側の縁部が、固体若しくは流体供給通路内まで延びて、この通路の側制限部を形成するように、選択されるようにすることが、提案されている。 | ||||||
| 189 | Fractionation method and apparatus according to the capillary fluid dynamics | JP50611890 | 1990-03-30 | JP2845620B2 | 1999-01-13 | SHIREBI SHIZAA EE; DOSU RAMOSU HOSE |
| 190 | How to separate the fine solids into two groups of particles and equipment | JP18467494 | 1994-08-05 | JP2752585B2 | 1998-05-18 | YURUGEN SHUTAIN |
| 191 | Desalination process for sand containing salt content | JP2187393 | 1993-01-14 | JPH08196937A | 1996-08-06 | SATO MASAYUKI; TAMARU HIROBUMI; BANDO HIROAKI; YANAKA ATSUSHI |
| PURPOSE: To use sea sand as sand to be mixed into cement or the like by removing simply a salt content contained in the sea sand. CONSTITUTION: Water is put into sand containing a salt content and disposed between electrodes facing each other, and then the salt content in sand is electrolyzed by applying direct current into the above-said electrodes to electrolyze the salt content (NaCl) contained in the sand into Na ions and Cl ions, and the Na ions are sucked to cathodes and Cl ions are sucked to anodes to separate the salt content and remove therefrom. COPYRIGHT: (C)1996,JPO | ||||||
| 192 | Sample feeder for sedimentation classifier | JP16346994 | 1994-07-15 | JPH0824706A | 1996-01-30 | NISHIYAMA YUGO |
| PURPOSE:To provide a sample feeder for a sedimentation classifier by which a sample of a culture cell lump or the like is fed to a classifier continuously, in large quantities and in an aseptive condition. CONSTITUTION:A cylindrical sample feeding part 1 is vertically fitted to the upper surface of a classifying tank 2 of a sedimentation classifier. A sample inflow pipe 5 communicating with a culture tank 3 is connected to the lower part of the sample feeding part 1. An outflow pipe 6 communicating with the culture tank 3 is connected to the top of the sample feeding part 1. A pump 4 for delivering a sample and a valve 7 are arranged in a flow route for the outflow pipe 6 and the culture tank 3. The flow velocity of a liquid contg. the sample in the sample feeding part 1 is set at the one a little larger than the terminal velocity in the fluid of the premature culture cell lump. | ||||||
| 193 | Wet processor | JP29235692 | 1992-10-30 | JPH06151402A | 1994-05-31 | YAMAMOTO MOTOHIKO |
| PURPOSE: To avoid the pollution of semiconductor substrates by impurities such as heavy metal ions by a method wherein a removing part having an impurity adsorbent is provided in either a wet process solution or a path of the same. CONSTITUTION: An etchant 7 overflowed out of the first processing vessel 2 rubs into the second processing vessel 4 wherein the heavy metal ions, etc., contained in the etchant 7 are adsorved by polysilicon coated silicon wafers 5 in this vessel 4 so as to purify the etchant 7. Later, the purified etchant 7 is to be fed back to the etching vessel 1 again through a piping 8 fitted with a filter 10. Through these procedures, the pollution of silicon wafers 5 being wet etching processed can be diminished thereby enabling any defective characteristics due to the pollution to be obviated. COPYRIGHT: (C)1994,JPO&Japio | ||||||
| 194 | JPH05502717A - | JP50611890 | 1990-03-30 | JPH05502717A | 1993-05-13 | |
| 195 | JPH0426905B2 - | JP18011888 | 1988-07-19 | JPH0426905B2 | 1992-05-08 | HONDA MUNETAKA |
| 196 | Continuous sorting-pipe classifier | JP18011888 | 1988-07-19 | JPH0231845A | 1990-02-01 | HONDA MUNETAKA |
| PURPOSE: To continuously and precisely classify fine powder in a wet state with a simple structure and to increase the throughput of the title classifier by classifying the fine powder at the intermediate part of the classifier by the difference between the settling velocity of the particles and the ascending velocity of a liq. CONSTITUTION: A slurry feed pipe 1 and a liq. feed pipe 2 are connected to the main body at the lower part of the classifier, a fine-particle recovery pipe 3 is connected to the outermost cylinder 5 at the uppermost part, and a coarse- particle recovery pipe 4 is connected to an inner cylinder 7 at the lowermost part. The diameter of the outermost cylinder 5 is larger than that at the lower part, the lower part is conically contracted, the intermediate cylinder 6 is set coaxially with the outermost cylinder 5, the diameter of the outermost cylinder 5 is increased from the position of the tip 8, and the lower part of the intermediate cylinder 6 is conically contracted. In addition, the inner cylinder 7 is set coaxially with the outermost cylinder 5 and intermediate cylinder 6, and the lower part is conically contracted. By such a constitution, the particle concn. in the classifying zone can be kept constant, and the classified products with steady classification can be stably obtained. COPYRIGHT: (C)1990,JPO&Japio | ||||||
| 197 | JPS61500278A - | JP50411484 | 1984-10-31 | JPS61500278A | 1986-02-20 | |
| 198 | JPS5822273B2 - | JP12811977 | 1977-10-27 | JPS5822273B2 | 1983-05-07 | HOSHIBA TOSHA |
| 199 | JPS5820659B2 - | JP5262780 | 1980-04-21 | JPS5820659B2 | 1983-04-25 | TAGUCHI KAORU |
| 200 | JPS575581B2 - | JP1451976 | 1976-02-13 | JPS575581B2 | 1982-01-30 | |
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