61 |
控制浮选槽选煤的方法和装置 |
CN88107711 |
1988-11-05 |
CN1014777B |
1991-11-20 |
海沃德·B·奥布拉德; 迈克尔·G·尼尔逊; 托马斯·D·桑德布鲁克 |
用于测定来自煤浮选槽的尾煤的反射率、以便使浮选槽的工作最佳化的方法和装置。光电探测器测定尾煤中的煤含量,并经由工艺过程控制装置监控加到浮选槽的起泡剂和捕收剂。将超声波能量振动周期性地传送到探测器,以便清除在探测器上的沉淀物,使探测器的工作最佳化。 |
62 |
浮选槽选矿的光纤探测装置 |
CN88107712 |
1988-11-05 |
CN1033016A |
1989-05-24 |
海沃德·B·奥布拉德; 迈克尔·G·尼尔逊 |
用于测定来自煤浮选槽的渣滓的反射率、以便使浮选槽工作最佳化的装置。分叉的光缆具有连接到光源和光电导体的终端,光缆的具有扫描器的终端浸没在煤矿浆中。传送到光缆的扫描器端的光被反向散射到起探测器作用的光电导体上,以便测定渣滓中的煤含量,并经由工艺过程控制装置监控加到浮选槽的起泡剂和促集剂。定时将超声波能振动传送到光缆的扫描器端,以便清除扫描器端上的沉淀物,使探测器的工作最佳化。 |
63 |
浮选槽选矿的方法和装置 |
CN88107711 |
1988-11-05 |
CN1032909A |
1989-05-17 |
海沃德·B·奥布拉德; 迈克尔·G·尼尔逊; 托马斯·D·桑德布鲁克 |
用于测定来自煤浮选槽的渣滓的反射率、以便使浮选槽的工作最佳化的方法和装置。光电探测器测定渣滓中的煤含量,并经由工艺过程控制装置监控加到浮选槽的起泡剂和促集剂。将超声波能量振动周期性地传送到探测器,以便清除在探测器上的沉淀物,使探测器的工作最佳化。 |
64 |
Or improvement in this regard in the separation method |
JP2000545981 |
1999-04-28 |
JP2002512886A |
2002-05-08 |
アースラク・ゴーダール; アラン・カスバートソン; ダグフィン・レーヴハウグ; ヘーゲ・フィエールディングスタード; ポール・ロングヴェド; マグネ・ソルバッケン |
Separation of target material from a liquid sample is achieved by coupling the target to targetable encapsulated gas microbubbles, allowing the microbubbles and coupled target to float to the surface of the sample to form a floating microbubble/target layer, and separating this layer from the sample. In a positive separation process the microbubbles are then removed from the target, e.g. by bursting. In a negative separation process target-free sample material is recovered following separation of the floating layer. The method may also be used diagnostically to detect the presence of a disease marker in a sample. Novel separation apparatus is also described. |
65 |
JPS5651094B2 - |
JP14090973 |
1973-12-15 |
JPS5651094B2 |
1981-12-03 |
|
|
66 |
JPS50100177A - |
JP14090973 |
1973-12-15 |
JPS50100177A |
1975-08-08 |
|
|
67 |
浮力を用いて薬剤を単離または濃縮するためのシステムおよび装置 |
JP2016567786 |
2015-05-08 |
JP2017522860A |
2017-08-17 |
シ、グシン; ベンシチモル、マイケル; ワトソン、タイラー |
生物学的薬剤を浮遊る溶液中に注入される生物学的薬剤を単離するためのシステムおよび装置である。これらのシステムおよび装置は、複数の研究、診断、臨床、消費者、および他の用途を有する。開示の一態様は、サンプルおよび複数のマイクロバブルを収容するための内部容積と、テーパ状端部と開放端部とを含むサンプル容器、開放端部に挿入されたプランジャ、およびサンプル容器の水平軸に対して鋭角を形成するテーパ状端部の先端を含む、サンプルから生物学的薬剤を単離または濃縮するための装置を提供し、マイクロバブルは、一つまたはそれ以上サンプルの生物学的薬剤を浮遊させ、プランジャは、サンプルから一つまたはそれ以上の生物学的薬剤を分離または濃縮するために、先端に向かって移動する。【選択図】図4 |
68 |
Processing system and a processing method of the cement kiln combustion gas extraction dust |
JP2006537685 |
2005-09-20 |
JP5180476B2 |
2013-04-10 |
紳一郎 齋藤; 聰一郎 岡村; 剛 松良 |
|
69 |
フライアッシュ中の未燃カーボン除去装置及び除去方法 |
JP2007549076 |
2006-11-28 |
JPWO2007066534A1 |
2009-05-14 |
齋藤 紳一郎; 紳一郎 齋藤; 阿部 一雄; 一雄 阿部; 松尾 和芳; 和芳 松尾 |
【課題】装置コストを低く抑え、フライアッシュの性状に応じて安定した性能調整が可能なフライアッシュ中の未燃カーボン除去方法等を提供する。【解決手段】フライアッシュに水を加えてスラリーとし、捕集剤を添加し、静止型混合器4又はベンチュリー管24等に供給して剪断力を付与し、起泡剤を添加して気泡を発生させ、気泡にフライアッシュの未燃カーボンを付着させて浮上させる。起泡剤、空気をスラリー及び捕集剤とともに静止型混合器等に供給してもよい。フライアッシュの性状の変化に応じて静止型混合器等の直列使用台数を増減し、必要処理能力に応じて静止型混合器等の並列使用台数を増減する。静止型混合器には、複数のガイドべーン4dを備えスラリー等を螺旋流に変換するガイドベーン室4bと、複数のきのこ状の突起4eでスラリー等に剪断力を与えるカレントカッター室4cを備えるものを使用できる。【選択図】図1 |
70 |
湿式排煙脱硫方法と装置 |
JP2017510964 |
2016-04-01 |
JPWO2016163318A1 |
2018-04-26 |
下平 和佳子; 吉川 博文; 片川 篤 |
脱硫吸収塔13内に噴霧する吸収液中に活性炭を添加して排ガスの脱硫と同時に排ガス中の水銀成分を除去し、前記脱硫処理後の吸収液を浮選装置32に送り、泡沫気泡層36を形成させ、該気泡層36の物性値が所定の範囲となるように、吸収液中の塩素イオン濃度が所定値を上回らない範囲で排水量を減少させ、同時にCaイオン及び/又はMgイオン、さらには起泡剤を吸収液に添加することで、浮選装置32における活性炭の分離回収率を高め、脱硫吸収塔13での水銀再放出と回収石膏への水銀移行を安定的に抑制する。 |
71 |
セメントキルン燃焼ガス抽気ダストの処理システム及び処理方法 |
JP2006537685 |
2005-09-20 |
JPWO2006035631A1 |
2008-05-15 |
齋藤 紳一郎; 紳一郎 齋藤; 岡村 聰一郎; 聰一郎 岡村; 剛 松良 |
【課題】設備コスト及び運転コストを低く押さえながら、セメントキルン燃焼ガス抽気ダストから鉛を効率よく除去する。【解決手段】セメントキルン2のキルン尻から最下段のサイクロンに至るまでのキルン排ガス流路より燃焼ガスの一部を冷却しながら抽気するプローブ3と、プローブ3で抽気した燃焼ガスに含まれるダストの粗粉を分離する分級機5と、分級機5から排出された微粉を含む抽気ガスを集塵する湿式集塵機6と、湿式集塵機6に、キルン排ガスに含まれる鉛の硫化を行うための硫化剤を供給する装置12、13とを備えるセメントキルン抽気ガス処理システム1等。硫化剤供給装置12、13から硫化剤を循環液槽7又はスラリー循環用のポンプ9に添加することが好ましい。湿式集塵機6によって得られたスラリーを、鉛を含むフロスと、石膏を含むテール側スラリーとに浮選設備14、17、18によって分離する。【選択図】図1 |
72 |
Method and apparatus for preparing and defoaming coating liquid |
JP2000265614 |
2000-09-01 |
JP2002066431A |
2002-03-05 |
TAKAHASHI YASUO |
PROBLEM TO BE SOLVED: To certainly remove air bubbles in a coating liquid regardless of the properties of the coating liquid and to treat a large amount of the coating liquid without exerting adverse effects on the quality of the coating liquid after defoaming. SOLUTION: At first, the whole amount of air bubbles in the coating liquid is reduced by the vacuum degassing performed in the stirring tank 14A of a primary process while the coating liquid is prepared and, next, air bubbles having a relatively large diameter among air bubbles not defoamed in the primary process are defoamed in a tank-shaped defoaming apparatus in the floating tank 16A of a secondary process and, finally, air bubbles having a fine-small diameter, hardly removed in the primary and secondary processes, are dissolved in the liquid under pressure in the pipeline 18B of a tertiary process to be defoamed. |
73 |
Purification method of fiber suspension |
JP51155298 |
1997-08-25 |
JP2000517007A |
2000-12-19 |
エーリツクソン,トーマス; ビツクストレーム,トーマス; フレドリツクソン,ベリエ |
PCT No. PCT/SE97/01401 Sec. 371 Date May 6, 1999 Sec. 102(e) Date May 6, 1999 PCT Filed Aug. 25, 1997 PCT Pub. No. WO98/08610 PCT Pub. Date Mar. 5, 1998A process for the purification of a fiber suspension (deinking or white water) in which a mixture of fiber suspension and gas bubbles are jtted into a flotation tank in an upwardly directed manner toward the free surface of the pulp at a velocity of greater than Sm/s and the jet ends at or just below the free surface of the mixture. |
74 |
Injector for flotation device |
JP9456594 |
1994-05-06 |
JPH073686A |
1995-01-06 |
ARUBUREHITO MAINETSUKE; MIHIYAERU TEREFUTSU; HERUMUUTO HAINTSUMAN |
PURPOSE: To mix effectively a fibrous floating matter with air bubbles by introducing air and the fibrous floating matter into a flow channel wherein a cross sectional area repeats narrowing and widening in the direction from a suction end toward a discharge end.
CONSTITUTION: In the injector in a flotation device, two flowing flat plates 3, 4 which have convex parts 8, 9 comprising a bar inclined at an angle (b) of 10-90° toward the direction of flow from a side wall 15 between a suction end E and a waste end A, are arranged oppositely each other. The inclined angle of the convex parts 8, 9 is gradually increased from the suction end E toward the discharge end A in a range of 20-90° to change the cross section toward the flow direction, and at the same time circular cylinders 21, 22 as air supplying paths are arranged at back side of an isolating wall 20 in a supplying path 23 of the fibrous floating matter to construct an injector. The fibrous matter is introduced with air into the mixing paths wherein the cross sectional area repeats narrowing and widening to the direction of the injector, and mixed effectively with generated bubbles.
COPYRIGHT: (C)1995,JPO |
75 |
Gas treating device |
JP3415482 |
1982-03-05 |
JPS57184423A |
1982-11-13 |
HANSU RIYUTOKE; ARUBERUTO BAARU; FURIIDORITSUHI BUIRUHERUMU MEE; KARURU REGUNAA |
Air or another gas is introduced into a liquid or slurry stream flowing in a duct 1, 3 by means of a row of bubble generators 10 made of resilient and porous plastics material, e.g. high-density polyethylene. As shown, each generator 10 is a resilient hose extending transversely of duct 1, 3 and fed by the gas from inlet 6. <IMAGE> |
76 |
High-energy efficiency phase transfer/dispersion device and its use |
JP6083282 |
1982-04-12 |
JPS57180488A |
1982-11-06 |
EBAN II KOSUROO |
|
77 |
IMPROVEMENTS IN OR RELATING TO SEPARATION PROCESSES |
PCT/GB9901317 |
1999-04-28 |
WO9955837A3 |
2000-02-10 |
CUTHBERTSON ALAN; RONGVED PAAL; LOEVHAUG DAGFINN; FJERDINGSTAD HEGE; SOLBAKKEN MAGNE; GODAL ASLAK |
Separation of target material from a liquid sample is achieved by coupling the target to targetable encapsulated gas microbubbles, allowing the microbubbles and coupled target to float to the surface of the sample to form a floating microbubble/target layer, and separating this layer from the sample. In a positive separation process the microbubbles are then removed from the target, e.g. by bursting. In a negative separation process target-free sample material is recovered following separation of the floating layer. The method may also be used diagnostically to detect the presence of a disease marker in a sample. Novel separation apparatus is also described. |
78 |
METHODS AND APPARATUS FOR INCREASING AND EXTENDING OIL PRODUCTION FROM UNDERGROUND FORMATIONS NEARLY DEPLETED OF NATURAL GAS DRIVE |
PCT/US0339533 |
2003-12-11 |
WO2004053330A3 |
2004-08-12 |
ARNAUD JOHNNY; BEARD FRANKLIN B |
Methods and apparatus employing inert gases injected into the lower level of sloping underground oil-bearing formations as a driving mechanism and water injected into the upper level of the formation as a gas blocking mechanism for increasing and extending the production of oil from underground formations is described. Also described is an inert gas and oil production system comprising an exhaust gas processing system, a well inert gas and water injection system, an oil production well system comprising an exhaust gas scrubbing or cleaning system (1) and a gas separation system (100), a well inert gas and water injection system, an oil production system, and a fuel gas generator (700). A hydraulically operated crude pump is also described. |
79 |
건설폐기물 내 부유물의 다단 선별 및 순환골재 회수 시스템 |
KR1020170067419 |
2017-05-31 |
KR101823975B1 |
2018-01-31 |
민원; 박인규 |
본발명은건설폐기물내 부유물의다단선별및 순환골재회수시스템에관한것으로특히, 1차조크러셔에서파쇄된건설폐기물인폐콘크리트가투입되면이를세척해줌과동시에물보다부력이작은폐콘크리트는수조바닥으로가라앉히고물보다부력이커 수면위로부상되는각종이물질은상기스크레이퍼를통해진동스크린측으로배출시켜주는부유선별장치와; 입자가큰 이물질거름용 1단스크린과, 폐콘크리트잔입자거름용 2단스크린, 상하부로일정간격을두고설치되는상,하부타공판으로이루어진슬러지거름용 3단스크린이본체내 상,하부사이에정해진간격을두고일측에서타측으로경사진형태를갖도록다층으로설치되고, 저면이일측으로경사지게형성된본체의일측면저부와상기부유선별장치의타측면저부사이에는플렉시블한물 리턴파이프가설치된구성을갖고상기부유선별장치에서선별하여투입시킨부유이물질을각각입자가큰 이물질과폐콘크리트잔입자, 슬러지및 물로분리선별해주는진동스크린과; 입자가큰 이물질을포집해주는부유이물질포집구와; 폐콘크리트잔입자를 2차더블조크러셔측으로이송시켜주는벨트컨베이어;를포함하는것을특징으로한다. 따라서, 건설폐기물로부터의순환골재생산량을대폭증대시킬수 있음은물론부유이물질의선별효율성을대폭향상시킬수 있다. |
80 |
탈황 슬래그의 분리장치 및 분리방법 |
KR1020110063201 |
2011-06-28 |
KR1020130002142A |
2013-01-07 |
권혁기; 이윤모; 박동철 |
PURPOSE: A desulfurized slag separation device and a method thereof are provided to collect Kish carbon and iron components from desulfurized slag for recycling, and to prevent environmental contamination caused by desulfurized slag. CONSTITUTION: A desulfurized slag separation device and a method thereof comprise a water treatment tank(110), an injection device (120), a floating material discharger(130), a precipitate discharger(140). The water treatment tank accommodates a fluid. The injection device injects desulfurized slag powder into the water treatment tank. The floating material discharger is installed inside the water treatment tank with a reciprocating motion to collect and discharge the floating materials on the water surface outwards. The precipitate discharger is installed on the bottom surface of the water treatment tank with an inclination to the upper side to discharge precipitated materials on the bottom surface of the water treatment tank outwards. The water treatment tank additionally includes separation membranes installed to divide the surface of a fluid into both sides. The injection device which injects the slag powder into one side of a separation membrane is arranged on the side of the separation membrane. |