序号 | 专利名 | 申请号 | 申请日 | 公开(公告)号 | 公开(公告)日 | 发明人 |
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101 | SYSTEM FOR PROCESSING A MIXTURE OF SUPERFINE MATERIALS | PCT/EP9901639 | 1999-03-12 | WO9947280A2 | 1999-09-23 | KUPCZIK GUENTER |
The invention relates to a system for processing a mixture of superfine materials containing mineral, organic and aqueous components. Said system comprises a revolving plate having a substantially vertical axis of rotation, a drive motor which drives the revolving plate, a feed device for the superfine material mixture which is directed towards the centre of the revolving plate, and a storage reservoir which is connected to the feed device and fitted with a supply device for the superfine material mixture so as to compensate for variations in said mixture. The system further comprises a collecting device having a floor for supporting a sediment formed by superfine particles spun off by the revolving plate and having a funnel-like upper surface, as well as a vent in the centre of the floor at the lower end of the funnel surface. | ||||||
102 | NUCLEIC ACID SEPARATION | PCT/US2018/024672 | 2018-03-27 | WO2019190490A1 | 2019-10-03 | SHKOLNIKOV, Viktor; GOVYADINOV, Alexander |
An example system includes an input channel to flow nucleic segments therethrough, a mixing portion coupled to the input channel, a separation chamber in fluid communication with the second end of the input channel, at least two output channels coupled to the chamber, and an integrated pump to facilitate flow through the separation chamber. The mixing portion is to include at least two different categories of beads having different sizes from each other and having a probe to attach to a corresponding nucleic acid segment. The separation chamber has a passive separation structure including an array of columns spaced apart to facilitate separation of the different categories of beads and attached corresponding nucleic acid segment into at least two flow paths based on a size of the category of the beads. Each output channel is to receive separated categories of beads and attached nucleic acid segments. |
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103 | CUSTOMIZABLE MICROFLUIDIC DEVICE WITH PROGRAMMABLEMICROFLUIDIC NODES | PCT/IB2018/054542 | 2018-06-20 | WO2018235014A1 | 2018-12-27 | DELAMARCHE, Emmanuel; GOEKCE, Onur |
The invention is directed to a microfluidic device. The device includes an input microchannel, a set of m distribution microchannels, a set of m microfluidic modules and a set of m nodes. The m microfluidic modules (m ≥ 2) are in fluidic communication with the m distribution microchannels, respectively. The one or more nodes of the set of m nodes branch from the input microchannel, and further branch to a respective one of the set of m distribution microchannels. In addition, a subset, but not all, of the nodes are altered. The nodes of the set of m nodes have different liquid pinning strengths. As a result, the extent in which a liquid passes through one or more of the m microfluidic modules varies based on the different liquid pinning strengths, in operation. Additional sets of nodes may be provided to allow liquid to pass through ordered pairs of modules. |
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104 | PROCESS TO CONCENTRATE MANGANESE ORES VIA REVERSE CATIONIC FLOTATION OF SILICATES | PCT/BR2014/000028 | 2014-02-03 | WO2014121358A1 | 2014-08-14 | LEAL FILHO, Laurindo de Salles; SOUZA, Helder Silva; BRAGA, André Soares |
The present invention relates to a process for concentrating manganese from the tailing of a manganese-carrying mineral characterized by comprising the stages of removing coarse particle size fraction from the tailing, desliming and conducting an acid or a basic reverse cationic flotation. The manganese-carrying minerals of the present invention are usually minerals with low manganese content being preferred derived from the lithologies "Tabular Pelite" (or PETB), Pelite Siltite (or PEST), Detritic (or DETR), Rich Pelite (or PERC) and Metallurgical Bioxide (or BXME). The present invention also relates to a reverse cationic flotation used to concentrate manganese which is carried out using depressors agents and collectors agents as flotation reagents. |
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105 | DISSIMILAR MATERIALS SORTING PROCESS, SYSTEM AND APPARATUS | PCT/US2006/041753 | 2006-10-24 | WO2007136403A2 | 2007-11-29 | VALERIO, Thomas, A. |
An automated system for sorting dissimilar materials, and in particular for sorting plastics from other materials and for sorting different types of plastics from one another comprises, depending upon the embodiment, combinations of a sizing mechanism, a friction separation, an air separator, a magnetic separator, a dielectric sensor sortation bed, shaker screening, a ballistic separator, an inductive sensor sortation system and a float/sink tank. The dielectric sensor sortation system may be either analog or digital, depending upon the particular implementation. One or more float/sink tanks can be used, depending upon the embodiment, each with a media of a different specific gravity. The media may be water, or water plus a compound such as calcium chloride. In addition, multiples of the same general type of module can be used for particular configurations. A heavy media system or a sand float process can be used either alternatively or additionally. |
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106 | SEPARATING SMALL RUBBISH AND ORGANIC MATTERS FROM GARBAGE | PCT/IB2004/001451 | 2004-05-07 | WO2004101098A3 | 2004-11-25 | TSE, Steven |
An apparatus and method for separating small rubbish and organic matters from garbage for collection by means of water by considering specific weight, buoyancy, and flow rate of water is disclosed. The apparatus comprises a plurality of conveyor screens (21, 24) incorporating injection nozzles (210, 240), a less inclined channel (32), a conveyor and an organic matter screen (34) for effectively separating floated rubbish, organic matters, and sunk rubbish from garbage for collection. |
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107 | APPARATUS AND METHOD OF SEPARATING SMALL RUBBISH AND ORGANIC MATTERS FROM GARBAGE FOR COLLECTION | PCT/IB2004001451 | 2004-05-07 | WO2004101098A2 | 2004-11-25 | TSE STEVEN |
An apparatus and method of separating small rubbish and organic matters from garbage for collection by means of water by considering specific weight, buoyancy, and flow rate of water is disclosed. The apparatus comprises a plurality of conveyor screens incorporating injection nozzles, a less inclined channel, a conveyor, and an organic matter screen for effectively separating floated rubbish, organic matters, and sunk rubbish from garbage for collection. | ||||||
108 | A method and apparatus for separating particles | JP2006507854 | 2004-03-16 | JP2006520688A | 2006-09-14 | コーイ、ローレンス アントン ヴァン; レム、ピーター、カルロ |
本発明は流体内で重力を使用して粒子流から粒子部分を分離する方法に関する。 この方法で各回収手段に回収された粒子部分が供給される。 発明によると流体および回収手段は互いに移動の相対方向を規定して移動する。 流体に対して分離される粒子の移動を移動の相対方向に制限するための手段が設けられる。 また発明は方法を実施する装置に関する。 | ||||||
109 | Method for producing cultivation soil | JP2002174018 | 2002-06-14 | JP2004016066A | 2004-01-22 | SUEMATSU SHINPEI; UMEDA AKIRA; YAMAMOTO KENGO; YANAGIDA TOMOTAKA; HIGA ISAO |
<P>PROBLEM TO BE SOLVED: To provide a method for producing cultivation soil, by which sodium salts, chlorides and sulfides contained in various soils and inhibiting the growth of plants can forcibly be removed to obtain the soil optimal as a cultivation soil, thereby effectively using the soil. <P>SOLUTION: This method for producing the cultivation soil is characterized by comprising the first process for removing foreign matters such as impurities, stones and sand from soil containing sodium salts and chlorides to obtain the fine particulate soil, the second process for diluting the obtained fine particulate soil with water to prepare the mud, and then mechanically dehydrating the mud to obtain the first dehydrated cake, the third process for crushing the first dehydrated cake, diluting the crushed product with water to prepare the mud, and then subjecting the mud to a chemical treatment for dissolving the exchangeable sodium salts and sulfides contained in the mud in water, the fourth process for mechanically dehydrating the chemically treated mud to obtain the second dehydrated cake, and the fifth process for, if necessary, crushing the second dehydrated cake to obtain the cultivation soil. <P>COPYRIGHT: (C)2004,JPO | ||||||
110 | Gravel sorter | JP14506096 | 1996-05-14 | JP2911818B2 | 1999-06-23 | MORI TERUO |
111 | Gravity separation apparatus and method of the solid particles | JP51021796 | 1995-09-13 | JPH10505782A | 1998-06-09 | シー ヤング ディビット |
(57)【要約】 充填材を含有する充填柱状体を含み、充填柱状体およびその内部の粒子を振動させる手段を有する重力分離装置および方法を提供する。 重力分離装置は、密度の異なる固体粒子を効率的かつ効果的に分離するものである。 重力分離方法では、好ましくは、鉱物鉱石の水性鉱泥を分散剤で調製して、分散水性鉱泥を入口部から充填柱状体の中間部へと供給して、柱状体の下部に高密度粒子の高密度層床を形成するとともに、柱状体の上部に低密度粒子の低密度層床を形成する。 尾鉱を柱状体の上端から取り出し、脈石レベルが低減された精鉱鉱物鉱石を柱状体の底部から取り出す。 本装置および方法は、粒子サイズが小さい鉄鉱石粒子から粒子サイズが小さい二酸化珪素粒子を分離するのに特に有用である。 | ||||||
112 | Method and device to separate fine-grained solid material into two fractions | JP18467494 | 1994-08-05 | JPH07155638A | 1995-06-20 | YURUGEN SHIYUTAIN |
PURPOSE: To enable sharp separation in a specific separation threshold grain size range with a cost effective system by dispersing fine-grained solids in liquid, thereby forcibly forming a sink flow and sink flow superimposed with a rotational flow produced gregardless of the sink flow. CONSTITUTION: A deflector wheel 3 having a perpendicular axis is driven via a belt wheel 12 and a hollow shaft 9 and a bearing is sealed to a bearing casing 1 by a shaft packing 6. The particulates to be classified which are dispersed in liquid pass a conduit juncture 2 and are introduced by a pumping effect into a casing 1 and arrive at the deflector wheel 3. The particulates separated by the separation effect of the deflector wheel 3 passes the inside of the hollow haft 9 as a particulate dispersion together with part of the liquid and are discharged into a fine fraction collecting chamber 10. These particulates are made to flow out of the conduit juncture 4 for the purpose of reuse. The coarse fractions rejected by the deflector wheel 3 are discharged together with the remaining liquid through an opening 11 at the center of the bottom of the casing 1 into a coarse fraction collecting chamber 13 and are discharged as the coarse fraction dispersion from the conduit juncture 5. | ||||||
113 | Separation method and apparatus of particulate material in a liquid medium | JP50411484 | 1984-10-31 | JPH0679682B2 | 1994-10-12 | SHURAMU KOONERIUSU JOON |
114 | JPS6343133B2 - | JP2359786 | 1986-02-04 | JPS6343133B2 | 1988-08-29 | NIWANO KAZUHISA; MINATO TETSUNORI; HIRATSU YUTAKA; HAMASE TAKAHIKO |
115 | JPS62130745U - | JP1624286 | 1986-02-06 | JPS62130745U | 1987-08-18 | |
116 | JPS5826979B2 - | JP803279 | 1979-01-25 | JPS5826979B2 | 1983-06-06 | NAKAJIMA YUKIO |
117 | JPS5751650U - | JP12967880 | 1980-09-10 | JPS5751650U | 1982-03-25 | |
118 | Method and device for classification of powder | JP6223280 | 1980-05-13 | JPS56158162A | 1981-12-05 | SHINHOU AKIRA; YAMAZAKI TAMOTSU |
PURPOSE: To classify a small amount of finely divided powder efficiently and accurately by sinking the suction ports of a drawing-out pipe in the shallow position below liquid surface, transferring liquid and powder into a take-out tank and stopping the drawing-out when the liquid surface or the suction port attains a fixed height. CONSTITUTION: Powder and a medium for gravity classification are put into a settling tank 11, and after stirring, the powder is allowed to settle. Thence, the suction ports 13 of a drawing-out pipe 12 are sunk in the shallow position below a liquid surface 10a, and the liquid and powder are transferred into a take-out tank 24. During this time, the suction ports 13 are lowered along with lowering of the liquid surface, and when the liquid surface 10a or the suction ports 13 attains a fixed height, the drawing-out is stopped. When the ports 13 are disposed upward and horizontally dispersedly, good results are obtained, and the distance between the ports 13 and the liquid surface 10a is maintained always short and constant, and therefore if the ports 13 are lowered at the velocity at which the amount of the water above the ports 13 and the rate of suction balance, the powder and liquid gather at the ports 13 all along the liquid surface at high velocity of flow. COPYRIGHT: (C)1981,JPO&Japio | ||||||
119 | JPS5633143B2 - | JP11554678 | 1978-09-19 | JPS5633143B2 | 1981-08-01 | |
120 | JPS5624526Y2 - | JP7973276 | 1976-06-16 | JPS5624526Y2 | 1981-06-09 | |