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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81 | Separation of ash from regenerated adsorbent | JP2183388 | 1988-02-01 | JPS63194702A | 1988-08-11 | MAAKU SHII HOFUMAN; MAABUIN JIEI DEIITORITSUHI; TOOMASU PII OOTEINGAA |
82 | Sorting of alumina particle | JP8591787 | 1987-04-09 | JPS62244458A | 1987-10-24 | JIEIMUZU KURARENSU ROMAIN |
83 | Separation of sperm | JP8043485 | 1985-04-17 | JPS6122851A | 1986-01-31 | UOORESU SHIYURINPUTON |
A process for the separation of X sperm and Y sperm by phenotypic differences in a gravity separation process wherein an osmolality gradient is provided within the separation vessel, the osmolality preferably being in inverse relationship to the density gradient. | ||||||
84 | Method for deashing coal | JP16283980 | 1980-11-18 | JPS5785891A | 1982-05-28 | AKIMOTO HIDETOSHI; KAJI RIYUUICHI; KOMURO TAKEO; MURANAKA TADASHI; KIKUCHI HIDEO; HISHINUMA TAKAO; NAKASHIMA FUMITO; TERADA HIROSHI |
PURPOSE: To carry out effectively the deashing of coal, by a method wherein oil droplets are introduced into a slurry of pulverized coal in water to deposit coal onto the ascending oil droplets, whereby coal is entrained in the oil and come up to the surface, the coal component is concentrated in an oil phase and separated, and ash is concentrated in water. CONSTITUTION: Coal A is pulverized in a pulverizer 2. Water is added to the pulverized coal in a mixer 3 to produce a slurry which is then supplied to a separating tower 5. Oil from an oil tank 10 is supplied to the bottom of the separating tower 5 to deposit lipophilic coal onto the ascending oil droplets, whereby coal is entrained in the oil and come up to the surface. Then a coal-oil mixture floating on the upper part of the separating tower 5 is introduced through a rinser 6 into a filter 7 where the mixture is separated into coal and oil to obtain coal C contg. less ash. The separated oil is introduced into a tank 9 where water entrained therein is separated. Then the oil is recycled for use. The separated water together with water contg. concentated ash from the separating tower 5 is introduced into a thickener 4 where ash B is separated, and then recycled for use. COPYRIGHT: (C)1982,JPO&Japio | ||||||
85 | Method of collecting coal from end of mine | JP9622177 | 1977-08-12 | JPS5323803A | 1978-03-04 | TOOMASU ARUFURETSUDO BIBIAN; JIEEMUSU DENISU DEMURAA |
86 | Kongobutsuno shoriho | JP9131974 | 1974-08-09 | JPS5120158A | 1976-02-18 | SAITO KOZO; IZUMI SUMIO |
87 | HIGH-THROUGHPUT METHODS AND SYSTEMS FOR PROCESSING BIOLOGICAL MATERIALS | EP10798290.2 | 2010-12-15 | EP2512676B1 | 2018-09-05 | GRIFFIN, Weston, Blaine; ROY, Jaydeep; SHOEMAKER, Philip, Alexander; WATERS, William, Patrick |
A high-throughput system for processing biological material that comprises: a tray that supports a functionally-closed fluid path subsystem comprising, a vessel for containing and enabling the biological material to separate into two or more distinct submaterials; one or more receptacles to receive one or more of the submaterials from the vessel; a filtration device; a conduit through which one or more submaterials are transported between at least the vessel and the filtration device; and a first engagement structure; a processing unit comprising, a pumping device for moving one or more of the submaterials between at least the vessel and the filtration device via the conduit; a second engagement structure corresponding to the first engagement structure; a locking mechanism for at least temporarily holding the tray in a fixed position relative to the processing unit; a control device that automatically starts and stops the pumping device in response to one or more commands. | ||||||
88 | METHOD OF SEPARATING BEADS IN A FLUIDIC CHIP | EP15735866.4 | 2015-06-19 | EP3158334A1 | 2017-04-26 | BORCH, Stig Morten; HAMSUND, Torgeir; HOLTLUND, Jostein Geir; GULLIKSEN, Anja |
The present invention provides a method of analyzing a sample containing an analyte to be qualitatively and/or quantitatively determined, comprising a binding step and a washing step, wherein the binding step comprises: interacting the analyte with beads having a density m1; obtaining a structure of packed beads comprising quantifiable bead complexes having a density m2; and the washing step comprises: dispersing the packed beads in a liquid medium having a density d>m2 and m1; and separating the liquid medium and the beads comprising the quantifiable bead complexes. | ||||||
89 | ANALYTICAL METHOD | EP15730158.1 | 2015-06-19 | EP3158332A1 | 2017-04-26 | BORCH, Stig Morten; HAMSUND, Torgeir; HOLTLUND, Jostein Geir; GULLIKSEN, Anja |
The present invention provides a method of analyzing a sample containing an analyte to be qualitatively and/or quantitatively determined, comprising a binding step and a washing step, wherein the binding step comprises: interacting the analyte with beads having a density m1; obtaining a structure of packed beads comprising quantifiable bead complexes having a density m2; and the washing step comprises: dispersing the packed beads in a liquid medium having a density d>m2 and m1; and separating the liquid medium and the beads comprising the quantifiable bead complexes. | ||||||
90 | DISSIMILAR MATERIALS SORTING PROCESS, SYSTEM AND APPARATUS | EP06836531 | 2006-10-24 | EP1960111A4 | 2013-11-20 | VALERIO THOMAS |
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. | ||||||
91 | HIGH-THROUGHPUT METHODS AND SYSTEMS FOR PROCESSING BIOLOGICAL MATERIALS | EP10798290.2 | 2010-12-15 | EP2512676A1 | 2012-10-24 | GRIFFIN, Weston, Blaine; ROY, Jaydeep; SHOEMAKER, Philip, Alexander; WATERS, William, Patrick |
A high-throughput system for processing biological material that comprises: a tray that supports a functionally-closed fluid path subsystem comprising, a vessel for containing and enabling the biological material to separate into two or more distinct submaterials; one or more receptacles to receive one or more of the submaterials from the vessel; a filtration device; a conduit through which one or more submaterials are transported between at least the vessel and the filtration device; and a first engagement structure; a processing unit comprising, a pumping device for moving one or more of the submaterials between at least the vessel and the filtration device via the conduit; a second engagement structure corresponding to the first engagement structure; a locking mechanism for at least temporarily holding the tray in a fixed position relative to the processing unit; a control device that automatically starts and stops the pumping device in response to one or more commands. | ||||||
92 | DISSIMILAR MATERIALS SORTING PROCESS, SYSTEM AND APPARATUS | EP06836531.1 | 2006-10-24 | EP1960111A2 | 2008-08-27 | Valerio, Thomas |
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. | ||||||
93 | DEVICES, MATERIALS AND METHODS FOR SORTING, SEPARATING AND SIZING VERY SMALL PARTICLES | EP04796494.5 | 2004-10-27 | EP1735066A2 | 2006-12-27 | KALECHOFSKY, Neal, Oxford Instruments America, Inc |
Advice for sorting separating and sizing very small particles is disclosed and claimed. The device comprises a cryogenic chamber within which particle movement, travel and separation can occur; a particle loading chamber for loading particles into the cryogenic chamber; and a particle collector. Also disclosed and claimed is helium, and more specifically helium in its superfluid state, for separating the particles. | ||||||
94 | TANGENTIALE FESTSTOFFABTRENNUNGS-VORRICHTUNG | EP99973628.3 | 1999-08-25 | EP1148951B1 | 2003-02-12 | NIEMCZYK, Bernhard; HEINZ, Robert; MENKE, Lucas; TROUBOUNIS, George |
The invention relates to a device and a method for chemically and physically separating solid materials from a suspension using flotation. A rotationally symmetrical flocculation/flow reactor (20) is provided with outlets in the lower part thereof and is arranged in a separating tank (12). At least one suspension inlet (24) extends eccentrically into said reactor. The supplied suspension is guided into the upper area of the flocculation reactor (20) via the suspension inlet (24). A circular flow is thus created which drains off from the flocculation reactor (20) downwards in a tangential and radial manner over the outer circumference into circularly arranged distribution cells (44) which reinforce the tangential component of the suspension flow when said flow is delivered into the separating tank (12). In prior art, the flow of the mixture consisting of the suspension and air-sacs extends radially outwards. One advantage of the invention is that said flow of the mixture has to travel a longer way to the outlets in the area of the wall of the tank due to the tangential flow component. The solid matter can be separated more effectively by virtue of the longer travel path or the longer presence in the separating tank. | ||||||
95 | Verfahren zur Trennung von Gemischen aus Partikeln und/oder Flüssigkeitströpfchen und einem flüssigen oder gasförmigen Trägermedium mittels der unterschiedlichen Kompressibilität der einzelnen Stoffe | EP95109784.9 | 1995-06-23 | EP0694327A2 | 1996-01-31 | Lezius, F., Dipl-Ing. |
Tröpfchen- und/oder Partikelgemische in Suspensionen. Emulsionen, Aerosolen oder Schwebstäuben werden zur differenzierten Trennung einem unter Über- oder Unterdruck stehenden Apparat zugeführt. Durch den Druck werden die Gemischbestandteile komprimiert bzw. expandiert, wodurch auch Bestandteile absinken bzw. aufsteigen, die bei Normalbedingungen nicht sedimentieren würden. Durch die unterschiedliche Kompressibilität der Gemischbestandteile entstehen Dichteunterschiede, welche die Sinkgeschwindigkeiten derart beeinflussen, daß eine sedimentative Abtrennung einzelner Gemischfraktionen ermöglicht wird. Zur Durchführung wird ein flüssige oder gasförmige Trägermedium (T) über einen Diffusor einem erfindugsgemäßen Apparat zugeführt. Die Gemischbestandteile, die entweder schon vor dem Apparat mit dem Trägermedium vereinigt sind oder separat zugeführt werden, erhalten in Abhängigkeit ihrer Kompressibilität, Masse und Dichte, des Druckes im Apparat und der Viskosität und Strömung des Trägermediums eine charakteristische Sink- oder Auftriebsbeweging, woduch die einzelnen Fraktionen in bestimmten Bereichen sedimentieren und dort gesammelt werden. Die sedimentierten Fraktionen werden über Anschlußflansche abgezogen und durch weitere Trennvorrichtungen von dem Trägermedium separiert. |
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96 | Verfahren und Vorrichtung zur Verwertung von Frischbetonresten und dgl. Verbundbaustoffen | EP93103372.4 | 1993-03-03 | EP0561217A3 | 1995-02-15 | Walke, Harald; Walke, Christian |
Bei einem Verfahren zur Verwertung von Frischbetonresten und dgl. Verbundbaustoffen wird der aus Betonmischern, Betonfahrmischern und dgl. Baumaschinen entfernte, insbesondere als ein Frischbeton-Spülwasser-Gemisch anfallendeFrischbetonrest in einer einen behälterförmigen Behandlungsaufbau aufweisenden Vorrichtung einem Entsorgungsschritt unterzogen. Das Frischbeton-Spülwasser-Gemisch wird in dem Behandlungsaufbau gesammelt, in diesem einer zumindest periodischen, eine Abbindung der Gemischbestandteile verhindernden Mischbewegung ausgesetzt, das Gemisch nach einer vorbestimmten Verweildauer in eine die Gemischbestandteile durch ein Sedimentationsgleichgewicht trennende Ruhestellung verbracht, ein nach einer Absetzzeit geklärter Spülwasseranteil aus dem Behandlungsaufbau abgeleitet und danach ein verbleibendes Frischbeton-Restgemisch einer Weiterverarbeitung zugeführt. |
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97 | Separation of materials from a liquid dispersion by sedimentation | EP86105116.7 | 1986-04-14 | EP0198462B1 | 1993-01-27 | Alspector, Benjamin |
98 | Procédé de restructuration d'un ensemble de particules fines | EP90400966.9 | 1990-04-10 | EP0394091A1 | 1990-10-24 | Karinthi, Pierre |
Procédé de restructuration d'un ensemble de particules fines, de granulométries inférieures à 100 microns, caractérisé en ce qu'on place lesdites particules à restructurer dans un bain de liquide cryogénique inerte à l'égard desdites particules, on assure l'opération de restructuration proprement dite, après quoi on procède au retrait du liquide cryogénique par exemple par évaporation. Applications à la réalisation d'alliages métalliques, de polymères spéciaux, de peintures, d'encres, de noir de carbone, de céramiques spéciales et de produits pharmeceutiques ou alimentaires. |
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99 | Verfahren und Vorrichtung zum Trennen von Feststoff-Feinpulvern in Korngrössenfraktionen | EP87106418.4 | 1987-05-04 | EP0245744A3 | 1989-07-05 | Volz, Otto; Mechau, Enrique; Lohfink, Werner |
Zum Trennen von Feststoff-Feinpulvern in Korngrößenfraktionen wird das Feinpulver in einer Flüssigkeit suspendiert. Die Suspension wird in einem säulenförmigen Suspensionsbehälter(1) sedimentieren gelassen. Der Suspensionsbehälter (1) hat in der Höhe gestaffelt von Schiebern (5,7) verschließbare Entnahmeöffnungen (4,6) für die jeweilige Suspensionsfraktion. Abhängig von der Art des zu klassierenden Feinpulvers wird nach einer jeweils vorher festgelegten Sedimentationszeit zunächst an der höchsten Entnahmeöffnung (4) eine Suspensionsfraktion entnommen, aus der dann das darin enthaltene Feinpulver gewonnen wird, dessen mittlere Korngröße erheblich kleiner ist als die des Ausgangspulvers. Anschließend wird nach Ablauf einer weiteren, jeweils vorher festgelegten Sedimentationszeit, über die in der Höhe weiter unten liegenden Auslässe nacheinander die entsprechenden Suspensionsfraktionen entnommen und entsprechend gröbere Feinpulver gewonnen. |
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100 | SEPARATION AND METHOD OF USE OF DENSITY SPECIFIC BLOOD CELLS | EP87902238.0 | 1987-03-04 | EP0260315A1 | 1988-03-23 | CERCEK, Boris; CERCEK, Lea |
Procédé amélioré de détection de certaines maladies et de certaines conditions somatiques se fondant sur la réaction à des antigènes associés à la maladie ou aux conditions que l'on désire déceler de la part de lymphocytes présentant des densités de flottaison allant de 1,0590g/cm3 à 1,0670g/cm3 et des densités allant de 1,0690g/cm3 à 1,0730g/cm3 dans une solution à gradient de densité continu possédant une osmolalité comprise entre 0,315 et 0,320 osm/kg à une température de 20°C. La réaction est indiquée par des modifications de la structure de la matrice cytoplasmique du globule, ainsi qu'on peut la mesurer par polarisation par fluorescence de fluorescine intracellulaire. Les lymphocytes sont séparés du sang périphérique par centrifugation dans une solution à gradient de densité continu possédant des gradients de densité de délimitation qui couvrent la plage de densité de flottaison des lymphocytes à séparer. |