| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | REMOVAL OF HYDROPHOBIC PARTICLES USING CARBON DIOXIDE | CA3058159 | 2018-03-27 | CA3058159C | 2021-11-30 | RYAN MICHAEL STEPHEN |
| A plurality of collection surfaces for use in an aqueous slurry has a polymeric coating to provide a compliant and sticky surface. The polymer coating has a chemical to render the surface hydrophobic so as to attract hydrophobic or hydrophobized mineral particles in the slurry. The substrate can take the form of a conveyor belt, a bead, a mesh, an impeller, a filter or a flat surface. The substrate can also be an open-cell foam. The collection surfaces having the mineral particles attached thereon are caused to interact with liquid and supercritical carbon dioxide so that the mineral particles can be stripped from the collection surfaces. | ||||||
| 142 | COMPOSIÇÃO AQUOSA ESTÁVEL DE COLETORES NEUTROS E SUA UTILIZAÇÃO EM PROCESSOS DE BENEFICIAÇÃO MINERAL | PT15719964 | 2015-04-22 | PT3169439T | 2020-11-27 | |
| 143 | RECOVERY OF HYDROCARBON DILUENT FROM TAILINGS | CA3018717 | 2017-06-05 | CA3018717C | 2020-07-14 | BARA BARRY; BHATTACHARYA SUJIT; MCKNIGHT CRAIG; BULBUC DANIEL JOHN; CYMERMAN GEORGE |
| A method for recovering hydrocarbon diluent from tailings comprising bitumen, particulate solids, hydrocarbon diluent and water, is provided comprising introducing the tailings into a high pressure stripping vessel operating at a pressure greater than 100 kPa; and introducing a stripping gas into the high pressure stripping vessel to strip the hydrocarbon diluent and water from the tailings and form a stripped tailings pool at the bottom of the vessel. | ||||||
| 144 | RECOVERY OF SOLVENTS FROM MIXED PRODUCTION FLUIDS AND SYSTEM FOR DOING SAME | CA2927967 | 2016-04-22 | CA2927967C | 2020-04-07 | NENNIGER JOHN; HOLCEK RONALD GERRY; EICHHORN MARK ANTHONY; VERMA SANDEEP; FARRELL SOLIMAR J; CHU LIANJIANG |
| A hydrocarbon separation system and process to separate solvent from mixed fluids extracted from an underground formation. The separation system includes a main separation chamber, a reboiler circuit, and a multi-stage reflux circuit. The main separation chamber separates liquid inputs into bottom liquids and top vapours. The reboiler circuit separates bottom liquids received from the main separation chamber into purified solvent and a reboiler vapour fraction. The multi-stage reflux circuit receives the top vapours from the main separation chamber and separates solvent from the top vapours in two stages. The first stage separates a first reflux liquid from the top vapours, and passes the first reflux liquid to the main separation chamber. The second stage receives top vapours remaining in the first stage, separates solvent therefrom, passes the separated solvent to the main separation chamber, and exhausts any remaining vapours. | ||||||
| 145 | PROCESO DE MAXIMIZACIÓN DE VALOR DE UN RECURSO DE MENA DE SULFURO MEDIANTE RECHAZO SECUENCIAL DE DESECHOS | ARP170101829 | 2017-06-30 | AR108937A1 | 2018-10-10 | |
| El proceso integrado para recuperar metales valiosos a partir de mena de sulfuro incluye los pasos de clasificación en bruto 16 y cribado 24 / 28 de la mena aplastada. La corriente de menas gruesas clasificadas / cribadas se muele y ordena 20 para proporcionar una fracción de gruesos 34 adecuada para flotación de gruesos y una primera fracción de finos 38 adecuada para flotación. La fracción de gruesos adecuada para la flotación de gruesos se somete a una flotación de gruesos 36 para obtener así una ganga 42 y un concentrado intermedio 46. El concentrado intermedio se somete a molienda 48 para proporcionar una segunda fracción de finos adecuada para flotación convencional. La primera fracción de finos y la segunda fracción de finos se someten a una flotación convencional 40 para proporcionar un concentrado y relaves. Este proceso capitaliza la heterogeneidad natural de los yacimientos de sulfuro y utiliza tecnologías de reducción de clasificación en bruto, cribado y flotación de gruesos en una configuración multietapa para rechazar la máxima cantidad de ganga de desecho antes de la conminución de finos. | ||||||
| 146 | processos para flotação de minério mineral na presença de íons de metal multivalente | BR102017016779 | 2017-08-04 | BR102017016779A2 | 2018-02-27 | ANNA CASASUS; DUANE C WILSON; SCOTT ROSENCRANCE; XIHUI YIN |
| processos para flotação de minério mineral na presença de íons de metal multivalente são divulgados processos para enriquecer um mineral desejado a partir de um minério compreendendo o mineral desejado e ganga, em que o processo compreende realizar um processo de flotação na presença de um ou mais agentes quelantes, um ou mais agentes de coleta, um ou mais tipos de íons de metal multivalente, e opcionalmente, um ou mais depressores, em uma solução, em que os um ou mais agentes quelantes são capazes, sozinhos ou como um grupo de compostos, de sequestrar um metal ou íon de metal na forma de um complexo de metal-agente quelante que permanece pelo menos parcialmente solúvel na solução. | ||||||
| 147 | RECOVERY OF SOLVENTS FROM MIXED PRODUCTION FLUIDS AND SYSTEM FOR DOING SAME | CA2927967 | 2016-04-22 | CA2927967A1 | 2017-10-22 | NENNIGER JOHN; HOLCEK RONALD GERRY; EICHHORN MARK ANTHONY; VERMA SANDEEP; FARRELL SOLIMAR J; CHU LIANJIANG |
| A separation facility and process to separate a mixed fluid stream produced from an underground formation by means of an in situ solvent based hydrocarbon extraction process into separate process streams. The separation facility includes a first separation stage to separate any produced mixed fluids into at least a mixed water process stream and a heavy and light hydrocarbon process stream. There is a second separation stage to separate said heavy and light hydrocarbon process stream into a heavy hydrocarbon process stream and a bulk light hydrocarbon process stream. Then there is a bulk light hydrocarbon separation stage for separating said solvent from the balance of said bulk light hydrocarbon process stream. This stage may include the use of a two or more step separation to minimize energy consumption. Then there is a mixed water separation stage to separate said mixed water process stream into a lower density mixed hydrocarbon rich process stream and a higher density water process stream. Lastly there is a final hydrocarbon separation stage to separate at least some residual light hydrocarbons from said heavy hydrocarbon process stream. | ||||||
| 148 | METHOD FOR RECOVERING SOLVENT FROM FROTH TREATMENT TAILINGS WITH IN-SITU STEAM GENERATION | CA2924307 | 2016-03-15 | CA2924307A1 | 2017-09-15 | WU XIN ALEX; BHATTACHARYA SUJIT |
| A method for recovering hydrocarbon diluent from froth treatment tailings comprising bitumen, solids, hydrocarbon diluent and water is provided, comprising; introducing the froth treatment tailings into a vessel chamber and allowing the coarse solids to settle to the bottom of the vessel and form a solids layer having a portion of hydrocarbon diluent and a portion of water trapped therein; and heating the water in the solids layer to generate steam bubbles in-situ and strip the hydrocarbon diluent associated with the coarse solids to produce stripped tailings. | ||||||
| 149 | ODOUR CONTROL | CA2725967 | 2009-04-06 | CA2725967C | 2017-07-18 | DU PLESSIS CHRIS; SENIOR GEOFFERY DAVID |
| Organic compounds that are associated with production of nickel sulphide concentrates are a major cause of the generation of odours in flotation processing plants and in stock-piled concentrates. The present invention discloses a process for producing a mineral concentrate product that at is at least a substantially odour-free product from a mined material that comprises floating selected mineral particles from a slurry of the mined material and forming a wet concentrate in the form of a froth product slurry, which includes a collector in the form of an organic xanthate compound for adsorbing selected mineral particles and promoting the flotation of the mineral particles, and treating the froth product slurry with heat and the addition of one or more chemicals selected from the group consisting of nitrate, molybdate, activated carbon and mixtures thereof, to prevent residual organic xanthate compounds or mineral concentrates from being converted to odorous compounds. | ||||||
| 150 | Reactivo colector selectivo de todo tipo de arcillas presentes en los yacimientos de minerales de metales no ferrosos que comprende una mezcla de sales de alquil aril sulfonatos, y una mezcla de sales de alquil hidroximatos. metodo de flotación usando dicho reactivo. | CL2016001201 | 2016-05-19 | CL2016001201A1 | 2017-04-21 | ZORAN PETKOVIC; JORGE IPINZA ABARCA |
| Formula colectora selectiva utilizada en flotación de todo tipo de arcillas presentes en los yacimientos de minerales de metales no ferrosos, sean sulfuros u óxidos, tales como Cu, Pb, Zn, Mo, Ag y Au, CARACTERIZADO por una composición de: 30% a 35% de Dodecilbencenosulfonato de amina, 51% a 55% de Dodecilbencenosulfonato de etilendiamina, 10% a 5% de dodecilbencenosulfonato de trietanolamina, 9% a 5% de Dodecilhidroxamato de potasio; y Método de flotación selectiva de arcilla y minerales no ferrosos. | ||||||
| 151 | PROCESSO DE FLUTUAÇÃO DE ESPUMA PARA A SEPARAÇÃO DE SILICATOS E DE CARBONATOS DE METAIS ALCALINOTERROSOS UTILIZANDO UM COLETOR QUE COMPREENDE PELO MENOS UMA POLIALQUILENOIMINA HIDROFOBICAMENTE MODIFICADA | PT10157099 | 2010-03-19 | PT2366456E | 2014-01-21 | BURI MATTHIAS; RENTSCH SAMUEL; GANE PATRICK A C; SOETEMANN JOERG |
| 152 | РЕГУЛИРОВАНИЕ ЗАПАХА | EA201170060 | 2009-04-06 | EA018117B1 | 2013-05-30 | DU PLESSIS CHRIS; SENIOR GEOFFERY DAVID |
| Визобретениипредставленспособполученияминеральногоконцентратногопродукта, которыйявляется, поменьшеймере, посуществу, продуктомбеззапаха, содержитлюбойодинилинесколькопунктовиз (а) удаленияорганическихсоединенийпутем (i) обработкипенистойсуспензиипродукта, содержащейвсплывшиеминеральныечастицы, судалениеморганическихсоединенийизданныхминеральныхчастици/или (ii) термическойобработки, и (b) добавленияхимическихагентовдляпредотвращенияостаточныхорганическихсоединенийнаминеральныхконцентратахотпревращенияв пахнущиесоединения, вчастности, когдаконцентратысохраняютсяилитранспортируются. | ||||||
| 153 | PROCESS AND UNIT FOR SOLVENT RECOVERY FROM SOLVENT DILUTED TAILINGS DERIVED FROM BITUMEN FROTH TREATMENT | CA2931815 | 2011-03-01 | CA2931815A1 | 2012-09-01 | DUERR RYAN; VAN DER MERWE SHAWN; HANN TOM |
| A tailings solvent recovery unit (TSRU) and a process for recovering paraffinic solvent from solvent diluted tailings derived from a bitumen froth treatment operation are described. The solvent diluted tailings are processed in order to recover certain compounds, such iso-paraffins or cyclo-paraffins, which are present in the paraffinic solvent previously added to the bitumen froth and which are preferentially retained within asphaltene-bitumen matrices with respect to other paraffins of the paraffinic solvent due to lower diffusivity. | ||||||
| 154 | PROCESO PARA PRODUCIR UN PRODUCTO CONCENTRADO MINERAL LIBRE DE OLOR | CO10137058 | 2010-11-04 | CO6311090A2 | 2011-08-22 | DU PLESSIS CHRIS; SENIOR GEOFFERY DAVID |
| Un proceso para producir un producto concentrado que es por lo menos un producto sustancialmente libre de olor que comprende cualquiera de una o más de una de (a) remoción de compuestos orgánicos por (i) tratamiento de un lodo espumoso del producto que contiene partículas del mineral en flotación para remover los compuestos orgánicos de las partículas del mineral y/o (ii) tratamiento térmico, y (b) la adición de productos químicos para evitar que los compuestos orgánicos residuales sobre los concentrados del mineral se conviertan en compuestos olorosos, particularmente mientras que los concentrados se apilan para almacenamiento o se transportan. | ||||||
| 155 | Austrags- und Reinigungsvorrichtung für verunreinigte Flotationsflüssigkeit bei Flotationsverfahren | DE102008051141 | 2008-10-09 | DE102008051141B4 | 2010-11-25 | KOSLOW ALEXANDER |
| Austrags- und Reinigungseinrichtung für verunreinigte Flotationsflüssigkeit bei Flotationsverfahren, dadurch gekennzeichnet, dass die Flotationsflüssigkeit in eine Sammelkammer (4) über einen Austragschlitz (6) fließt, in der zwei einander gegenüberliegende, zur Übertrittsöffnung (7) hin arbeitende, mit je einem Antrieb (17) ausgestattete Schneckenförderer (9) angeordnet sind und ein von der Übertrittsöffnung (7) unter einem Steigwinkel von etwa 45° zur Vertikalen ausgehender Steigkanal (8) vorgesehen ist, in dem eine Förderschnecke (10), die mit einem Antrieb (18) ausgestattet ist und mit circa 50 U/min rotiert, angeordnet ist, die verschmutzte Flotationsflüssigkeit zu einer mindestens 60 cm über dem Niveau der Flotationsflüssigkeit im Flotationsbecken (1) liegenden Entleerungsöffnung (11) transportiert, an die ein aus feinem Gewebe gefertigter Filtersack (12) anschließt, der Flotationsflüssigkeit in ein Becken (13) gereinigt austreten lässt. | ||||||
| 156 | Discharge and cleaning device for contaminated fluid in flotation process, comprises collecting chamber for flotation fluid over discharge slot, where two opposite facing helical conveyors are provided with drive | DE102008051141 | 2008-10-09 | DE102008051141A1 | 2010-04-22 | KOSLOW ALEXANDER |
| The discharge and cleaning device comprises a collecting chamber (4) for a flotation fluid over a discharge slot (6). Two opposite facing helical conveyors (9) are provided with a drive (17). An ascending channel (8) comes out from an over flow opening (7) at an ascending angle of about 45 degree, where a screw conveyor (10) is provided with a drive (18). | ||||||
| 157 | BRPI0705593 | 2007-11-22 | BRPI0705593A2 | 2009-07-21 | YOSHIDA MARIA IRENE; DE FREITAS CARVALHO CORNELIO; MARQUES DE ARAUJO DANIELLE | |
| 158 | MANIFOLD ASSEMBLY AND METHOD OF USE | CA2616036 | 2007-12-21 | CA2616036A1 | 2009-06-21 | COLENRANDER GERT W |
| The present invention relates to a manifold assembly comprising an inlet and one or more outlets, wherein the inlet and the one or more outlets are in fluid communication via a chamber having a cross-sectional area that is larger than the combined surface area of the one or more outlets. The manifold assembly may be used in a tailings solvent recovery unit. | ||||||
| 159 | Method for separation of waste mixture from wood and rubber, involves placing mixture in flotation basin that is filled with water shifted in pulsation, where rubber is deposited on sieve base to control jerky shaking motion | DE102007024048 | 2007-05-23 | DE102007024048A1 | 2008-11-27 | KOSLOW ALEXANDER |
| The method involves placing mixture in a flotation basin that is filled with water shifted in pulsation. A rubber is deposited on a sieve base to control the jerky shaking motion. The rubber is carried to a discharge opening due to the jerky movements, with changeable cross section, by which the rubber is precipitated in a reservoir below the sieve base. The rubber is removed by a discharge sluice for further utilization. A wood is delivered in a wood collecting container and is supplied to the further utilization. | ||||||
| 160 | A separation process and system | AU2007264411 | 2007-06-29 | AU2007264411A1 | 2008-01-03 | LAMBERT NOEL WILLIAM ALEXANDER |
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