| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 41 | JPH02503690A - | JP50769189 | 1989-08-03 | JPH02503690A | 1990-11-01 | |
| 42 | JPS5033173A - | JP7863174 | 1974-07-09 | JPS5033173A | 1975-03-31 | |
| 43 | PROCESSES FOR PRODUCING HIGH BIOGENIC CONCENTRATION FISCHER-TROPSCH LIQUIDS DERIVED FROM MUNICIPAL SOLID WASTES (MSW) FEEDSTOCKS | EP15898468.2 | 2015-10-30 | EP3322770A1 | 2018-05-23 | LUCAS, Stephen H.; TIVERIOS, Peter G.; RICH, Lewis L. |
| Processes for producing high biogenic concentration Fischer-Tropsch liquids derived from the organic fraction of municipal solid wastes (MSW) feedstock that contains a relatively high concentration of biogenic carbon (derived from plants) and a relatively low concentration of non-biogenic carbon (derived from fossil sources) wherein the biogenic content of the Fischer-Tropsch liquids is the same as the biogenic content of the feedstock. | ||||||
| 44 | WASTE TREATMENT | EP11724434.3 | 2011-05-06 | EP2566809A1 | 2013-03-13 | CHAPMAN, Chris; STEIN, Rolf; BROOKS, Martin; MANUKIAN, Edward, S.; CLARK, Robert, M. |
| A process and related apparatus for the treatment of hazardous waste and an initially separate waste stream, the process comprising gasifying the waste stream in a gasification unit to produce an offgas and a char material; and plasma treating the offgas, and optionally the char material, in a plasma treatment unit to produce a syngas; and blending hazardous waste with the waste stream at a point in the process determined by the relative chemical and/or physical properties of the hazardous waste and the waste stream. | ||||||
| 45 | PROCESSES FOR ECONOMICALLY CONVERTING MUNICIPAL SOLID WASTE INTO ETHANOL | EP11740545.6 | 2011-02-08 | EP2534122A2 | 2012-12-19 | LUCAS, Stephen, H.; TIVERIOS, Peter, G.; JONES, James, R. |
| Processes for producing high biogenic concentration Fischer-Tropsch liquids derived from the organic fraction of municipal solid wastes (MSW) feedstock that contains a relatively high concentration of biogenic carbon (derived from plants) and a relatively low concentration of non-biogenic carbon (derived from fossil sources) wherein the biogenic content of the Fischer-Tropsch liquids is the same as the biogenic content of the feedstock. | ||||||
| 46 | Method and system for retrieving metals, ecological sludge and energy from waste electronic equipment | EP12460014.9 | 2012-04-02 | EP2508271A2 | 2012-10-10 | Malecki, Stanislaw; Jarosz, Piotr; Kalawski, Krzysztof; Szabowski, Jerzy; Zajac, Wojciech; Zajac, Kazimierz |
The method of destruction of and retrieving metals, ecological sludge, gas and energy from waste electrotechnical and electronic equipment according to the invention consists in that it is carried out in three basic stages, closely interrelated and following in succession, where in the first stage, the formerly stored equipment is disassembled on the multistation semi-automatic processing line (4) and sorted into groups of components containing iron (5), plastics (6), copper (7), aluminum (8), electrical batteries (9); moreover, luminophore (10) is sucked off from picture tubes, and refrigerant and oil (11) from refrigerating units, and then the sorted iron elements containing iron and aluminum alloys are transported to storages (14 and 15, respectively), while elements containing plastics (6), copper components (7) and electrical batteries (9) to fragmenting devices (18), (21) and (25). Crushed plastics (6) are transported by means of a conveyor to the energy generator; crushed electronic modules (21) to the converter-plasma furnace (32); and fragmented batteries (9) as well as luminophore (10) and oil (11) to the gasifier-plasma furnace (40), where metal alloys (29), (33) and (41), sludges (30), (34) and (42) and syngases (28), (35) and (43) are separated from them; then metal alloys and sludges by means of a belt conveyor (51) are transported to induction crucible furnaces (47) and subject to fire refining, and syngases to the plasma converter (44) and then to the cooling-cleaning device (45) and to the gas furnace (49) and heat exchanger (50), while the quality of combustion gases leaving the gas furnace (49) for the stack (58) is subject to continuous control on the monitoring device (62).
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| 47 | METHOD AND APPARATUS FOR PLASMA GASIFICATIION OF CARBONIC MATERIAL BY MEANS OF MICROWAVE RADIATION | EP08778971.5 | 2008-06-25 | EP2163597A1 | 2010-03-17 | LEÓN SÁNCHEZ, Antonio |
A method and apparatus for gasifying carbonic material in order to produce carbon monoxide and hydrogen; the method comprises the following steps: (a) providing carbonic material; (b) heating, by means of microwave radiation, the carbonic material provided until a plasma point cloud forms in the carbonic material; (c) causing the cloud of plasma points of carbonic material to react with superheated water vapour in order to produce a synthesis gas; and (d) purifying the produced synthesis gas by refeeding it through the cloud of plasma points in the carbonic material wherein it is broken up by microwave radiation of step (b) to achieve the generally complete transformation of the synthesis gas into carbon monoxide and hydrogen. Additionally the cloud of plasma points reacts with oxidation gas (air, oxygen or gas enriched with oxygen) in order to produce the synthesis gas. |
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| 48 | Verfahren zum Betreiben eines Hochtemperaturreaktors zur Behandlung von Entsorgungsgütern | EP97101505.2 | 1997-01-31 | EP0790291B1 | 2001-07-18 | Kiss, Günter H. |
| 49 | Verfahren zum Vergasen von Abfallstoffen in der zirkulierenden Wirbelschicht | EP95104128.4 | 1995-03-21 | EP0676465B1 | 1998-08-05 | Albrecht, Johannes, Dr.; Löffler, Johannes, Dr.; Reimert, Rainer, Dr.; Hirsch, Martin, Dr. |
| 50 | Verfahren zum Betreiben eines Hochtemperaturreaktors zur Behandlung von Entsorgungsgütern | EP97101505.2 | 1997-01-31 | EP0790291A3 | 1997-11-05 | Kiss, Günter H. |
Die Erfindung betrifft ein Verfahren zum Betreiben eines Hochtemperaturreaktors zur Behandlung von heterogenen Entsorgungsgütern, bei dem die Entsorgungsgüter über eine Beschickungsstelle in den Reaktor eingebracht werden und unterhalb der Beschickungsstelle ein loses, geschüttetes Vergasungsbett bilden, in dem durch Sauerstoff die anorganischen bzw. organischen Bestandteile einer Aufschmelzung bzw. Vergasung und Homogenisierung unterworfen werden und oberhalb der Beschickungsstelle die gasförmigen Vergasungsprodukte zur Bildung und Stabilisierung von Synthesegas einer Hochtemperaturbehandlung unter Sauerstoffzugabe unterzogen werden, wobei zur Hochtemperaturbehandlung wassergekühlte Sauerstofflanzen eingesetzt werden. |
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| 51 | Verfahren zum Betreiben eines Hochtemperaturreaktors zur Behandlung von Entsorgungsgütern | EP97101505.2 | 1997-01-31 | EP0790291A2 | 1997-08-20 | Kiss, Günter H. |
Die Erfindung betrifft ein Verfahren zum Betreiben eines Hochtemperaturreaktors zur Behandlung von heterogenen Entsorgungsgütern, bei dem die Entsorgungsgüter über eine Beschickungsstelle in den Reaktor eingebracht werden und unterhalb der Beschickungsstelle ein loses, geschüttetes Vergasungsbett bilden, in dem durch Sauerstoff die anorganischen bzw. organischen Bestandteile einer Aufschmelzung bzw. Vergasung und Homogenisierung unterworfen werden und oberhalb der Beschickungsstelle die gasförmigen Vergasungsprodukte zur Bildung und Stabilisierung von Synthesegas einer Hochtemperaturbehandlung unter Sauerstoffzugabe unterzogen werden, wobei zur Hochtemperaturbehandlung wassergekühlte Sauerstofflanzen eingesetzt werden. |
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| 52 | Synthesis gas separation and reforming process | US14031182 | 2013-09-19 | US09764277B2 | 2017-09-19 | Richard Peter Glynn Jewell; Melissa Gaucher; Louis Denomme |
| A method of obtaining purified hydrogen and purified carbon monoxide from crude synthesis gas. A first crude synthesis gas stream is passed through a first separation zone to separate a hydrogen stream from a stream comprising carbon monoxide and methane. The carbon monoxide and methane are subjected to thermal reforming to produce a second crude synthesis gas, which is passed through a second separation zone to separate carbon monoxide from the second crude synthesis gas stream. | ||||||
| 53 | METHOD USING PLASMA-COUPLED SOLAR THERMAL ENERGY AND RELATED DEVICE | US15116723 | 2015-02-06 | US20160348211A1 | 2016-12-01 | Nicolas UGOLIN |
| A microwave thermosolar method and device used in a tubular reactor (110) includes a conveyor for substrates defined as materials thus conveyed. According to this method, a step is provided for circulating an electric current in the conveyor in order to produce heat in this conveyor by Joule effect and optionally to cause, in the substrates, at least some of the following: curing, pyrolyses, gasifications, fusions and chemical reactions including oxidation-reduction reactions, under the action of the electric current. | ||||||
| 54 | Gasification system with processed feedstock/char conversion and gas reformulation | US14173957 | 2014-02-06 | US09321640B2 | 2016-04-26 | Andreas Tsangaris; Marc Bacon |
| The invention provides a system designed for the complete conversion of carbonaceous feedstock into syngas and slag. The system comprises a primary chamber for the volatilization of feedstock generating a primary chamber gas (an offgas); a secondary chamber for the further conversion of processed feedstock to a secondary chamber gas (a syngas) and a residue; a gas-reformulating zone for processing gas generated within one or more of the chambers; and a melting chamber for vitrifying residue. The primary chamber comprises direct or indirect feedstock additive capabilities in order to adjust the carbon content of the feedstock.The system also comprises a control system for use with the gasification system to monitor and regulate the different stages of the process to ensure the efficient and complete conversion of the carbonaceous feedstock into a syngas product. | ||||||
| 55 | System and method for production of Fischer-Tropsch synthesis products and power | US13661807 | 2012-10-26 | US09163179B2 | 2015-10-20 | Bruce E. McComish; Benjamin H. Carryer; Bryan C. Borum; Weibin Jiang; Mark D. Ibsen; Mark K. Robertson; Eric R. Elrod; Sim Weeks; Harold A. Wright |
| A method for generation of power and Fischer-Tropsch synthesis products by producing synthesis gas comprising hydrogen and carbon monoxide, producing Fischer-Tropsch synthesis products and Fischer-Tropsch tailgas from a first portion of the synthesis gas, and generating power from a second portion of the synthesis gas, from at least a portion of the Fischer-Tropsch tailgas, or from both. The method may also comprise conditioning at least a portion of the synthesis gas and/or upgrading at least a portion of the Fischer-Tropsch synthesis products. A system for carrying out the method is also provided. | ||||||
| 56 | Hydrogen sulfide and carbonyl sulfide removal apparatus using microwave plasma, and method thereof | US14062490 | 2013-10-24 | US09090840B2 | 2015-07-28 | Sang Jun Yoon; Jae Goo Lee; Yong Ku Kim |
| A hydrogen sulfide and carbonyl sulfide removal method using microwave plasma comprising a hydrogen sulfide and carbonyl sulfide containing mixed-gas supplying step, a microwave supplying step, a plasma flame forming step, a hydrogen sulfide and carbonyl sulfide decomposing step in which hydrogen sulfide and the carbonyl sulfide are dissociated into atomic units, a rebinding step in which atomic units are rebound so that combustible gases are generated, and a separately collecting step in which the gases are separated and then are separately collected. | ||||||
| 57 | Waste treatment | US13636059 | 2011-03-21 | US08957275B2 | 2015-02-17 | Rolf Stein; Chris Chapman |
| The present invention relates to a process for the treatment of hazardous waste, the process comprising: (i) providing a hazardous waste; (ii) providing a further waste; (iii) plasma treating the hazardous waste in a first plasma treatment unit, (iv) gasifying the further waste in a gasification unit to produce an offgas and a char material; and (v) plasma treating the offgas, and optionally the char material, in a second plasma treatment unit to produce a syngas, (vi) optionally treating the syngas in a gas cleaning plant, wherein the first plasma treatment unit is arranged to plasma treat at least some of the solid by-products from the gasification unit and/or the second plasma treatment unit and/or the gas cleaning plant. | ||||||
| 58 | GASIFICATION SYSTEM WITH PROCESSED FEEDSTOCK/CHAR CONVERSION AND GAS REFORMULATION | US14173957 | 2014-02-06 | US20140332724A1 | 2014-11-13 | Andreas TSANGARIS; Marc Bacon |
| The invention provides a system designed for the complete conversion of carbonaceous feedstock into syngas and slag. The system comprises a primary chamber for the volatilization of feedstock generating a primary chamber gas (an offgas); a secondary chamber for the further conversion of processed feedstock to a secondary chamber gas (a syngas) and a residue; a gas-reformulating zone for processing gas generated within one or more of the chambers; and a melting chamber for vitrifying residue. The primary chamber comprises direct or indirect feedstock additive capabilities in order to adjust the carbon content of the feedstock.The system also comprises a control system for use with the gasification system to monitor and regulate the different stages of the process to ensure the efficient and complete conversion of the carbonaceous feedstock into a syngas product. | ||||||
| 59 | METHOD FOR PURIFICATION AND CONDITIONING OF CRUDE SYNGAS BASED ON PROPERTIES OF MOLTEN SALTS | US14125857 | 2012-05-24 | US20140131621A1 | 2014-05-15 | Xiaobo Wang; Zengli Zhao; Haibin Li; Anqi Liu; Hongxiang Wu |
| A method for purification and conditioning of crude syngas based on properties of molten salts, includes removing particles at a high-temperature by enabling the high-temperature crude syngas produced by a gasification device to firstly pass through a high-temperature particle removal device to remove solid particles in the gas; removing hydrocarbons in the presence of oxygen by introducing an oxidant into the crude syngas after treatment, selectively removing the hydrocarbons in the crude syngas and simultaneously utilizing high temperature produced by oxidation of the hydrocarbons to crack tar; and removing gas pollutants and conditioning by introducing the obtained crude syngas into molten salts medium, removing pollutants containing sulfur and chlorine in the crude syngas, and simultaneously adjusting the H2/CO ratio of the syngas to obtain purified syngas. | ||||||
| 60 | Synthesis Gas Separation and Reforming Process | US14031182 | 2013-09-19 | US20140086818A1 | 2014-03-27 | Richard Peter Glynn Jewell; Melissa Gaucher; Louis Denomme |
| A method of obtaining purified hydrogen and purified carbon monoxide from crude synthesis gas. A first crude synthesis gas stream is passed through a first separation zone to separate a hydrogen stream from a stream comprising carbon monoxide and methane. The carbon monoxide and methane are subjected to thermal reforming to produce a second crude synthesis gas, which is passed through a second separation zone to separate carbon monoxide from the second crude synthesis gas stream. | ||||||
