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1. 发明授权

EP3160899B1 METHOD AND APPARATUS FOR PRODUCING H2-RICH SYNTHESIS GAS 有权转让
公开(公告)号：EP3160899B1
公开(公告)日：2018-12-12
申请号：EP15723692.8
申请日：2015-05-13
申请人： CCP Technology GmbH
发明人： KÜHL, Dr. Olaf
IPC分类号： C01B3/24 , C01B32/40 , C10G2/00 , C10K3/04
CPC分类号： C01B3/24 , C01B3/12 , C01B2203/0272 , C01B2203/0283 , C01B2203/0288 , C01B2203/049 , C01B2203/061 , C01B2203/062 , C01B2203/0805 , C01B2203/0844 , C01B2203/0861 , C01B2203/0883 , C01B2203/1276 , C01B2203/141 , C01B2203/145 , C10G2/30 , C10G2/32 , C10G2/34 , C10J3/00 , C10J3/46 , C10J3/721 , C10J2300/0966 , C10J2300/0973 , C10J2300/1618 , C10J2300/1659 , C10J2300/1675 , C10J2300/1853 , C10K3/04 , Y02P20/129
摘要： A method for producing ¾-rich synthesis gas comprises the following steps: decomposing a hydrocarbon-containing fluid into an H2/C-aerosol in a first hydrocarbon converter by supplying energy which is at least partly provided in the form of heat; introducing at least a first stream of the H2/C-aerosol into a first sub-process which comprises the following steps: directing at least a part of the H2/C-aerosol from the first hydrocarbon converter into a first C-converter; introducing CO2 into the first C-converter and mixing the CO2 with the H2/C-aerosol introduced into the first C-converter; converting the mixture of H2/C-aerosol and CO2 into a synthesis gas at a temperature of 800 to 1700° C.; mixing additional H2 with the synthesis gas for the production of H2-rich synthesis gas. In a second sub-process running in parallel with the first sub-process, hydrogen H2 and carbon dioxide CO2 are produced from a hydrocarbon-containing fluid, wherein at least a portion of the CO2 produced in the second sub-process is introduced into the first C-converter; and wherein at least a portion of the H2 produced in the second sub-process is mixed with the synthesis gas from the first C-converter. The CO2 which is needed for the conversion of C in the first C-converter can thereby be provided independently of an external source, and the entire operational sequence is easily controllable.

2. 发明授权

EP2334762B1 METHOD FOR PRODUCTION OF A CLEAN HOT GAS BASED ON SOLID FUELS 有权转让
公开(公告)号：EP2334762B1
公开(公告)日：2018-10-10
申请号：EP09776275.1
申请日：2009-08-28
申请人： Dall Energy Holding ApS
发明人： BENTZEN, Jens Dall
IPC分类号： C10J3/34 , C10J3/72 , C10J3/80 , C10K1/10 , F23L7/00 , F23G5/027 , F23G5/50 , F23G5/24
CPC分类号： F23G5/24 , C10J3/34 , C10J3/723 , C10J3/80 , C10J2200/09 , C10J2200/154 , C10J2200/158 , C10J2300/0916 , C10J2300/092 , C10J2300/0946 , C10J2300/0956 , C10J2300/0973 , C10J2300/1884 , C10J2300/1892 , C10K1/101 , F23G5/027 , F23G5/50 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23L7/007 , F23L2900/00001 , Y02E20/12 , Y02E20/344
摘要： Solid fuel can be converted into a clean hot flue gas with a low content of volatile organic compounds (VOC's), NOx and dust, and clean ash with a low carbon content by means of a stage-divided thermal reactor, where the conversion process of the solid fuel is in separate vertical stages (from below and up): ash burn-out, char oxidation and gasification, pyrolysis, drying, and a gas combustion stage where gas from the gasifier is combusted.

3. 发明授权

EP2558555B1 METHOD FOR GASIFICATION OF CARBONACEOUS MATERIALS 有权
公开(公告)号：EP2558555B1
公开(公告)日：2018-06-06
申请号：EP11716096.0
申请日：2011-04-11
申请人： Ineos Bio SA
发明人： SUTRADHAR, Bhagya, Chandra , KO, Ching-Whan
IPC分类号： C10J3/16 , C10J3/10 , C12P7/02 , C10J3/20 , C10J3/72 , C01B3/36 , C12P7/06 , C12P7/08
CPC分类号： C10B49/02 , C01B3/36 , C01B2203/025 , C10J3/00 , C10J3/002 , C10J3/16 , C10J3/20 , C10J3/721 , C10J2300/092 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/1665 , C10J2300/1681 , C12P7/065 , C12P7/08 , Y02E50/17 , Y02E50/18 , Y02E50/32 , Y02W10/30
摘要： The present disclosure is generally directed to process of gasification of carbonaceous materials to produce synthesis gas or syngas. The present disclosure provides improved methods of gasification comprising adding a molecular oxygen-containing gas and optionally adding water into said gasifier. This disclosure is also directed to process of production of one or more alcohols from said syngas via fermentation or digestion in the presence of at least one microorganism.

4. 发明授权

EP2419497B1 METHOD FOR THE PRODUCTION OF A COMBUSTIBLE GAS FROM A FUEL 有权转让
公开(公告)号：EP2419497B1
公开(公告)日：2018-05-30
申请号：EP10713265.6
申请日：2010-04-14
申请人： Stichting Energieonderzoek Centrum Nederland
发明人： VAN DER MEIJDEN, Christiaan Martinus , RABOU, Lucas Petrus Loduvicus Maria
IPC分类号： C10L3/08 , C10L3/10 , C10J3/00 , C10K3/02 , C10K3/04 , C07C9/04
CPC分类号： C10L3/08 , C10J3/00 , C10J3/482 , C10J3/523 , C10J3/84 , C10J2300/0916 , C10J2300/0956 , C10J2300/0973 , C10J2300/1618 , C10J2300/1662 , C10J2300/1838 , C10K1/005 , C10K1/04 , C10K1/08 , C10K1/143 , C10K3/02 , C10L3/10 , C10L3/102
摘要： Method and system for the production of a combustible gas from a fuel, comprising the conversion of the fuel, at a temperature that is between 600 and 1000° C. and at a pressure that is lower than 10 bar, into at least a combustible gas that comprises CH4, CO, H2, CO2, H2O and higher hydrocarbons in a reactor installation (1). At least part of the higher hydrocarbons present in the combustible gas is catalytically converted into at least CH4, CO, H2, CO2 and H2O in a reactor (45) at a pressure that is lower than 10 bar. After this catalytic conversion, an amount of H2O and an amount of CO2 are removed from the combustible gas in a separator installation (50) at a pressure that is lower than 10 bar. After the removal of H2O and CO2, the pressure of the combustible gas is raised by a compressor (71).

5. 发明授权

EP3126473B1 VERFAHREN UND VORRICHTUNG ZUR UMSETZUNG ORGANISCHER MATERIALIEN IN WASSERSTOFFGAS 有权转让
公开(公告)号：EP3126473B1
公开(公告)日：2018-05-23
申请号：EP15702394.6
申请日：2015-01-16
申请人： CleanCarbonConversion Patents AG
发明人： JENEY, Peter
IPC分类号： C10J3/00 , C10J3/72 , F16L51/02 , F23G5/20 , C10B1/10 , C10B47/30
CPC分类号： C10J3/723 , C01B3/02 , C01B3/501 , C10J3/005 , C10J3/721 , C10J2200/09 , C10J2200/158 , C10J2300/0916 , C10J2300/0946 , C10J2300/0973 , C10J2300/0976 , C10J2300/1276 , C10K1/002 , C10K1/003 , C10K1/007 , F16L51/022 , Y02P20/145

6. 发明授权

EP2478073B1 INTEGRATED GASIFICATION COMBINED CYCLE PLANT WITH CHAR PREPARATION SYSTEM 失效转让
标题翻译：综合气化联合循环厂与制粉系统
公开(公告)号：EP2478073B1
公开(公告)日：2018-03-28
申请号：EP10817971.4
申请日：2010-09-20
申请人： Wormser Energy Solutions, Inc.
发明人： WORMSER, Alex
IPC分类号： C10J3/54 , F02C3/28 , B01D53/62 , B01D53/047 , C10K1/26 , C10K1/32 , C10K1/00 , C10B49/10 , C10J3/48 , C10J3/84 , C10J3/56
CPC分类号： C10B49/10 , B01D53/047 , B01D53/62 , B01D2251/404 , B01D2253/10 , B01D2253/25 , C10J3/56 , C10J3/84 , C10J2300/093 , C10J2300/094 , C10J2300/0943 , C10J2300/0959 , C10J2300/0973 , C10J2300/0983 , C10J2300/1612 , C10J2300/1653 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1884 , C10K1/005 , C10K1/26 , C10K1/32 , F02C3/28 , Y02E20/18 , Y02E20/185

7. 发明公开

EP3174959A4 METHOD OF SYNTHETIC FUEL GAS PRODUCTION 审中-公开
公开(公告)号：EP3174959A4
公开(公告)日：2018-03-07
申请号：EP15827790
申请日：2015-07-28
申请人： SUSTAINABLE WASTE POWER SYSTEMS INC
发明人： GILLESPIE MICHAEL JOSEPH III , GILLESPIE CHRISTOPHER PAUL , ZAMBITO JOSEPH J
IPC分类号： C10J3/48 , C10J3/46 , C10J3/66 , C10J3/74 , C10L9/08
CPC分类号： C10J3/66 , C10J3/466 , C10J3/485 , C10J3/74 , C10J2300/094 , C10J2300/0946 , C10J2300/0959 , C10J2300/0973 , C10J2300/0976 , C10L9/086 , Y02P20/144
摘要： The invention concern methods for converting carbonaceous feedstock slurry into synthetic fuel gas comprising: (a) introducing a carbonaceous feed stock slurry into a first reaction vessel via a continuous feed; (b) converting said carbonaceous feed stock slurry to a carbon char slurry comprising carbon char, and water by allowing said carbonaceous feed stock slurry to have a residency time of between 5 and 30 minutes in said first reaction vessel, said carbonaceous feed stock slurry being heated to a temperature of between about 260 to about 320° C. at a pressure such that water does not flash to steam.

8. 发明授权

EP2129749B1 Vergasungsverfahren mit einem Reduktionsverfahren im stabilen Schwebebett 有权转让
标题翻译：在稳定的悬浮床中进行还原过程的气化过程
公开(公告)号：EP2129749B1
公开(公告)日：2017-11-22
申请号：EP08734625.0
申请日：2008-03-14
申请人： SynCraft Engineering GmbH
发明人： HUBER, Marcel, Bernard
IPC分类号： C10J3/50 , C10J3/66
CPC分类号： C10J3/66 , C10J3/506 , C10J3/721 , C10J3/725 , C10J2200/152 , C10J2300/0916 , C10J2300/092 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/1609 , Y02P20/145

9. 发明授权

EP2542654B1 METHOD OF REFORMING GASIFICATION GAS 有权转让
标题翻译： VERFAHREN ZUR REFORMIERUNG VON VERGASUNGSGAS
公开(公告)号：EP2542654B1
公开(公告)日：2017-04-19
申请号：EP11750242.7
申请日：2011-03-03
申请人： Neste Oyj
发明人： SIMELL, Pekka , KURKELA, Esa , HILTUNEN, Ilkka
IPC分类号： C10K1/34 , B01J23/38 , C10J3/84 , C10K3/02 , C10J3/00 , B01J21/06 , B01J23/40 , C10J3/48
CPC分类号： C10J3/00 , B01J21/066 , B01J23/40 , C10J3/482 , C10J3/84 , C10J2300/0916 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10K1/34 , C10K3/023 , Y02E20/18 , Y02P20/52

10. 发明公开

EP3126473A1 VERFAHREN UND VORRICHTUNG ZUR UMSETZUNG ORGANISCHER MATERIALIEN IN WASSERSTOFFGAS 有权转让
标题翻译： VERFAHREN UND VORRICHTUNG ZUR UMSETZUNG组织机构在WASSERSTOFFGAS
公开(公告)号：EP3126473A1
公开(公告)日：2017-02-08
申请号：EP15702394.6
申请日：2015-01-16
申请人： CleanCarbonConversion Patents AG
发明人： JENEY, Peter
IPC分类号： C10J3/00 , C10J3/72 , F16L51/02 , F23G5/20 , C10B1/10 , C10B47/30
CPC分类号： C10J3/723 , C01B3/02 , C01B3/501 , C10J3/005 , C10J3/721 , C10J2200/09 , C10J2200/158 , C10J2300/0916 , C10J2300/0946 , C10J2300/0973 , C10J2300/0976 , C10J2300/1276 , C10K1/002 , C10K1/003 , C10K1/007 , F16L51/022 , Y02P20/145
摘要： Device (100) for reacting an organic starting material (1) to give a gas which comprises hydrogen, with: • a feed device (30), • a tubular furnace (20) with an entry zone (E), an interior space (I), an axis (R) of rotation and an exit side (A), • a water feed (31) arranged in the region of the feed device (30) or entry zone (E), in order to permit addition of water (W) to the starting material (1), where the arrangement and design of the feed device (30) and the tubular furnace (20) are such that via the feed device (30) it is possible to feed the starting material (1) in the region of the entry zone (E) into the interior space (I) of the tubular furnace (20), and a solid material (2) and a gas mixture (3) can be discharged at the exit side (A) of the tubular furnace (20), where • the tubular furnace (20) comprises a first zone (Z1) and a second zone (Z2), the first zone (Z1) being in a region between the entry zone (E) and the second zone (Z2), and the second zone (Z2) being in a region between the first zone (Z1)and the exit side (A), • the tubular furnace (20) comprises a compensator (21) designed for compensation of different thermal expansions of the first zone (Z1) and the second zone (Z2), · arranged at the exit side (A) of the tubular furnace (20) there is a gas-conducting system (40) designed to conduct the gas mixture (3) onward, • arranged in the region of the gas-conducting system (40) there is a gas monitor (41), the gas monitor (41) being designed to monitor the content of hydrogen in the gas mixture (3), the water feed (31) being amenable to regulation as a function of the content of hydrogen in the gas mixture (3).
摘要翻译：用于使有机原料反应以产生包括氢的气体的装置具有进料装置，具有进入区的管式炉，内部空间，旋转轴线和出口侧，以及由进料装置布置的给水装置或入口区域，并且可以作为气体混合物中氢的含量的函数来控制。进料装置将入口区域中的起始材料进料到管状炉的内部空间中，从其中排出固体材料和气体混合物。管状炉具有用于第一区和第二区的不同热膨胀的补偿器。导气系统包括用于气体混合物中的氢气含量的气体监测器。

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