公开(公告)号：EP1725635B1

公开(公告)日：2018-08-15

申请号：EP04762836.7

申请日：2004-09-16

申请人： Jacobsen, Anker Jarl

发明人： Jacobsen, Anker Jarl

IPC分类号： C10J3/04

CPC分类号： F28D20/0056 ,  C10J3/04 ,  C10J3/12 ,  C10J3/14 ,  C10J3/721 ,  C10J3/723 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1223 ,  C10J2300/1253 ,  C10J2300/1646 ,  C10J2300/165 ,  C10J2300/1665 ,  C10J2300/1693 ,  C10J2300/1807 ,  C10J2300/1823 ,  C10J2300/1884 ,  C10K3/023 ,  Y02E50/18 ,  Y02E50/32 ,  Y02E60/142 ,  Y02P20/129 ,  Y02P20/145

摘要： Method and apparatus for producing synthesis gas comprising the steps of combusting (4) a combustible gas to form hot flue gasses (7), passing the flue gasses (7) through heat storing means (1) so as to heat the heat storing means (1) to an elevated temperature, using the heat thus stored to heat biomass (2) to an elevated temperature so as to form synthesis gas, and withdrawing at least part of the synthesis gas formed, wherein following heating of the heat storing means (1) gaseous medium is circulated through the heat storing means (1), the biomass (2) and back to the heat storing means (1). Furthermore computer program product for performing the method of the invention and the use of the produced biogas are disclosed.

公开(公告)号：EP3094706B1

公开(公告)日：2018-04-04

申请号：EP15704375.3

申请日：2015-01-13

申请人： Turboden S.p.A.

发明人： BINI, Roberto ,  GAIA, Mario

IPC分类号： C10J3/20 ,  F01D15/10 ,  F02B65/00 ,  F02C3/28 ,  C10J3/02 ,  C10J3/72 ,  F02B63/04

CPC分类号： C10J3/02 ,  C10J3/20 ,  C10J3/721 ,  C10J2200/156 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/1223 ,  C10J2300/1653 ,  F01D15/10 ,  F02B63/04 ,  F02B65/00 ,  F02C3/28 ,  F05D2220/32 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/145

摘要： A method for producing syngas from preferably vegetal biomass is described. The method provides for the use of a fixed bed gasifier, equipped with two reactors. The biomass is fed to both reactors together with a primary flow rate of air. Advantageously, the method according to the present invention is different from the known art since a secondary flow rate of air is withdrawn from the first reactor at the area where the biomass dries, and fed to the second reactor at the area where the biomass dries, and vice versa, alternately during time. Alternatively, an oscillating air flow is created in each reactor. The achievable result is a greater syngas production, but not exclusively. The syngas quality is improved too, since the biomass has a longer time for completing the gasification reactions.

公开(公告)号：EP3000865B1

公开(公告)日：2018-03-14

申请号：EP14801705.6

申请日：2014-04-11

申请人： Urbaser, S.A.

发明人： BILBAO DUÑABEITIA, Rafael ,  ARAUZO PÉREZ, Jesús María ,  GUERRERO ÁLVAREZ, Marta ,  GALA BURO, Alberto Jesús ,  ARTIGAS AYALA, Alfonso ,  FERNÁNDEZ GIMÉNEZ, Eduardo

IPC分类号： C10J3/46 ,  B09B3/00 ,  C01B3/58 ,  C10K3/02

CPC分类号： C10J3/463 ,  C01B3/58 ,  C01B2203/0233 ,  C01B2203/0435 ,  C01B2203/048 ,  C01B2203/1252 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10K3/023

摘要： The present invention relates to a method for producing a synthesis gas from municipal solid waste (MSW) and, more particularly, from the fraction thereof called refuse-derived fuel (RDF). The method comprises a step of gasification on a bubbling fluidized bed at atmospheric pressure and temperatures in the range of 750°C a 850°C, using oxygen-enriched air as a gasifying agent, and a step of immediate cleaning and conditioning of the synthesis gas, mainly based on the use of a catalytic reforming reactor comprising a bed formed by a metal catalyst, which operates at a temperature between 750°C and 850°C, where the endothermic reforming process is carried out with water vapor from tars and other hydrocarbons.

公开(公告)号：EP3088492B1

公开(公告)日：2018-02-07

申请号：EP15166002.4

申请日：2015-04-30

申请人： WS-Wärmeprozesstechnik GmbH

发明人： Wünning, Joachim A. ,  Wünning, Joachim G.

IPC分类号： C10J3/26 ,  C10J3/66 ,  C10J3/30 ,  C10K1/32 ,  C10K1/04 ,  C10J3/00 ,  C10B53/02 ,  C01B32/324 ,  C10B47/44 ,  C10B47/06

CPC分类号： C10J3/26 ,  C01B32/324 ,  C10B47/06 ,  C10B47/44 ,  C10B53/02 ,  C10J3/007 ,  C10J3/30 ,  C10J3/66 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/094 ,  C10J2300/0956 ,  C10J2300/1246 ,  C10J2300/1606 ,  C10J2300/1693 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1884 ,  C10K1/046 ,  C10K1/32 ,  Y02E50/14

公开(公告)号：EP2663617B1

公开(公告)日：2017-10-25

申请号：EP12701436.3

申请日：2012-01-09

申请人： Wolf, Bodo M. ,  SunCoal Industries GmbH

发明人： WOLF, Bodo M.

IPC分类号： C10J3/50 ,  C10L5/36 ,  C10L5/44 ,  C10L9/08 ,  C10J3/76 ,  C10J3/48

CPC分类号： C10L5/366 ,  C10J3/485 ,  C10J3/506 ,  C10J3/76 ,  C10J2200/152 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/1223 ,  C10L5/44 ,  C10L9/086 ,  Y02E20/16 ,  Y02E50/10 ,  Y02E50/30

公开(公告)号：EP3041918A4

公开(公告)日：2017-08-30

申请号：EP14842814

申请日：2014-09-04

申请人： AG ENERGY SOLUTIONS INC

发明人： APPEL PHILIP W ,  WEIR THOMAS D ,  CULLEY JACOB M ,  LOVE SARAH E ,  FARLEY TIMOTHY E ,  HOWARD DANIEL A

IPC分类号： C10J3/20 ,  C10J3/74

CPC分类号： C10J3/723 ,  C10J3/32 ,  C10J3/74 ,  C10J2200/156 ,  C10J2200/31 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/165 ,  C10J2300/1869 ,  C10J2300/1884 ,  C10K1/026 ,  Y02P20/145

公开(公告)号：EP3183322A1

公开(公告)日：2017-06-28

申请号：EP15834115.6

申请日：2015-08-21

申请人： Simple Approach Systems Inc.

发明人： REHMAT, Amirali G.

IPC分类号： C10J3/00

CPC分类号： C10J3/005 ,  C10J1/26 ,  C10J3/723 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0976 ,  Y02P20/129

摘要： An apparatus, system, and method for processing hydrocarbon-containing wastes are described. The system and method include the use of a gasification apparatus comprising a rotary kiln reactor and a gas distributor. The rotary kiln reactor and gas distributor are configured to generate multiple reaction environments within the gasification apparatus. Each of the reaction environments has unique temperature reaction conditions to suit various physical and chemical properties associated with processing of the varied-source hydrocarbon-containing wastes.

摘要翻译： 描述了用于处理含烃废物的装置，系统和方法。 该系统和方法包括使用包括回转窑反应器和气体分配器的气化装置。 回转窑反应器和气体分配器构造成在气化装置内产生多个反应环境。 每个反应环境具有独特的温度反应条件以适应与处理不同来源的含烃废物相关的各种物理和化学性质。

公开(公告)号：EP2895579B1

公开(公告)日：2016-11-09

申请号：EP13798924.0

申请日：2013-09-13

申请人： Big Dutchman International GmbH

发明人： SCHWARZ, Armin

IPC分类号： C10J3/06 ,  C10J3/26 ,  C10J3/64 ,  C10J3/72 ,  C10J3/82

CPC分类号： C10J3/723 ,  C10J3/06 ,  C10J3/26 ,  C10J3/64 ,  C10J3/725 ,  C10J3/82 ,  C10J2200/15 ,  C10J2200/152 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0956 ,  C10J2300/1207 ,  C10J2300/1609 ,  C10J2300/1618 ,  C10J2300/1846

公开(公告)号：EP2686287A4

公开(公告)日：2016-11-02

申请号：EP12745320

申请日：2012-02-17

申请人： JURANITCH JAMES CHARLES

发明人： JURANITCH JAMES CHARLES

IPC分类号： C06B43/00 ,  C06D5/00 ,  C10J3/57

CPC分类号： F01K13/006 ,  C01B3/02 ,  C01B3/342 ,  C01B3/348 ,  C01B2203/0216 ,  C01B2203/0255 ,  C01B2203/0861 ,  C10J3/57 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1238 ,  C10J2300/1276 ,  C10J2300/1675 ,  C21B13/0073 ,  F01K7/16 ,  F23G5/027 ,  F23G5/085 ,  F23G2202/20 ,  F23G2204/201 ,  F23G2204/204 ,  Y02E20/12 ,  Y02E20/344 ,  Y02P10/34 ,  Y02P20/13

摘要： A method of generating syngas as a primary product from renewable feedstock, fossil fuels, or hazardous waste with the use of a cupola. The cupola operates selectably on inductive heat alone, chemically assisted heat, or plasma assisted heat. Additionally, the operation of the cupola is augmented by the use of direct acting carbon or graphite rods that carry electrical current for additional heat generation into the metal bath that is influenced by the inductive element. The method includes the steps of providing a cupola for containing a metal bath; and operating an inductive element to react with the metal bath. Feedstock in the form of a combination of fossil fuel, a hazardous waste, and a hazardous material is supplied to the cupola. A plasma torch operates on the metal bath selectably directly and indirectly. Steam, air, oxygen enriched air, and oxygen are supplied in selectable combinations.

公开(公告)号：EP2928590A4

公开(公告)日：2016-09-21

申请号：EP13863180

申请日：2013-12-10

申请人： SOUTHERN CO

发明人： LIU GUOHAI ,  VIMALCHAND PANNALAL ,  PENG WANWANG

IPC分类号： B01J8/18 ,  B01J8/26 ,  C01B3/30 ,  C10J3/48 ,  C10J3/72 ,  C10K3/00 ,  F23C10/01

CPC分类号： C10J3/482 ,  C01B3/30 ,  C01B2203/0277 ,  C01B2203/04 ,  C01B2203/049 ,  C10J3/721 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1807 ,  C10K3/005 ,  Y02E20/18 ,  Y02P20/125

摘要： A second stage gasification unit in a staged gasification integrated process flow scheme and operating methods are disclosed to gasify a wide range of low reactivity fuels. The inclusion of second stage gasification unit operating at high temperatures closer to ash fusion temperatures in the bed provides sufficient flexibility in unit configurations, operating conditions and methods to achieve an overall carbon conversion of over 95% for low reactivity materials such as bituminous and anthracite coals, petroleum residues and coke. The second stage gasification unit includes a stationary fluidized bed gasifier operating with a sufficiently turbulent bed of predefined inert bed material with lean char carbon content. The second stage gasifier fluidized bed is operated at relatively high temperatures up to 1400° C. Steam and oxidant mixture can be injected to further increase the freeboard region operating temperature in the range of approximately from 50 to 100° C. above the bed temperature.