公开(公告)号：EP3000865A1

公开(公告)日：2016-03-30

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

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.

摘要翻译： 本发明涉及一种从城市固体废物（MSW）生产合成气的方法，更具体地说，涉及一种称为垃圾衍生燃料（RDF）的合成气。 该方法包括使用富氧空气作为气化剂在大气压和750℃-850℃的温度下在鼓泡流化床上气化的步骤，以及立即清洗和调节合成的步骤 气体，主要基于使用催化重整反应器，其包含由金属催化剂形成的床，其在750℃和850℃之间的温度下操作，其中吸热重整过程与来自焦油和其它的水蒸汽进行 烃类。

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.