公开(公告)号：US20160068390A1

公开(公告)日：2016-03-10

申请号：US14653482

申请日：2013-12-13

Applicant: BASF SE ,  LINDE AG ,  THYSSENKRUPP INDUSTRIAL SOLUTIONS AG

Inventor： Christian SCHNEIDER ,  Andreas BODE ,  Dirk KLINGLER ,  Otto MACHHAMMER ,  Philipp BRUEGGEMANN ,  Matthias KERN ,  Wolfgang Alois HORMUTH ,  Marcus GUZMANN ,  Rene KOENIG ,  Jens BERNNAT ,  Grigorios KOLIOS ,  Volker GOEKE ,  Hans-Juergen MAASS ,  Karsten BUEKER

IPC: C01B3/34

CPC classification number: C01B3/344 ,  C01B2203/0222 ,  C01B2203/0238 ,  C01B2203/0244 ,  C01B2203/06 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0855 ,  C01B2203/0861 ,  C01B2203/0883 ,  C01B2203/1235

Abstract: The invention relates to a process for utilizing a hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas, wherein hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas is introduced into a reaction space and the multicomponent mixture comprised in the coproduct gas, accompanying gas and/or biogas is converted in a high-temperature zone at temperatures of more than 1000° C. and in the presence of a carrier into a product gas mixture which comprises more than 95% by volume of CO, CO2, H2, H2O, CH4 and N2 and optionally into a carbon-comprising solid which is deposited to an extent of at least 75% by weight, based on the total mass of the carbon-comprising solid, on the carrier where the flow velocity of the gas mixture of coproduct gas, accompanying gas and/or biogas in the reaction zone is less than 20 m/s.

Abstract translation: 本发明涉及一种利用含烃和/或二氧化碳的副产物气体，伴随的气体和/或生物气体的方法，其中含烃和/或二氧化碳的副产物气体，伴随的气体和/或生物气体是 引入到反应空间中，包含在副产气体中的伴随气体和/或生物气体的多组分混合物在高于1000℃的温度的高温区域中并且在载体存在下转化成产物气体混合物 其包含超过95体积％的CO，CO 2，H 2，H 2 O，CH 4和N 2，并任选地加入到基于碳的总质量至少75重量％的程度沉积的含碳固体 在载体上，反应区中副产物气体，伴随气体和/或生物气体的气体混合物的流速小于20m / s。

公开(公告)号：US20170275161A1

公开(公告)日：2017-09-28

申请号：US15504982

申请日：2015-08-13

Applicant: BASF SE

Inventor： Otto MACHHAMMER ,  Grigorios KOLIOS ,  Andreas Bode ,  Hans-Juergen MAASS

IPC: C01B3/28 ,  C01B5/00

CPC classification number: C01B3/28 ,  C01B3/24 ,  C01B5/00 ,  C01B31/18 ,  C01B32/40 ,  C01B2203/0216 ,  C01B2203/0222 ,  C01B2203/0238 ,  C01B2203/0272 ,  C01B2203/0838 ,  C01B2203/1235 ,  Y02P20/13 ,  Y02P20/142

Abstract: The invention relates to a process for producing synthesis gas (5) in which hydrocarbon (2) is decomposed thermally in, a first reaction zone (11) to hydrogen and carbon, and hydrogen formed is passed from the first reaction zone (Z1) into a second action zone (Z2) in order to be reacted therein with carbon dioxide (4) to give water and carbon monoxide. The characteristic feature here is that energy required for the thermal decomposition of the hydrocarbon is supplied to the first reaction zone (Z1) from the second reaction zone (Z2).