PROCESS SCHEME FOR CATALYTIC PRODUCTION OF RENEWABLE HYDROGEN FROM OXYGENATE FEEDSTOCKS
摘要
A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200° C. to about 375° C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.
申请公布号
EP2964569(A4)
申请公布日期
2017.01.04
申请号
EP20130855695
申请日期
2013.11.11
申请人
Phillips 66 Company;Paul, Uchenna P.;Randolph, Bruce B.;Nelson, Jon M.;Fjare, Kristi A.;Smith, Danielle K.;Cragun, Mark Rumel;Sadok, Richard, D.
发明人
RANDOLPH, Bruce B.;FJARE, Kristi A.;SMITH, Danielle K.;CRAGUN, Mark Rumel;SADOK, Richard D.