发明名称 PROCESS FOR CONVERSION OF FEEDSTOCKS OBTAINED FROM RENEWABLE SOURCES BASED ON MARINE FUELS
摘要 The invention relates to a process for the production of diesel fuel bases comprising a sulfur content that is less than 100 ppm, starting from a feedstock that is obtained from a renewable source, comprising the following stages: a) A stage for bringing the feedstock into contact with a fixed-bed hydrotreatment catalyst for producing an effluent that comprises a gaseous fraction comprising hydrogen and a hydrocarbon-based liquid fraction,d) A stage for bringing into contact at least one portion of the hydrocarbon-based liquid fraction in the presence of a selective hydroisomerization catalyst in a fixed bed,e) A stage for separating the effluent that is obtained from stage d) into a gaseous fraction that comprises hydrogen and at least one diesel-fuel-based fraction.
申请公布号 US2014291200(A1) 申请公布日期 2014.10.02
申请号 US201314106889 申请日期 2013.12.16
申请人 IFP ENERGIES NOUVELLES 发明人 WEISS Wilfried;CHAPUS Thierry
分类号 C10G65/04 主分类号 C10G65/04
代理机构 代理人
主权项 1. Process for the production of diesel fuel bases comprising a sulfur content of less than 100 ppm, starting from a feedstock that is obtained from a renewable source, comprising the following stages: a) A stage for bringing the feedstock into contact with a fixed-bed hydrotreatment catalyst, at a temperature of between 200 and 450° C., at a pressure of between 1 MPa and 10 MPa, at an hourly volumetric flow rate of between 0.1 h−1 and 10 h−1 and in the presence of a total quantity of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is between 150 and 750 Nm3 of hydrogen/m3 of feedstock for producing an effluent that comprises a gaseous fraction comprising hydrogen and a hydrocarbon-based liquid fraction, d) A stage for bringing into contact at least one portion of the hydrocarbon-based liquid fraction in the presence of a selective hydroisomerization catalyst in a fixed bed, said catalyst comprising at least one group VIII metal and/or at least group VIB metal, said stage d) being carried out at a temperature of between 300 and 380° C., at a pressure of between 3 MPa and 7 MPa, at an hourly volumetric flow rate of between 0.5 and 5 h−1, and in the presence of a total quantity of hydrogen mixed with said hydrocarbon-based liquid fraction such that the hydrogen/hydrocarbon-based liquid fraction ratio is between 70 and 1,000 Nm3/m3, e) A stage for separating the effluent that is obtained from stage d) into a gaseous fraction that comprises hydrogen and at least one diesel-fuel-based fraction, and in which the hydrogen that is used in stage a) and/or in stage d) is obtained at least in part from the separated gaseous fraction of stage e).
地址 Rueil-Malmaison Cedex FR