发明名称 PRODUCTION OF RENEWABLE BIOFUELS
摘要 Renewable fuels are produced in commercial quantities and with enhanced efficiency by integrating a bio-oil production system with a conventional petroleum refinery so that the bio-oil is co-processed with a petroleum-derived stream in the refinery. The techniques used to integrate the bio-oil production system and conventional petroleum refineries are selected based on the quality of the bio-oil and the desired product slate from the refinery.
申请公布号 US2015044107(A1) 申请公布日期 2015.02.12
申请号 US201414521171 申请日期 2014.10.22
申请人 KiOR, Inc. 发明人 Ramirez Corredores Maria Magdalena;Iglesias Vicente Sanchez
分类号 C10L1/00 主分类号 C10L1/00
代理机构 代理人
主权项 1. A system for producing renewable fuels, said system comprising: a bio-oil production facility comprising a biomass conversion reactor for converting biomass into bio-oil; a petroleum refinery for refining petroleum products; and an integration system for combining at least a portion of said bio-oil from said bio-oil production facility with one or more petroleum-derived streams in said petroleum refinery for co-processing therewith, wherein said integration system comprises at least one of a first, second, third, fourth, fifth, and/or sixth integration mechanism for combining at least a portion of said bio-oil with at least one of said petroleum-derived streams, wherein said refinery comprises one or more of the following refining systems (i) through (vi) (i) a first hydrotreating unit and a first fractionator, wherein said first hydrotreating unit is located downstream of said first integration mechanism and said first fractionator is located downstream of said first hydrotreating unit;(ii) a second catalytic cracking unit and a second fractionator, wherein said second catalytic cracking unit is located downstream of said second integration mechanism and said second fractionator is located downstream of said second catalytic cracking unit;(iii) a third hydrotreating unit, a third catalytic cracking unit, and a third fractionator, wherein said third hydrotreating unit is located downstream of said third integration mechanism, wherein said third catalytic cracking unit is located downstream of said third hydrotreating unit, wherein said third fractionator is located downstream of said third catalytic cracking unit;(iv) a fourth hydrotreating unit, a fourth hydrocracking unit, and a fourth fractionator, wherein said fourth hydrotreating unit is located downstream of said fourth integration mechanism, wherein said fourth hydrocracking unit is located downstream of said fourth hydrotreating unit, wherein said fourth fractionator is located downstream of said fourth hydrocracking unit;(v) a fifth thermal cracking unit and a fifth fractionator, wherein said fifth thermal cracking unit is located downstream of said fifth integration mechanism and said fifth fractionator is located downstream of said fifth thermal cracking unit; and/or(vi) a sixth fractionator, a sixth thermal cracking unit, and a sixth hydrotreating unit, wherein said sixth fractionator is located downstream of said sixth integration mechanism, wherein said sixth thermal cracking unit is located downstream of said sixth fractionator, wherein said sixth hydrotreating unit is located downstream of said sixth fractionator.
地址 Pasadena TX US