发明名称 Process for the production of pitch
摘要 Pitch is obtained, in a reactor configured for the atmospheric process, from a feedstock of oil hydrocarbons consisting of a feedstock of decanted oil. In the process, the feedstock is subjected to heating stages in reflux and distillation conditions with removal of volatile products generated, wherein the gaseous products are eliminated at each stage and the successively generated residual products comprise a final residue recovered as a predominantly isotropic pitch.
申请公布号 US9243187(B2) 申请公布日期 2016.01.26
申请号 US201114110045 申请日期 2011.05.27
申请人 PETROLEO BRASILEIRO S.A.—PETROBRAS 发明人 Depine de Castro Luiz;Monteiro de Castro Dutra Carlos Henrique;Ferraz de Souza Wladimir
分类号 C10C3/06;C10C1/16;C10G31/06;C10G7/00 主分类号 C10C3/06
代理机构 Sughrue Mion, PLLC 代理人 Sughrue Mion, PLLC
主权项 1. Process for the production of pitch, comprising the following steps at atmospheric pressure: a) preheating of a feedstock up to a initial reaction temperature; b) continuous and uniform heating, in conditions of a first reflux at an initial reaction temperature of between 300° C. and 370° C., for a time sufficient to promote reactions between hydrocarbon components, in a homogeneous liquid phase, generating: gaseous products that are eliminated and residual products in the reaction conditions; c) distillation of the residual products generated in stage b) up to a maximum temperature between 380° C. and 450° C., generating: residual products, gaseous products that are eliminated, and volatile products that are removed by condensation in the proportion between 5% and 60% by weight in relation to the feedstock; d) continuous and uniform heating of the residual products generated in the preceding distillation stage in reflux conditions at a temperature between 5° C. and 50° C. below the maximum temperature of the distillation, for a time between 1 and 60 times less than that of the heating in stage b), to promote reactions, generating: gaseous products that are removed and residual products in the reaction conditions; e) distillation of the residual products generated in stage d) up to a maximum temperature between 390° C. and 485° C., generating: gaseous products that are eliminated, volatile products that are removed by condensation, and residual products; f) sequential repetition of the two preceding stages, d) and e), to obtain residual products comprising pitch with a yield in relation to the feedstock between 30% and 60% by weight; and g) recovery of the pitch under refrigeration to specify a predominantly isotropic end product; wherein steps a)-g) occur at atmospheric pressure.
地址 Rio de Janeiro BR