发明名称 Upgrading hydrocarbon pyrolysis products
摘要 The invention relates to a process for upgrading pyrolysis tar, such as steam cracker tar, in the presence of a utility fluid. The utility fluid contains 2-ring and/or 3-ring aromatics and has solubility blending number (SBN)≧120. The invention also relates to the upgraded pyrolysis tar and to the use of the upgraded pyrolysis tar, for example, for fuel oil blending.
申请公布号 US9637694(B2) 申请公布日期 2017.05.02
申请号 US201514683482 申请日期 2015.04.10
申请人 ExxonMobil Chemical Patents Inc. 发明人 Evans Christopher M.;Soultanidis Nikolaos;Koc-Karabocek Reyyan;Ferrughelli David T.;Xu Teng
分类号 C10G69/06;C10G9/36;C10G69/00 主分类号 C10G69/06
代理机构 代理人
主权项 1. A hydrocarbon conversion process, comprising: (a) providing a pyrolysis feedstock comprising ≧10.0 wt. % hydrocarbon based on the weight of the pyrolysis feedstock; (b) pyrolysing the pyrolysis feedstock to produce a pyrolysis effluent comprising pyrolysis tar and ≧1.0 wt. % of C2 unsaturates, based on the weight of the pyrolysis effluent; (c) separating at least a portion of the pyrolysis tar from the pyrolysis effluent, wherein the separated pyrolysis tar has IN>110 and ≧90 wt. % of the pyrolysis effluent's molecules have an atmospheric boiling point of ≧290° C.; (d) providing a utility fluid, the utility fluid comprising ring aromatics, in an amount ≧25.0 wt. % based on the weight of the utility fluid, and the utility fluid having SBN≧120; (e) combining at least a portion of the separated pyrolysis tar and utility fluid; (f) providing treat gas comprising molecular hydrogen; (g) hydroprocessing the combined pyrolysis tar and utility fluid in a hydroprocessing zone in the presence of treat gas under catalytic hydroprocessing conditions to produce hydroprocessed effluent, comprising hydroprocessed tar; (h) separating from the hydroprocessed effluent a bottoms stream and a first vapor stream; (i) separating from the first vapor stream a mid-cut stream and a second vapor stream; (j) separating from the second vapor stream a light liquid overhead stream and a total vapor product; (k) combining at least a portion of the mid-cut stream with at least a portion of the bottoms stream to form a heavy mid-cut stream, the heavy mid-cut stream having SBN≧120; and (l) conducting at least a portion of the heavy mid-cut stream to step (d), wherein the utility fluid comprises ≧10.0 wt. % of the heavy mid-cut stream, based on the weight of the utility fluid.
地址 Baytown TX US