Hydrotreating process and apparatus
US-9476000-B2 · Oct 25, 2016 · US
US2019382663A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019382663-A1 |
| Application number | US-201916549708-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 23, 2019 |
| Priority date | Nov 15, 2016 |
| Publication date | Dec 19, 2019 |
| Grant date | — |
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Systems and methods are provided for forming specialty products from hydrotreated FCC fractions. Optionally, the hydrotreated FCC fractions used for forming the specialty products can further include a (hydrotreated) portion of a steam cracker tar fraction. The specialty products that can be formed from hydrotreated FCC fractions include, but are not limited to, carbon blacks, resins, and carbon fibers. A convenient method for forming the hydrotreated FCC fractions can be fixed bed hydrotreatment.
Opening claim text (preview).
1 .- 11 . (canceled) 12 . A hydrotreated effluent comprising an 850° F.+ (454° C.+) fraction, the 850° F.+(454° C.+) fraction comprising at least about 50 wt % of polycyclic hydrocarbonaceous compounds, at least about 5 wt % aromatics, a content of aromatics different from naphthenoaromatics of about 1.0 wt % or less, and a content of naphthenoaromatics having 4 or more aromatic rings being about 1000 wppm or less, based on a weight of the 850° F.+ (454° C.+) fraction, wherein at least about 50 wt % of the polycyclic hydrocarbonaceous compounds comprise naphthenes based on a total weight of polycyclic hydrocarbonaceous compounds in the 850° F.+ (454° C.+) fraction. 13 . The hydrotreated effluent of claim 12 , wherein the 850° F.+ (454° C.+) fraction comprises at least about 60 wt % of polycyclic hydrocarbonaceous compounds. 14 . The hydrotreated effluent of claim 12 , wherein the 850° F.+ (454° C.+) fraction comprises at least about 50 wt % of polycyclic hydrocarbons. 15 . The hydrotreated effluent of claim 12 , wherein the content of aromatics different from naphthenoaromatics is about 1000 wppm or less. 16 . The hydrotreated effluent of claim 12 , wherein the hydrotreated effluent is formed by a process comprising hydrotreatment of a feed comprising at least 60 wt % of a catalytic slurry oil based on a weight of the feed, at least 10 wt % of a steam cracker tar based on a weight of the feed, or a combination thereof. 17 . A hydrotreated effluent fraction having a T10 boiling point of at least 510° C. and a T90 boiling point of 621° C. or less, the hydrotreated effluent fraction comprising, based on a weight of the hydrotreated effluent fraction, at least about 50 wt % of polycyclic hydrocarbonaceous compounds and about 0.1 wt % to about 5.0 wt % aromatics, a content of aromatics different from naphthenoaromatics of about 1.0 wt % or less, and a content of naphthenoaromatics having 4 or more aromatic rings of about 1000 wppm or less. 18 . The hydrotreated effluent fraction of claim 17 , wherein the hydrotreated effluent fraction comprises at least about 70 wt % polycyclic hydrocarbonaceous compounds based on the weight of the hydrotreated effluent fraction. 19 . The hydrotreated effluent fraction of claim 17 , wherein the hydrotreated effluent fraction comprises about 10 wt % of paraffins or less based on the weight of the hydrotreated effluent fraction. 20 . The hydrotreated effluent fraction of claim 12 , wherein the hydrotreated effluent fraction is formed by a process comprising hydrotreatment of a feed comprising at least 60 wt % of a catalytic slurry oil based on a weight of the feed, at least 10 wt % of a steam cracker tar based on a weight of the feed, or a combination thereof.
including at least one step of catalytic cracking in the absence of hydrogen · CPC title
Fractional distillation {or use of a fractionation or rectification column} · CPC title
Residues · CPC title
Apparatus for fixed bed hydrotreatment processes · CPC title
Aromatics · CPC title
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