Process for converting petroleum feedstocks comprising an ebullating-bed hydrocracking stage, a maturation stage and a stage of separating the sediments for the production of fuel oils with a low sediment content
US-9840674-B2 · Dec 12, 2017 · US
US10787401B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10787401-B2 |
| Application number | US-201916372156-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 1, 2019 |
| Priority date | Jul 2, 2013 |
| Publication date | Sep 29, 2020 |
| Grant date | Sep 29, 2020 |
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The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, aromatic ring opening, and olefins synthesis, which process comprises subjecting a hydrocarbon feed to aromatic ring opening to produce LPG and subjecting the LPG produced in the integrated process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising a crude distillation unit comprising an inlet for crude oil and at least one outlet for kerosene and/or gasoil; an aromatic ring opening unit comprising an inlet for a hydrocarbon feed to aromatic ring opening and an outlet for LPG; and a unit for the olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocarbon feed subjected to aromatic ring opening comprises kerosene and/or gasoil produced by crude oil distillation in the process; and refinery unit-derived middle-distillate produced in the process. The process and the process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved propylene yield.
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It is claimed: 1. An integrated petrochemical process installation to convert crude oil into petrochemical products comprising: a crude distillation unit comprising an inlet for crude oil and at least one outlet for kerosene and/or gasoil; an aromatic ring opening unit comprising an inlet for a hydrocarbon feed to aromatic ring opening and an outlet for LPG; and a unit for olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins, wherein said hydrocarbon feed to aromatic ring opening comprises: kerosene and/or gasoil produced by the crude oil distillation unit; and refinery unit-derived middle-distillate produced in the integrated petrochemical process installation; a fluid catalytic cracking unit comprising an inlet for a part of the liquid resid upgrading effluent and light-distillate produced by aromatic ring opening and an outlet for middle-distillate produced by fluid catalytic cracking and olefins produced by fluid catalytic cracking; wherein the crude distillation unit comprises an outlet for gases fraction, an outlet for resid and at least one outlet for kerosene and/or and gasoil; and a resid upgrading unit comprising an inlet for resid and refinery unit-derived heavy-distillate, an outlet for LPG produced by resid upgrading and outlet for liquid resid upgrading effluent.
to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins (C10G32/00 takes precedence; improving or increasing the octane number or aromatic content of naphtha C10G35/00) · CPC title
C2-C4 olefins · CPC title
plural serial stages only · CPC title
including at least one step of catalytic cracking in the absence of hydrogen · CPC title
Distillation of hydrocarbon oils · CPC title
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