Process and installation for the conversion of crude oil to petrochemicals having an improved propylene yield

Patent metadata

Field	Value
Publication number	US-10259758-B2
Application number	US-201816153268-A
Country	US
Kind code	B2
Filing date	Oct 5, 2018
Priority date	Jul 2, 2013
Publication date	Apr 16, 2019
Grant date	Apr 16, 2019

Abstract

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.

First claim

It is claimed:

1. 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 and an outlet for resid;
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 for receiving;
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 in the resid upgrading unit or the aromatic ring opening unit, said unit for olefin synthesis including an outlet for olefins produced in the olefins synthesis unit, and
a fluid catalytic cracking unit comprising an inlet for a part of the liquid resid upgrading effluent produced by aromatic ring opening and an outlet for middle-distillate produced by fluid catalytic cracking and olefins produced by fluid catalytic cracking;
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 by the fluid catalytic cracking unit.

2. The process installation according to claim 1 , wherein:
the crude distillation unit further comprises an outlet for gases fraction.

3. The process installation according to claim 2 , further comprising a gas separation unit comprising an inlet for gases produced in the integrated process, an outlet for ethane and an outlet for propane; an ethane cracker comprising an inlet for ethane and an outlet for ethylene; and a propane dehydrogenation unit comprising an inlet for propane and an outlet for propylene.

4. The process installation according to claim 2 , further comprising a butane cracker comprising an inlet for butane and an outlet for olefins and an outlet for BTX.

5. The process installation according to claim 1 , further comprising a butane cracker comprising an inlet for butane and an outlet for olefins and an outlet for BTX.

6. The process installation according to claim 3 , further comprising a butane cracker comprising an inlet for butane and an outlet for olefins and an outlet for BTX.

7. The process installation according to claim 4 , further comprising a gas separation unit comprising an inlet for the gases, an outlet for ethane and an outlet for propane;
an ethane cracker comprising an inlet for ethane and an outlet for ethylene; and
a propane dehydrogenation unit comprising an inlet for propane and an outlet for propylene.

Assignees

• Saudi Basic Ind Corp
• Sabic Global Technologies Bv

Inventors

• Ward Andrew Mark
• Narayanaswamy Ravichander
• Rajagopalan Vijayanand
• Oprins Arno Johannes Maria
• Schaerlaeckens Egidius Jacoba Maria
• Velasco Pelaez Raul

Classifications

• C10G69/06

  including at least one step of thermal cracking in the absence of hydrogen · CPC title

• C10G9/00

  Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils · CPC title

• C10G9/36

  with heated gases or vapours · CPC title

• C10G69/00

  Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process (C10G67/00 takes precedence) · CPC title

• C10G2400/20

  C2-C4 olefins · CPC title