Patent ID: 11939541
Assignee: SAUDI ARABIAN OIL COMPANY
Field: Basic materials chemistry (Chemistry)
Classification: CPC C | IPC C

Claim 10:
11. The process of claim 8, wherein:
the solvent deasphalting unit is operated at a temperature of from 60° C. to 90° C. and a pressure of from 0.1 MPa to 0.4 MPa;
the delayed coker is operated at a temperature of from 450° C. to 600° C. and a pressure of from 0.1 MP a to 0.4 MP a;
the hydrotreating zone is operated at a temperature of from 370° C. to 500° C. and a pressure of from 0.1 MP a to 0.2 MP a;
the steam enhanced catalytic cracking system is operated at a temperature of from 525° C. to 750° C. and a pressure of from 0.1 MPa to 0.2 MPa;
the methane cracking zone is operated at a temperature of from 850° C. to 1200° C. and a pressure of from 0.1 MPa to 0.2 MPa;
the steam cracking zone is operated at a temperature of from 800° C. to 950° C. and a pressure of from 0.1 MPa to 0.2 MPa;
the catalytic reformer is operated at a temperature of from 450° C. to 600° C. and a pressure of from 0.7 MP a to 7 MP a; and
the transalkylation unit is operated at a temperature of from 350° C. to 450° C. and a pressure of from 1 MPa to 5 MPa.