Premium coking process

• US 4,720,338 A
• Filed: 11/03/1986
• Issued: 01/19/1988
• Est. Priority Date: 11/03/1986
• Status: Expired due to Term

• Current Assignee: Conoco Incorporated (ConocoPhillips)
• Original Assignee: Conoco Incorporated (ConocoPhillips)
• Inventors: Shigley, John K., Newman, Bruce A., Fu, Ta-Wei
• Primary Examiner(s): Doll, John
• Assistant Examiner(s): Caldarola, Glenn A.
• Application Number:
  US06/926,039
• Time in Patent Office: 442 Days
• Field of Search: 208/131, 208/50
• US Class Current: 208/131
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: C10B 57/045 containing mineral oils, bitumen, tar or the like or mixtures thereof

Abstract

A process for providing more uniform premium coke in a delayed coking operation by adding an aliphatic petroleum fraction to the premium coking feed during the latter part of the coking cycle. Preferably the aliphatic petroleum fraction is added gradually and is increased in quantity over the period of addition.

Claims

1. In a delayed premium coking process in which an aromatic mineral oil feedstock having an f_a of at least about 40 and selected from the group consisting of decant oil, gas oil, thermal tar and extracted coal tar pitch is combined with conventional recycle and coked at premium coking conditions, the improvement comprising adding to said feedstock and natural recycle during about the latter half of the fill cycle an aliphatic petroleum residual oil fraction having an f_a below about 25 and a Richfield pentane insolubles content of less than 15 weight percent whereby the coke formed during the latter part of the fill cycle will have a CTE value more near that of the coke formed during the initial part of the fill cycle than would be the case if the aliphatic material were not added.

2. The process of claim 1 in which the total amount of aliphatic petroleum fraction added during the coking cycle is between about 15 weight percent and about 70 weight percent of the combined mixture of aliphatic petroleum fraction and the aromatic mineral oil feedstock.

3. The process of claim 2 in which the amount of aliphatic petroleum fraction added is gradually increased to reach a maximum at the end of the coking cycle.

4. The process of claim 3 in which the amount of aliphatic petroleum fraction initially added is between about 5.0 weight percent and about 50.0 weight percent of the combined mixture of aliphatic petroleum fraction and the aromatic mineral oil feedstock and the amount added by the end of the coking cycle is between about 50.0 weight percent and about 95.0 weight percent.

5. The process of claim 4 in which the aromatic mineral oil feedstock is a thermal tar.

6. The process of claim 5 in which the aliphatic petroleum fraction is a residual oil.