Systems and methods for external processing of flash zone gas oil from a delayed coking process

• US 10,443,003 B2
• Filed: 02/24/2017
• Issued: 10/15/2019
• Est. Priority Date: 03/15/2013
• Status: Active Grant

• Current Assignee: Bechtel Hydrocarbon Technology Solutions, Inc. (Bechtel Group Incorporated)
• Original Assignee: Bechtel Hydrocarbon Technology Solutions, Inc. (Bechtel Group Incorporated)
• Inventors: Earhart, Jr., Robert F
• Primary Examiner(s): Leung, Jennifer A
• Application Number:
  US15/441,861
• Publication Number:
  US 20170204341A1
• Time in Patent Office: 963 Days
• CPC Class Codes: C10G 2300/1077 Vacuum residues
• CPC Class Codes: C10G 47/00 Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06
• CPC Class Codes: C10G 69/06 including at least one step of thermal cracking in the absence of hydrogen
• CPC Class Codes: C10G 9/005 Coking (in order to produce liquid products mainly)

Abstract

Systems and methods for the external processing flash zone gas oil by recycling it through a vacuum residuum hydroprocessing unit before reentering the delayed coking process.

Claims

1. A system for external processing of flash zone gas oil from a delayed coking process, which comprises:

a vacuum residuum hydroprocessing unit for converting the flash zone gas oil by one of ebullated bed hydrocracking and dispersed catalyst hydrocracking;

a delayed coking process system for producing the flash zone gas oil;

a flash zone gas oil line in fluid communication between the vacuum residuum hydroprocessing unit and the delayed coking process system configured for carrying hydroprocessing unit; and

a feed line directly connecting the vacuum residuum hydroprocessing unit and a fractionator in the delayed coking process system.

2. The system of claim 1, wherein at least 65% of the flash zone gas oil is converted by the vacuum residuum hydroprocessing unit to lighter hydrocarbons.

3. The system of claim 2, wherein the lighter hydrocarbons comprise at least one of gas, naphtha, light gas oil and heavy gas oil.

4. The system of claim 1, wherein the flash zone gas oil line carries only unfiltered flash zone gas oil directly from the delayed coking process system to the vacuum residuum hydroprocessing unit.

5. A method for external processing of flash zone gas oil from a delayed coking process, which comprises:

producing flash zone gas oil from a delayed coking process system;

carrying only the flash zone gas oil from the delayed coking process system to a vacuum residuum hydroprocessing unit; and

converting the flash zone gas oil in the vacuum residuum hydroprocessing unit by one of ebullated bed hydrocracking and dispersed catalyst hydrocracking.

6. The method of claim 5, further comprising carrying a vacuum residuum feed comprising unconverted flash zone gas oil from the vacuum residuum hydroprocessing unit to the delayed coking process system.

7. The method of claim 6, wherein at least 65% of the flash zone gas oil is converted by the vacuum residuum hydroprocessing unit to lighter hydrocarbons.

8. The method of claim 7, wherein the lighter hydrocarbons comprise at least one of gas, naphtha, light gas oil and heavy gas oil.