Processing vacuum residuum and vacuum gas oil in ebullated bed reactor systems

Patent metadata

Field	Value
Publication number	US-10894922-B2
Application number	US-201916263956-A
Country	US
Kind code	B2
Filing date	Jan 31, 2019
Priority date	Feb 12, 2014
Publication date	Jan 19, 2021
Grant date	Jan 19, 2021

Abstract

A process for upgrading vacuum residuum and vacuum gas oil hydrocarbons is disclosed. The process may include: contacting a heavy distillate hydrocarbon fraction and hydrogen with a zeolite selective hydrocracking catalyst in a first ebullated bed hydrocracking reaction zone to convert at least a portion of the vacuum gas oil to lighter hydrocarbons. Contacting a residuum hydrocarbon fraction and hydrogen with a non-zeolite base metal hydroconversion catalyst in a second ebullated bed hydroconversion reaction zone may produce a vapor stream containing unconverted hydrogen, acid gases and volatilized hydrocarbons which may be fed along with the vacuum gas oil in the first ebullated bed hydrocracking zone.

First claim

What is claimed:

1. A system for upgrading residuum hydrocarbons and heavy distillate feedstocks, the system comprising:
an ebullated bed hydroconversion reactor system configured to contact residuum hydrocarbons and hydrogen with a non-zeolitic base metal hydroconversion catalyst to produce a first effluent,
a first separation unit configured to separate the first effluent to recover a first liquid product and a first vapor product;
an absorption tower configured to concurrently contact counter-currently the first vapor product with a hydrocarbon stream, and produce a second vapor product and a second liquid product, wherein the second vapor product is lean in middle distillate content and comprises gasoil range hydrocarbon;
a first flowline configured to feed the first vapor product to the absorption tower;
an ebullated bed hydrocracking reactor system configured to contact the second vapor product and a heavy distillate feedstock with a zeolitic selective hydrocracking catalyst to produce a second effluent;
a second flowline configured to feed the second vapor product to the ebullated bed hydrocracking reactor system; and
a third separation unit configured to separate the second effluent and recover one or more hydrocarbon fractions.

2. The system of claim 1 , further comprising a heat exchange unit configured to heat residuum hydrocarbons and hydrogen prior to contact with the non-zeolitic base metal hydroconversion catalyst.

3. The system of claim 1 , wherein the residuum hydrocarbons are selected from the group consisting of petroleum crudes, shale oils, tar sands bitumen, coal-derived oils, tall oils, black oils, organic wastes, biomass-derived liquids, and mixtures thereof.

4. The system of claim 1 , wherein the heavy distillate feedstock is selected from the group consisting of atmospheric gas oil, light vacuum gas oil, heavy vacuum gas oil, virgin vacuum gas oil, or heavy coker gas oil, FCC cycle oil, and deasphalted oil, and mixtures thereof, wherein the heavy distillate feedstock is derivable from petroleum, bitumen, kerogen, biomass, or organic waste sources.

5. The system of claim 4 , wherein the residuum hydrocarbons are derived from a crude, and wherein the heavy distillate feedstock is a virgin vacuum gas oil topped off of the crude.

6. The system of claim 1 , wherein the residuum hydrocarbons comprise at least one of petroleum atmospheric or vacuum residua, deasphalted oils, deasphalter pitch, hydrocracked atmospheric tower or vacuum tower bottoms, fluid catalytically cracked (FCC) slurry oils, residuum derived from shale-derived oils, coal-derived oils, bio-derived crude oils, tar sands bitumen, tall oils, and black oils.

7. The system of claim 1 , wherein the zeolitic selective hydrocracking catalyst has a substrate consisting essentially of at least one of H Y-zeolite, H ZSM-5, mordenite, erionite or ultrastable faujasite, USY zeolite, Beta zeolite, ZSM-11, ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, ZSM-34, REY molecular sieve, or REHY molecular sieve.

8. The system of claim 7 , wherein the zeolitic selective hydrocracking catalyst further comprises one or more of cobalt, molybdenum, tungsten, nickel, platinum, or palladium.

9. The system of claim 1 , wherein the zeolitic selective hydrocracking catalyst is manufactured to be fluidizable and have high attrition resistance under the reaction conditions in the ebullated bed hydrocracking reactor system.

10. The system of claim 9 , wherein the zeolitic selective hydrocracking catalyst is comprised of a noble metal incorporated onto a zeolitic support.

Assignees

• Lummus Technology Inc

Inventors

• Arora Arun
• Greene Marvin I

Classifications

• C10G65/12 Primary

  including cracking steps and other hydrotreatment steps · CPC title

• C10G65/10

  including only cracking steps · CPC title

• C10G65/02

  plural serial stages only · CPC title

• C10G49/16

  according to the "fluidised-bed" technique · CPC title

• C10G49/10

  with moving solid particles · CPC title