Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications

Patent metadata

Field	Value
Publication number	US-2020376456-A1
Application number	US-202016996548-A
Country	US
Kind code	A1
Filing date	Aug 18, 2020
Priority date	Sep 16, 2016
Publication date	Dec 3, 2020
Grant date	—

Abstract

Apparatus and processes herein provide for converting hydrocarbon feeds to light olefins and other hydrocarbons. The processes and apparatus include, in some embodiments, feeding a hydrocarbon, a first catalyst and a second catalyst to a reactor, wherein the first catalyst has a smaller average particle size and is less dense than the second catalyst. A first portion of the second catalyst may be recovered as a bottoms product from the reactor, and a cracked hydrocarbon effluent, a second portion of the second catalyst, and the first catalyst may be recovered as an overhead product from the reactor. The second portion of the second catalyst may be separated from the overhead product, providing a first stream comprising the first catalyst and the hydrocarbon effluent and a second stream comprising the separated second catalyst, allowing return of the separated second catalyst in the second stream to the reactor.

First claim

What is claimed:

1 . A system for cracking hydrocarbons, comprising:
a regenerator; a riser reactor configured to:
receive a mixture of first particles and second particles from the regenerator, wherein the first particles have a smaller average particle size and/or are less dense than the second particles, and wherein the first particles and second particles may independently be catalytic or non-catalytic particles;
contact a hydrocarbon fraction with the mixture of first particles and second particles to convert at least a portion of the hydrocarbon fraction; and
produce an overhead product from the riser reactor comprising the converted hydrocarbon fraction, the second particles, and the first particles;
an integrated disengagement vessel configured to receive the overhead product, the integrated disengagement vessel comprising:
a housing;
a solids separation device disposed within the housing for separating the second particles from the overhead product to provide a first stream, comprising the first particles and the carrier fluid and/or a reaction product of the carrier fluid, and a second stream, comprising the separated second particles;
one or more cyclones disposed within the housing for separating the first stream to recover a solids fraction, comprising the first particles, and a vapor fraction, comprising the carrier fluid and/or a reaction product of the carrier fluid;
an internal vessel disposed within the housing for receiving the second stream comprising the separated second particles;
an annular region between the housing and the internal vessel for receiving the solids fraction comprising the first particles;
a vapor outlet for recovering the vapor fraction;
a flow line for feeding the solids fraction from the annular region to the regenerator; and a flow line for enhancing a concentration of the second particles within the riser reactor by feeding the separated second particles from the internal vessel to the riser reactor, wherein the separated second particles are mixed with the mixture of first particles and second particles from the regenerator.

2 . The system of claim 1 , further comprising:
a second reactor configure to receive a second hydrocarbon feedstock and a mixture of first particles and second particles from the regenerator, wherein the mixture of first and second particles is contacted with a second hydrocarbon feedstock to crack the second hydrocarbon feedstock and form a second reactor effluent comprising lighter hydrocarbons and a mixture of first and second particles; a separator configured to receive the second reactor effluent and to separate the first and second particles from the lighter hydrocarbons and the converted hydrocarbon effluent.

3 . The system of claim 1 , further comprising:
a flow line for feeding fresh second particles to the riser reactor; and a flow line for feeding fresh first particles to the regenerator.

4 . The system of claim 1 , further comprising:
a fractionation system configured for receiving both the vapor fraction recovered via the vapor outlet and the hydrocarbon product recovered from the separator and for separating the hydrocarbon products therein into two or more hydrocarbon fractions including a naphtha fraction; and a flow line for feeding the naphtha fraction to the riser reactor as the hydrocarbon feedstock.

5 . The system of claim 1 , further comprising a controller configured to adjust a vapor split ratio in the solids separation device to carry over a portion of the second catalyst in the first stream.

6 . An integrated disengagement vessel comprising:
a housing; a solids separation device disposed within the housing for separating a hydrocarbon stream comprising a hydrocarbon fraction, a second particles, and a first particles into a first stream, comprising the first particles and the hydrocarbon fraction, and a second stream, comprising the separated second particles; one or more cyclones disposed within the housing for separating the first stream to recover a solids fraction, comprising the first particles, and a vapor fraction, comprising the hydrocarbon fraction; an internal vessel disposed within the housing for receiving the second stream comprising the separated second particles; an annular region between the housing and the internal vessel for receiving the solids fraction comprising the first particles; a vapor outlet for recovering the vapor fraction.

7 . The system of claim 6 , further comprising a flow line for feeding the solids fraction from the annular region to a regenerator.

8 . The system of claim 6 , further comprising:
a fractionation system configured for receiving the vapor fraction and separating the hydrocarbon fraction therein into two or more hydrocarbon streams including a naphtha fraction; and a flow line for feeding the naphtha fraction to a riser reactor as a hydrocarbon feedstock.

Assignees

• Lummus Technology Inc

Inventors

• Chen Liang
• Loezos Peter
• Marri Rama Rao
• Tomsula Bryan
• Hood Jon A
• Singh Hardik
• Dorsey Michael
• Breckenridge Justin

Classifications

• C10G2300/1044

  Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title

• C10G11/182 Primary

  Regeneration · CPC title

• B01J8/0055

  using cyclones · CPC title

• B01J2208/00991

  Disengagement zone in fluidised-bed reactors · CPC title

• B01J8/26

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title