Process and apparatus for contacting feed and catalyst with improved catalyst mixing

Patent metadata

Field	Value
Publication number	US-11794159-B2
Application number	US-202117553717-A
Country	US
Kind code	B2
Filing date	Dec 16, 2021
Priority date	Dec 16, 2021
Publication date	Oct 24, 2023
Grant date	Oct 24, 2023

Abstract

A process and reactor for contacting a feed stream with a catalyst stream comprises a reaction chamber comprising two spent catalyst inlets for delivering two spent catalyst streams to the reaction chamber and at least one regenerated catalyst inlet for delivering a regenerated catalyst stream to the reaction chamber. The reaction chamber may also include a second regenerated catalyst inlet for delivering a second regenerated catalyst stream to the reaction chamber. The second spent catalyst inlet enables thorough mixing of catalyst streams.

First claim

The invention claimed is:

1. A process for contacting a feed stream with fluidized catalyst comprising:
charging said feed stream to a reactor;
feeding a first spent catalyst stream to said reactor and feeding a second spent catalyst stream to said reactor;
feeding a first regenerated catalyst stream to said reactor;
contacting said feed stream with the first spent catalyst stream, the second spent catalyst stream and the first regenerated catalyst stream to produce a product gas stream and spent catalyst; and
separating said product gas stream from said spent catalyst,
wherein a spent angle between a first longitudinal axis of a first spent catalyst inlet and a second longitudinal axis of a second spent catalyst inlet is between about 105 and about 135 degrees.

2. The process of claim 1 further comprising recycling said first spent catalyst stream and said second spent catalyst stream from said spent catalyst.

3. The process of claim 1 further comprising feeding a second regenerated catalyst stream to said reactor.

4. The process of claim 1 further comprising feeding the second spent catalyst stream to said reactor in opposition to the first regenerated catalyst stream.

5. The process of claim 3 further comprising feeding the first spent catalyst stream to said reactor in opposition to the second regenerated catalyst stream.

6. The process of claim 3 wherein the first spent catalyst stream is fed to the reactor at a first spent vector and the second spent catalyst stream is fed to the reactor at a second spent vector that defines a spent angle with the first spent vector and the first regenerated catalyst stream is fed to the reactor at a first regenerated vector and the second regenerated catalyst stream is fed to the reactor at a second regenerated vector that defines a regenerated angle with the first regenerated vector and the spent angle is greater than the regenerated angle.

7. The process of claim 3 wherein the first spent catalyst stream is fed to said reactor through a first spent catalyst pipe; the first spent catalyst stream, the second spent catalyst stream, the first regenerated catalyst stream and the second regenerated catalyst stream mix and at one spent catalyst pipe diameter of the first spent catalyst pipe above all catalyst inlets the temperature differential among catalyst in a cross section is no more than 20° C.

8. A process for contacting a feed stream with fluidized catalyst comprising:
charging said feed stream to a reactor;
feeding a first spent catalyst stream to said reactor through a spent catalyst pipe having a first spent catalyst pipe diameter;
feeding a first regenerated catalyst stream to said reactor;
feeding a second spent catalyst stream or a second regenerated catalyst stream to said reactor:
mixing the first spent catalyst stream, the first regenerated catalyst stream, and the second spent catalyst stream or the second regenerated catalyst stream such that at one of said spent catalyst pipe diameter above all catalyst inlets the temperature differential among catalyst in a cross section is no more than 20° C.;
contacting said feed stream with a mixture of the first spent catalyst stream the first regenerated catalyst stream, and the second spent catalyst stream or the second regenerated catalyst stream to produce a product gas stream and spent catalyst; and
separating said product gas stream from said spent catalyst.

9. The process of claim 8 further comprising feeding a second spent catalyst stream to said reactor and feeding a second regenerated catalyst stream to said reactor.

10. A process for contacting a feed stream with fluidized catalyst comprising:
charging said feed stream to a reactor;
feeding a first spent catalyst stream to said reactor;
feeding a first regenerated catalyst stream to said reactor;
feeding a second spent catalyst stream or a second regenerated catalyst stream to said reactor;
contacting said feed stream with the first spent catalyst stream, the second spent catalyst stream, the first regenerated catalyst stream and the second regenerated catalyst stream to produce a product gas stream and spent catalyst; and
separating said product gas stream from said spent catalyst,
wherein a spent angle between a first longitudinal axis of a first spent catalyst inlet and a second longitudinal axis of a second spent catalyst inlet is greater than a regenerated angle between a first regenerated longitudinal axis of a first regenerated catalyst inlet and a second regenerated longitudinal axis of a second regenerated catalyst inlet.

Assignees

• Uop Llc

Inventors

• Johnson Ii Richard A
• Spieker Wolfgang A
• Mostofi-Ashtiani Mohammad-Reza

Classifications

• B01J8/0095 Primary

  in which two different types of particles react with each other · CPC title

• B01J8/005

  Separating solid material from the gas/liquid stream (separation processes per se B01D) · CPC title

• B01J8/0025

  by an ascending fluid · CPC title

• B01J8/1872 Primary

  Details of the fluidised bed reactor (B01J8/1836 takes precedence) · CPC title

• B01J8/32

  with introduction into the fluidised bed of more than one kind of moving particles · CPC title