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US Patent 11214741 Fluid catalytic cracking process for cracking multiple feedstocks

Patent 11214741 was granted and assigned to Honeywell UOP on January, 2022 by the United States Patent and Trademark Office.

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Contents

Is a
Patent
Patent

Patent attributes

Patent Applicant
Honeywell UOP
Honeywell UOP
Current Assignee
Honeywell UOP
Honeywell UOP
Patent Jurisdiction
United States Patent and Trademark Office
United States Patent and Trademark Office
Patent Number
11214741
Date of Patent
January 4, 2022
Patent Application Number
16801019
Date Filed
February 25, 2020
Patent Citations Received
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US Patent 12018216 Methods and systems for enhancing processing of hydrocarbons in a fluid catalytic cracking unit using plastic
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US Patent 11692141 Methods and systems for enhancing processing of hydrocarbons in a fluid catalytic cracking unit using a renewable additive
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US Patent 11802257 Systems and methods for reducing rendered fats pour point
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US Patent 11860069 Methods and assemblies for determining and using standardized spectral responses for calibration of spectroscopic analyzers
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US Patent 11885739 Methods and assemblies for determining and using standardized spectral responses for calibration of spectroscopic analyzers
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...
Patent Primary Examiner
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Renee Robinson
Patent abstract

A fluid catalytic cracking (FCC) process for cracking multiple feedstocks in a FCC apparatus comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips is provided. A first feed is injected into the riser from first distributor tips. A second feed is injected into the riser from second distributor tips. The first distributor tips and the second distributor tips are positioned at different radii in the riser. The first feed and the second feed are cracked in the riser in the presence of an FCC catalyst to provide a cracked effluent stream. The first distributor tips and the second distributor tips are located into a region of lower catalyst density and a region of higher catalyst density respectively in the riser.

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