Framework-Substituted Zeolite Catalyst for FCC Product Selectivity

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Solution Overview

Problem

The fluidized catalytic cracking (FCC) industry faces challenges in reducing the production of dry gas and coke while maximizing the production of gasoline and light olefins, as existing catalysts do not effectively balance these outcomes.

Innovation Solution

A catalyst comprising a framework-substituted ultra-stable Y-type zeolite with zirconium and/or hafnium atoms substituted for aluminum atoms, along with optional titanium substitution, is used to enhance cracking activity and reduce dry gas and coke production, characterized by specific crystal lattice constants, surface areas, and silica-alumina ratios.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional FCC catalysts are used, then cracking activity is maintained, but production of dry gas and coke increases

Engineering Contradiction:
Improvegasoline and light olefins productionVSAvoiddry gas and coke production
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by substituting aluminum atoms in the zeolite framework with zirconium and/or hafnium atoms. This atomic substitution modifies the chemical and physical parameters of the catalyst, including acid site density, pore structure, and thermal stability, thereby improving selectivity toward gasoline and light olefins while reducing dry gas and coke formation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite materials by creating a framework-substituted zeolite that combines multiple elements (aluminum, zirconium, hafnium, and optionally titanium) within the zeolite structure. This composite approach at the atomic level generates synergistic effects that enhance cracking activity for desired products while suppressing harmful byproducts

Inventive Principle:
Principle #40Composite materials

2Productivity

If framework-substituted ultra-stable Y-type zeolite with zirconium and/or hafnium substitution is used, then gasoline and light olefins production increases, but catalyst complexity increases

Engineering Contradiction:
Improvegasoline and light olefins productionVSAvoidcatalyst composition complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent applies local quality by introducing zirconium and/or hafnium atoms at specific locations within the zeolite framework rather than uniformly throughout. This localized substitution at atomic sites creates specific active centers that enhance gasoline and light olefins production while maintaining overall catalyst simplicity and avoiding excessive complexity

Inventive Principle:
Principle #3Local quality

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The catalyst effectively increases the production of gasoline and light olefins while minimizing dry gas and coke formation, optimizing the product slate in FCC processes.

Implementation Method 1

a catalyst for fluidized catalytic cracking of hydrocarbon oil including as a support, the zeolite in which a part of aluminum atoms constituting the zeolite framework is replaced with zirconium atoms and/or hafnium atoms

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10357761B2Catalyst for fluidized catalytic cracking and method for fluidized catalytic cracking
Publication Date: 2019.07.23 JAPAN COOP CENT FOR PETROLEUM & SUSTAINABLE ENERGY
  • US10357761B2 patent drawing
  • US10357761B2 patent drawing

AI summary

The present invention relates to a catalyst for fluidized catalytic cracking of hydrocarbon oil containing a framework-substituted zeolite-1 in which zirconium atoms and/or hafnium atoms form a part of a framework of an ultra-stable Y-type zeolite.