Modified ZSM-5 Catalyst for Higher Light Olefin and Aromatic Yields

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Solution Overview

Problem

Conventional refinery systems face challenges in achieving high selectivity for light olefins and light aromatic compounds during the steam enhanced catalytic cracking of crude oil using ZSM-5 zeolites, as they often result in lower yields of these valuable products.

Innovation Solution

A cracking catalyst composition is developed that includes a metal species impregnated on a ZSM-5 zeolite, such as chromium, vanadium, iron, platinum, molybdenum, or cerium, which is prepared by a method involving mixing with water, evaporation, and calcination to enhance dispersion, thereby improving the conversion of crude oil to light olefins and aromatic compounds.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional ZSM-5 zeolite is used for steam enhanced catalytic cracking, then the process is simple, but the yield of light olefins and light aromatic compounds is low

Engineering Contradiction:
Improveyield of light olefins and light aromatic compoundsVSAvoidcatalyst composition complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent applies composite materials by combining metal species (such as chromium, vanadium, iron, platinum, molybdenum, or cerium) with ZSM-5 zeolite to create a composite catalyst. This composite structure integrates the cracking activity of ZSM-5 with the selective properties of the metal species, thereby increasing the yield of light olefins and light aromatic compounds while managing the added complexity through systematic catalyst design

Inventive Principle:
Principle #40Composite materials

2Productivity

If metal species are impregnated on ZSM-5 zeolite to improve product yield, then the yield of light olefins and aromatic compounds increases, but the manufacturing process becomes more complex

Engineering Contradiction:
Improveyield of light olefins and aromatic compoundsVSAvoidcatalyst preparation process
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent applies preliminary action by performing metal species impregnation on the ZSM-5 zeolite before the cracking reaction. The metal species are pre-loaded onto the zeolite support through impregnation followed by drying and calcination, creating a pre-assembled catalyst that is ready for use. This preliminary preparation ensures optimal distribution of metal species and activates the catalyst for enhanced cracking performance

Inventive Principle:
Principle #10Preliminary action

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 composition significantly enhances the yield of light olefins and aromatic compounds, achieving yields of up to 40-60% and 15-45% respectively, compared to conventional methods, by ensuring greater dispersion of the metal species on the ZSM-5 zeolite surfaces.

Implementation Method 1

a cracking catalyst composition is developed that includes a metal species impregnated on a ZSM-5 zeolite

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

which is prepared by a method involving mixing with water, evaporation, and calcination

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 3

contacting the hydrocarbon feed with steam in the presence of a cracking catalyst composition at reaction conditions sufficient to cause at least a portion of hydrocarbons in the hydrocarbon feed to undergo one or more cracking reactions

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS12351760B2Modified ZSM-5 for steam enhanced catalytic cracking of crude oil to light olefins and aromatics
Publication Date: 2025.07.08 SAUDI ARABIAN OIL CO
  • US12351760B2 patent drawing
  • US12351760B2 patent drawing
  • US12351760B2 patent drawing

AI summary

A process for upgrading a hydrocarbon feed comprises contacting the hydrocarbon feed with steam in the presence of a cracking catalyst composition at reaction conditions sufficient to cause at least a portion of hydrocarbons in the hydrocarbon feed to undergo one or more cracking reactions to produce a steam catalytic cracking effluent comprising light olefins, light aromatic compounds, or both, where the cracking catalyst composition comprises a cracking additive comprising metal species impregnated on a ZSM-5 zeolite, where the metal species comprises a metal selected from the group consisting of chromium, vanadium, iron, platinum, molybdenum, cerium, and nickel.