Flake Zeolite Cracking for Light Olefin and Paraffin Selectivity

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing methods for catalytic cracking of n-dodecane using zeolites face challenges in achieving high conversion and selectivity towards light olefins, necessitating improvements in the physical and chemical characteristics of zeolites to enhance their efficiency and selectivity.

Innovation Solution

A method involving a modified aluminosilicate zeolite catalyst with a specific SiO2 to Al2O3 ratio, flake morphology, and defined structural properties is used to crack hydrocarbons, particularly n-dodecane, into olefins and paraffins, with a high conversion rate and selective production of compounds with 1 to 6 carbon atoms.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional zeolite catalysts are used for catalytic cracking of n-dodecane, then the process can proceed, but the conversion rate and selectivity towards light olefins are insufficient

Engineering Contradiction:
Improveconversion rateVSAvoidselectivity towards light olefins
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent applies parameter changes by modifying the SiO2/Al2O3 ratio to specific ranges (20:1 to 100:1, preferably 30:1 to 70:1), controlling particle size (5-50 nm), and adjusting crystal structure parameters of the zeolite catalyst. These parameter optimizations simultaneously improve conversion rate (90-99%) and selectivity towards light olefins (C2-C4), resolving the contradiction between productivity and manufacturing precision.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite materials by creating modified zeolite structures with specific SiO2/Al2O3 ratios and combining them with controlled particle size distributions (5-50 nm range). This composite approach with optimized physical and chemical properties enables both high conversion and high selectivity, addressing the technical contradiction effectively.

Inventive Principle:
Principle #40Composite materials

2Productivity

If the SiO2/Al2O3 ratio is increased to improve catalytic performance, then conversion efficiency improves, but catalyst synthesis complexity increases

Engineering Contradiction:
Improvecatalytic conversion efficiencyVSAvoidcatalyst synthesis complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent optimizes the SiO2/Al2O3 ratio within specific ranges (20:1 to 100:1, preferably 30:1 to 70:1) to achieve high catalytic efficiency. By defining precise parameter boundaries, the patent simplifies the synthesis process while maintaining superior performance, resolving the contradiction between productivity and device complexity.

Inventive Principle:
Principle #35Parameter changes

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 modified zeolite catalyst achieves a conversion rate of at least 90% of n-dodecane into smaller carbon compounds, with a high yield of light olefins and paraffins, including 25% paraffins with 3-4 carbon atoms and 15% olefins with 2-4 carbon atoms, demonstrating improved catalytic performance.

Implementation Method 1

a method of cracking hydrocarbons using zeolites

Methodology Applied
Scientific EffectCatalytic cracking: Catalysis

Data Source

PatentUS20260022082A1Method for forming a paraffin/olefin mixture from a hydrocarbon
Publication Date: 2026.01.22 KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
  • US20260022082A1 patent drawing
  • US20260022082A1 patent drawing
  • US20260022082A1 patent drawing

AI summary

A method of cracking a hydrocarbon including contacting the hydrocarbon with a catalyst; where on the contacting, the hydrocarbon is cracked into a plurality of compounds, each having a smaller number of carbon atoms than the hydrocarbon. The catalyst includes an aluminosilicate zeolite, the aluminosilicate zeolite includes a weight ratio of SiO2 to Al2O3 of 10-200:1. Particles of the aluminosilicate zeolite have a flake shape with an average longest dimension of 10 nanometers (nm) to 50 nm and the flakes are stacked on top of one another.