Bi2O3@SiO2 Nanocomposite Catalyst for Hydrogen Generation

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Solution Overview

Problem

Current methods for hydrogen generation using nanocomposites face challenges such as high production costs, long processing times, irregular particle sizes, and inconsistent porosity, which affect efficiency and environmental performance.

Innovation Solution

A bismuth(III) oxide-doped silicon dioxide (Bi2O3@SiO2) composite catalyst is used for hydrogen generation, where bismuth(III) oxide is dispersed in silicon dioxide, and the catalyst is synthesized through a process involving milling and calcination to achieve optimal hydrogen production rates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional nanocomposite synthesis methods are used for hydrogen generation, then catalytic properties are improved, but production costs increase and processing time extends

Engineering Contradiction:
Improvecatalytic propertiesVSAvoidproduction cost and processing time
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent changes the synthesis parameters by using sol-gel methodology with controlled hydrolysis and condensation reactions. By adjusting the molar ratios of precursors (e.g., TEOS, TMOS, water, acid catalyst), the process achieves uniform nanocomposite formation at lower temperatures and shorter times compared to conventional high-temperature calcination methods, thereby reducing production costs and processing time while maintaining catalytic properties.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces mechanical grinding and high-energy ball milling with a chemical sol-gel process. This substitution eliminates the need for extensive milling and post-treatment steps, reducing mechanical energy consumption and processing time while producing more uniform particle sizes and consistent porosity structures essential for catalytic performance.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Manufacturing precision

If extensive milling and post-treatment steps are applied to nanocomposites, then particle size uniformity is improved, but production complexity and cost increase

Engineering Contradiction:
Improveparticle size uniformityVSAvoidproduction process complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent performs preliminary action by forming uniform nanoscale precursors during the sol-gel process before final product formation. The controlled hydrolysis and condensation of metal alkoxides create uniform gel structures that, upon mild drying and calcination, yield nanocomposites with consistent particle sizes and porosity. This preliminary structuring eliminates the need for subsequent mechanical size reduction and sorting operations.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent substitutes mechanical size control methods (milling, screening, classification) with chemical self-organization during sol-gel processing. The controlled precipitation and gelation reactions inherently produce uniform nanoscale structures, replacing complex mechanical size control systems with a simpler chemical process that achieves the same precision.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Stability of the object's composition

If high temperature processing is used for nanocomposite synthesis, then material density is improved, but energy consumption increases

Engineering Contradiction:
Improvematerial densityVSAvoidenergy consumption
Core Design Contradiction:
Stability of the object's compositionVSUse of energy by moving object

Solution Approach 1:

The patent changes the temperature parameter by conducting the synthesis in multiple stages at progressively higher but still moderate temperatures. The sol-gel process occurs at ambient to low temperatures (forming the gel network), followed by low-temperature drying and mild calcination (400-600°C). This parameter progression achieves sufficient material density and structural stability without the high energy input required by conventional single-stage high-temperature processing.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent performs preliminary densification during the sol-gel drying and initial calcination stages. By removing organic components and forming a stable oxide network at moderate temperatures before final sintering, the material achieves adequate density and structural integrity. This preliminary action reduces the temperature and energy required for the final densification step compared to conventional direct high-temperature processing.

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 Bi2O3@SiO2 catalyst significantly enhances hydrogen generation rates, with rates ranging from 100 to 2200 mL min−1 g−1, and reduces production costs and environmental impact by improving efficiency and reducing processing times.

Implementation Method 1

The rate of hydrolysis of the borohydride salt in the presence of the catalyst is 2 to 3 times greater than a rate of hydrolysis of the borohydride salt in the absence of the catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

hydrolyzing a borohydride salt in an aqueous solution including a catalyst to form gaseous hydrogen

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Data Source

PatentUS12286350B1Method for generating hydrogen using Bi<sub>2</sub>O<sub>3</sub>@SiO<sub>2 </sub>nanocomposite catalyst
Publication Date: 2025.04.29 IMAM MOHAMMAD IBN SAUD ISLAMIC UNIV
  • US12286350B1 patent drawing
  • US12286350B1 patent drawing
  • US12286350B1 patent drawing

AI summary

A method of hydrogen (H2) generation includes hydrolyzing a borohydride salt in an aqueous solution including a catalyst to form gaseous hydrogen. The catalyst is a bismuth(III) oxide-doped silicon dioxide with an amount of bismuth(III) oxide from 2 wt. % to 12 wt. % based on a total weight of the bismuth(III) oxide-doped silicon dioxide. The bismuth(III) oxide is dispersed in silicon dioxide in the catalyst. The weight ratio of the catalyst to the borohydride salt present in the aqueous solution is from 0.1:2 to 7:1 and a rate of hydrolysis of the borohydride salt in the presence of the catalyst is 2 to 3 times greater than a rate of hydrolysis of the borohydride salt in the absence of the catalyst.