Nickel Boron Magnesium Oxide Catalyst for Low-Temperature Hydrogen Production

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Solution Overview

Problem

Existing catalysts for steam reforming of hydrocarbons, such as nickel-based catalysts, are unstable and non-reactive at low temperatures, and noble metal alternatives are expensive, while current technologies face challenges with carbon deposition and catalyst poisoning in hydrogen-lean conditions.

Innovation Solution

A porous catalyst comprising nickel, boron, and magnesium, with specific pore sizes and compositions, is developed for efficient hydrogen and syngas production, suitable for a broad temperature range, including low-temperature reforming, and enhanced stability through confinement effects and the presence of magnesium.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If nickel-based catalysts are used for steam reforming, then catalytic activity is achieved, but stability and reactivity at low temperatures deteriorate

Engineering Contradiction:
Improvecatalyst stabilityVSAvoidoperating temperature range
Core Design Contradiction:
ReliabilityVSTemperature

Solution Approach 1:

The patent uses a composite catalyst structure consisting of nickel particles supported on magnesium oxide with boron addition. This composite material combines the catalytic activity of nickel with the thermal stability of MgO and the structural promotion effect of boron, enabling stable operation across a broad temperature range including low temperatures where conventional nickel catalysts fail.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The catalyst exhibits local quality through confined nickel particles within specific pore structures of the MgO support. The boron addition creates local structural modifications that enhance nickel dispersion and stability, providing different functional properties in different regions of the catalyst material to achieve both low-temperature activity and high-temperature stability.

Inventive Principle:
Principle #3Local quality

2Reliability

If noble metals are used as catalyst alternatives, then catalytic activity and stability improve, but cost increases

Engineering Contradiction:
Improvecatalyst stabilityVSAvoidcatalyst cost
Core Design Contradiction:
ReliabilityVSQuantity of substance

Solution Approach 1:

The patent replaces expensive noble metals with a cheaper nickel-based catalyst system. By using nickel supported on MgO with boron promotion, the catalyst achieves comparable stability and activity to noble metals but at significantly lower cost, making the catalyst economically viable for industrial applications.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent modifies the catalyst composition parameters by adding boron to the nickel-MgO system. This parameter change (boron addition) fundamentally alters the catalyst properties, providing noble-metal-like stability and low-temperature activity without the associated high cost, effectively decoupling performance from material expense.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If conventional catalysts are used in hydrogen-lean conditions, then steam reforming proceeds, but carbon deposition increases causing catalyst poisoning

Engineering Contradiction:
Improvehydrogen production rateVSAvoidcarbon deposition
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent converts the potentially harmful carbon deposition into a beneficial effect by using boron-promoted nickel catalyst. The boron modifies the nickel surface properties to promote selective carbon gasification reactions, where deposited carbon is converted to CO/CO2, thereby preventing catalyst poisoning while maintaining high hydrogen production rates in hydrogen-lean conditions.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The boron component acts as an intermediary between nickel and carbon. It modifies the interaction between nickel catalyst and carbon deposits, facilitating carbon removal through gasification reactions and preventing the formation of problematic carbon structures like graphite and soot that would poison the catalyst.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 achieves high catalytic activity and stability at lower temperatures, reduces carbon formation, and maintains catalyst particle size, enabling efficient hydrogen production with reduced energy requirements and extended operational stability.

Implementation Method 1

enhanced stability through confinement effects and the presence of magnesium

Methodology Applied
Scientific EffectConfinement effects: Physical Containment

Implementation Method 2

catalyst for hydrogen production, especially a reforming process

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP2640509B1Catalyst for hydrogen production
Publication Date: 2023.01.04 NEDERLANDSE ORG VOOR TOEGEPAST NATUURWETENSCHAPPELIJK ONDERZOEK TNO
  • EP2640509B1 patent drawingFigure 1a~1b
  • EP2640509B1 patent drawingFigure 2~3
  • EP2640509B1 patent drawingFigure 4

AI summary

The invention provides a catalyst for the production of hydrogen by steam reforming. The catalyst is a porous catalyst which is based on at least aluminium oxide and preferably magnesium oxide, and further comprises boron and nickel. The porous catalyst comprises pores having an average pore size in the range of 0.1-50 nm. The activity of the catalyst may be further enhanced by addition of a noble metal such as Rh, Ru, Pd, Ir or Pt. The catalyst can be broadly used in hydrogen production processes, and is especially suitable for reforming using a membrane which is selective for a predetermined reaction product. Such process can be operated at relatively low temperatures of about 450-700 ?C.