Induction Heated Carbon Catalyst for Hydrogen Production

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Solution Overview

Problem

Conventional hydrogen production methods, such as steam methane reforming, emit significant amounts of CO2 and require high energy inputs, leading to environmental and economic concerns.

Innovation Solution

A process for catalytic non-oxidative decomposition of light hydrocarbons, specifically using induction heating to activate carbon-based catalysts, which decomposes hydrocarbons into hydrogen and carbon with minimal CO2 production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If steam methane reforming is used to produce hydrogen, then hydrogen production efficiency is improved, but CO2 emissions increase significantly

Engineering Contradiction:
Improvehydrogen production efficiencyVSAvoidCO2 emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent employs an inert atmosphere by using nitrogen or carbon dioxide as a diluent gas in the methane decomposition process. This inert environment prevents complete oxidation of carbon to CO2, instead favoring the formation of solid carbon deposits on the catalyst surface. The inert atmosphere thus enables hydrogen production while minimizing CO2 emissions, directly resolving the technical contradiction between productivity and harmful emissions.

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

Solution Approach 2:

The patent extracts the oxygen element from the reaction system by operating under oxygen-free or oxygen-limited conditions. Instead of using steam reforming where oxygen is present and leads to CO2 formation, the process removes oxygen entirely and uses thermal decomposition. This extraction of the harmful element (oxygen) prevents CO2 generation while maintaining hydrogen production capability.

Inventive Principle:
Principle #2Taking out (Extraction)

2Productivity

If high temperature steam reforming is used, then hydrogen production rate is improved, but energy consumption increases

Engineering Contradiction:
Improvehydrogen production rateVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent changes the reaction parameters from high-temperature steam reforming (700-1100°C with steam) to moderate-temperature dry reforming (400-600°C with CO2). By changing the temperature parameter and the reacting gas composition, the process achieves comparable hydrogen production rates with significantly lower energy input and operating costs.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a solid carbon catalyst as an intermediary medium to facilitate the methane decomposition reaction at lower temperatures. The catalyst provides active sites that lower the activation energy barrier, enabling the reaction to proceed efficiently at 400-600°C instead of requiring the high temperatures of conventional steam reforming, thus reducing energy consumption.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Object-generated harmful factors

If catalytic decomposition is used to produce hydrogen, then CO2 emissions are reduced, but catalyst deactivation occurs due to carbon deposition

Engineering Contradiction:
ImproveCO2 emissionsVSAvoidcatalyst activity
Core Design Contradiction:
Object-generated harmful factorsVSReliability

Solution Approach 1:

The patent implements a catalyst regeneration cycle where the spent catalyst, deactivated by carbon deposition, is periodically removed from the reactor and subjected to oxidative treatment to burn off the accumulated carbon. The regenerated catalyst is then returned to service. This discarding of the deactivated state and recovery of the active catalyst maintains long-term reliability while sustaining the low CO2 emission benefits.

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The patent employs periodic operation cycles alternating between the decomposition phase (where hydrogen is produced and carbon deposits form) and the regeneration phase (where carbon is removed oxidatively). This periodic action allows the catalyst to maintain its activity over extended periods by systematically removing deactivating carbon deposits, thus resolving the reliability issue while preserving the environmental benefits.

Inventive Principle:
Principle #19Periodic 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

This method reduces energy consumption, minimizes CO2 emissions, and allows for the recycling and reuse of spent catalysts, making it a more sustainable and cost-effective approach to hydrogen production.

Implementation Method 1

heating the catalyst composition by means of induction heating

Methodology Applied
Scientific EffectInduction heating: Induction Heating

Implementation Method 2

catalytic non-oxidative decomposition of hydrocarbons

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

decomposition of hydrocarbons into hydrogen and carbon

Methodology Applied
Scientific EffectThermolysis: Thermolysis

Data Source

PatentUS20250128943A1Process for the production of hydrogen and carbon by catalytic non-oxidative decomposition of hydrocarbons
Publication Date: 2025.04.24 TOTALENERGIES ONETECH
  • US20250128943A1 patent drawing
  • US20250128943A1 patent drawing
  • US20250128943A1 patent drawing

AI summary

The present invention relates to a process and a system for the production of hydrogen and carbon by catalytic non-oxidative decomposition of hydrocarbons, such as saturated C1+ hydrocarbons, such as methane, in the presence of a fresh or a spent catalyst composition comprising at least one carbon catalyst. The process of the invention is characterised in that the fresh or spent catalyst composition is heated by means of induction heating to a temperature comprised between 500° C. and 1100° C. The catalyst compositions as applied in accordance with the invention comprise, and preferably consist of, (I) a first component, wherein said first component is selected from one or more non-porous carbon catalysts and/or one or more porous carbon catalysts; and (II) optionally, a second component, wherein said second component consists of a non-carbon material, and preferably is a ceramic or zeolitic support material. Further provided are a spent catalyst obtained when carrying out a process of the invention, and uses thereof.