Hydrogen Extraction from Natural Gas with CO2 Recycling

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Solution Overview

Problem

Conventional hydrogen extraction methods from natural gas result in significant carbon dioxide emissions due to the production of CO2 during steam splitting and subsequent conversion stages, making them major contributors to environmental pollution.

Innovation Solution

A method involving catalytic splitting of hydrocarbons in a reformer using steam to produce hydrogen, carbon monoxide, and carbon dioxide, followed by conversion of carbon monoxide to carbon dioxide, which is then removed through gas scrubbing, and the use of a pressure swing adsorption system to separate hydrogen, with the waste gas being recycled as a fuel gas free of carbon, eliminating the need for carbon-containing fuels in reformer firing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional steam splitting and conversion methods are used to extract hydrogen from natural gas, then hydrogen production efficiency is improved, but carbon dioxide emissions increase significantly

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

Solution Approach 1:

The patent converts the harmful CO2 produced during steam splitting into a beneficial resource by recycling it to the reformer combustion chamber. The CO2 from the conversion stage is used as a fuel component, replacing external carbon-containing fuels and thereby reducing net CO2 emissions while maintaining the energy needed for hydrogen production

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

Solution Approach 2:

Instead of discarding the CO2 produced during the conversion stage as waste, the patent recovers and reuses it by feeding it back to the reformer combustion chamber. This recovery approach transforms a harmful emission into a useful fuel source, reducing the need for external carbon-containing fuels

Inventive Principle:
Principle #34Discarding and recovering

2Productivity

If additional carbon-containing fuels are fired in the reformer combustion chamber to maintain energy supply, then hydrogen production continues, but carbon dioxide emissions increase further

Engineering Contradiction:
Improvehydrogen production continuityVSAvoidcarbon dioxide emissions from fuel firing
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The system becomes self-sufficient by using its own internally generated CO2 as fuel for the reformer combustion chamber. This eliminates the need to import external carbon-containing fuels, as the CO2 produced during hydrogen production is recycled and utilized to maintain the energy supply needed for continuous hydrogen production

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent recovers the CO2 that would otherwise be discarded from the conversion stage and uses it as fuel in the reformer combustion chamber. This recovery process replaces the need for additional carbon-containing fuels, thereby maintaining hydrogen production continuity while reducing CO2 emissions

Inventive Principle:
Principle #34Discarding and recovering

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 approach reduces carbon dioxide emissions by approximately 75% compared to conventional methods, utilizing proven technologies with minimal additional effort and expense, and allows for retrofitting existing hydrogen plants to achieve this reduction.

Implementation Method 1

Hydrocarbons contained in the gas are catalytically split into hydrogen, carbon monoxide, and carbon dioxide, in a reformer, by means of steam

Methodology Applied
Scientific EffectCatalytic splitting (steam reforming): Catalysis

Implementation Method 2

in a subsequent conversion stage, catalytic conversion of the carbon monoxides that have been formed to carbon dioxide and hydrogen takes place, with steam

Methodology Applied
Scientific EffectCatalytic conversion: Catalysis

Implementation Method 3

The carbon dioxide is removed from the converted gas stream by means of gas scrubbing

Methodology Applied
Scientific EffectGas scrubbing: Absorption (physical)

Implementation Method 4

the scrubbed, hydrogen-rich gas stream is subsequently separated into a product gas stream that consists of hydrogen, and a waste gas stream, in a pressure swing adsorption system

Methodology Applied
Scientific EffectPressure swing adsorption: Pressure Swing Adsorption

Implementation Method 5

The waste gas stream is passed to the reformer, together with hydrogen that is branched off from the gas stream behind the gas scrubber, as a fuel gas that is extensively free of carbon, and combusted there

Methodology Applied
Scientific EffectCombustion: Combustion

Data Source

PatentUS7682597B2Method for extracting hydrogen from a gas that contains methane, especially natural gas, and system for carrying out said method
Publication Date: 2010.03.23 THYSSENKRUPP UHDE GMBH
  • US7682597B2 patent drawing
  • US7682597B2 patent drawing
  • US7682597B2 patent drawing

AI summary

The invention relates to a method for extracting hydrogen from a gas containing methane, especially natural gas. Hydrocarbons contained in the gas are catalytically broken down in a reformer (4) by steam in order to form hydrogen, carbon monoxide and carbon dioxide. Catalytic conversion of the obtained carbon monoxide with steam occurs in a downstream conversion step in order to form carbon monoxide and water. Carbon dioxide is removed from the converted gas flow (8) by gas washing (7), and the washed hydrogen-rich gas flow (10) is subsequently divided in a pressure-swing adsorption system (11) into a product gas flow (12) made of hydrogen and a waste gas flow (13). The waste gas flow (13) is introduced with hydrogen (14), which is separated from the gas flow (10) after gas washing, into a reformer (4) which is essentially a carbon-free combustible gas, and is combusted there. The invention also relates to a system for carrying out the method.