Fluidized-Bed Hydrogen Reactor With Microwave Catalyst Activation

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Solution Overview

Problem

Conventional hydrogen production methods, such as those using thermochemical decomposition or steam reforming, are energy-intensive and generate environmental pollutants like CO2, while existing pyrolysis techniques suffer from catalyst deactivation and low production efficiency due to fixed-bed reaction processes.

Innovation Solution

A hydrogen production device employing a fluidized-bed reactor with a catalyst filler and microwave irradiation, which supplies hydrocarbon gas at a fluidizing flow rate to activate the catalyst for pyrolysis, allowing for continuous operation and the generation of industrially useful carbon aggregates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If a fixed-bed type reaction process is employed for pyrolysis of hydrocarbon, then the catalyst can be easily contained and controlled, but the catalyst is deactivated in a short time due to solid carbon deposition on its surface

Engineering Contradiction:
Improvecatalyst containment and controlVSAvoidcatalyst activity duration
Core Design Contradiction:
Ease of operationVSDuration of action of moving object

Solution Approach 1:

The patent applies the dynamics principle by transitioning from a fixed-bed reactor to a fluidized-bed reactor. In the fluidized-bed system, the catalyst particles are suspended and circulated continuously through the reaction zone and regenerative zone. This dynamic circulation prevents solid carbon accumulation on catalyst surfaces by continuously removing deposited carbon in the regenerative zone, thereby maintaining catalyst activity over extended periods while still providing effective catalyst containment.

Inventive Principle:
Principle #15Dynamics

2Device complexity

If a fixed-bed reaction process is used, then the system structure is simple, but production efficiency per unit catalyst is poor and continuous operation is difficult

Engineering Contradiction:
Improvereactor structure complexityVSAvoidhydrogen production efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The patent applies segmentation by dividing the fluidized-bed reactor into distinct functional zones: a reaction zone where hydrocarbon pyrolysis occurs and hydrogen is produced, and a regenerative zone where catalyst regeneration takes place. This segmentation allows different catalyst particles to cycle through different functional stages, enabling continuous hydrogen production while maintaining high catalyst efficiency. The segmented structure facilitates continuous operation by separating the deactivation and regeneration processes in different spatial and temporal domains.

Inventive Principle:
Principle #1Segmentation

3Productivity

If conventional steam reforming is used for hydrogen production, then hydrogen can be produced efficiently, but a large amount of steam is required resulting in energy loss and CO2 generation

Engineering Contradiction:
Improvehydrogen production rateVSAvoidenergy consumption and environmental load
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The patent applies the 'blessing in disguise' principle by converting the harmful by-product (solid carbon) from catalyst deactivation into a useful outcome. Instead of viewing carbon deposition as purely detrimental, the system utilizes the carbon as a fuel source in the regenerative zone, where it reacts with oxygen to produce heat that regenerates the catalyst and generates additional energy. This converts what was previously waste material into a beneficial energy source, reducing overall energy consumption and eliminating CO2 emissions associated with external heating sources.

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

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 enables environmentally friendly, economically excellent hydrogen production with industrially useful carbon aggregates, maintaining catalyst efficiency and achieving larger particle diameters for carbon materials.

Implementation Method 1

a microwave irradiation section that irradiates the catalyst with a microwave

Methodology Applied
Scientific EffectMicrowave irradiation: Microwave Radiation

Implementation Method 2

the catalyst activated by the microwave

Methodology Applied
Scientific EffectDielectric heating: Dielectric Heating

Implementation Method 3

The gas supply section supplies the gas at a flow rate at which the filler is fluidized

Methodology Applied
Scientific EffectFluidization: Fluidisation

Implementation Method 4

hydrogen is generated by the hydrocarbon compound being pyrolyzed in the presence of the catalyst

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 5

a filler containing a catalyst for pyrolysis of a hydrocarbon

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20240208821A1Hydrogen producing device and hydrogen producing method
Publication Date: 2024.06.27 SUMITOMO CHEM CO LTD
  • US20240208821A1 patent drawing
  • US20240208821A1 patent drawing
  • US20240208821A1 patent drawing

AI summary

A hydrogen production device that includes a reactor that includes a filler containing a catalyst for pyrolysis of a hydrocarbon; a gas supply section that supplies gas containing a hydrocarbon compound; and a microwave irradiation section that irradiates the catalyst with a microwave. The gas supply section supplies the gas at a flow rate at which the filler is fluidized, and hydrogen is generated by the hydrocarbon compound being pyrolyzed in the presence of the catalyst activated by the microwave. A carbon aggregate production device includes a reactor that includes a filler containing a catalyst for pyrolysis of a hydrocarbon; a gas supply section that supplies, to the reactor, gas containing a hydrocarbon compound; and a microwave irradiation section that irradiates the catalyst with a microwave. The gas supply section supplies the gas at a flow rate at which the filler is fluidized, and a carbon aggregate is generated by the hydrocarbon compound being pyrolyzed in the presence of the catalyst activated by the microwave.