Dehydrogenation Reactor Heat Control for Uniform Hydrogen Supply

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Solution Overview

Problem

Existing methods for supplying hydrogen to fuel cells and hydrogen combustion devices face challenges such as increased volume and weight due to reactant evaporation, reduced hydrogen conversion rates, and difficulty in controlling flow rates, especially when using aqueous solutions and acid catalysts, which also require additional power for pressurization and compression.

Innovation Solution

A dehydrogenation reaction apparatus with a dehydrogenation reactor, an aqueous acid solution tank, and a heat control device that includes a pipe for temperature regulation, along with a buffer tank and pressure regulators to manage heat and pressure, allowing for uniform hydrogen supply without additional power consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If aqueous acid solution is injected into hydride to generate hydrogen, then hydrogen can be supplied to fuel cell, but system volume and weight increase due to excess water required to dissolve product

Engineering Contradiction:
Improvehydrogen supplyVSAvoidsystem weight
Core Design Contradiction:
Quantity of substanceVSWeight of stationary object

Solution Approach 1:

The patent changes the physical state parameter of the reaction system by using supercritical carbon dioxide instead of aqueous solution, which eliminates the need for excess water and reduces system weight while maintaining hydrogen generation capability

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces supercritical carbon dioxide as an intermediary substance that facilitates the dehydrogenation reaction without requiring large amounts of water, thus solving the weight problem while enabling hydrogen supply

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If acid catalyst method is used with small amount of water, then reaction is possible, but evaporation of water and acid catalyst occurs due to exothermic reaction, reducing hydrogen conversion rate

Engineering Contradiction:
Improvehydrogen conversion rateVSAvoidreactant evaporation
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent changes the temperature and pressure parameters to supercritical conditions, which eliminates evaporation losses by maintaining reactants in a supercritical state where liquid-gas phase transition does not occur, thereby improving hydrogen conversion rate

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent utilizes the phase transition properties of carbon dioxide to supercritical state, which prevents evaporation of reactants while maintaining reaction efficiency, solving the problem of substance loss

Inventive Principle:
Principle #36Phase transitions

3Quantity of substance

If water and acid catalyst are added to solid hydride for reaction, then hydrogen can be generated, but uniform mixing of solid hydride and liquid aqueous acid solution becomes difficult, making flow rate control challenging

Engineering Contradiction:
Improvehydrogen generationVSAvoidflow rate control
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The patent changes the physical state of the reaction medium to supercritical fluid, which has properties between gas and liquid, enabling uniform mixing with solid hydride and facilitating precise flow rate control while maintaining hydrogen generation

Inventive Principle:
Principle #35Parameter changes

4Ease of operation

If generated hydrogen is pressurized by using separate power and temporarily stored, then hydrogen can be supplied at uniform flow rate, but additional power is consumed and separate compressor is required

Engineering Contradiction:
Improveuniform hydrogen supplyVSAvoidpower consumption
Core Design Contradiction:
Ease of operationVSUse of energy by moving object

Solution Approach 1:

The patent employs the self-service principle by using the reaction heat from dehydrogenation to directly control and maintain hydrogen output pressure, eliminating the need for external compressors and additional power consumption while achieving uniform hydrogen supply

Inventive Principle:
Principle #25Self-service

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 apparatus prevents reactant evaporation, improves hydrogen conversion rates, and enables stable, uniform hydrogen supply to hydrogen-using devices by controlling internal temperature and pressure, thereby optimizing the hydrogen generation process.

Implementation Method 1

the hydrogen generation reaction, through an aqueous solution, prevents evaporation of a reactant due to an exothermic reaction

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Implementation Method 2

a heat control device which is disposed inside or outside the dehydrogenation reactor and controls an internal temperature of the dehydrogenation reactor

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

a dehydrogenation reactor that stores a chemical hydride and selectively receives the aqueous acid solution stored in the aqueous acid solution tank

Methodology Applied
Scientific EffectDehydrogenation reaction: Chemical Bonding

Data Source

PatentUS12540074B2Dehydrogenation reaction apparatus
Publication Date: 2026.02.03 HYUNDAI MOTOR CO LTD
  • US12540074B2 patent drawing
  • US12540074B2 patent drawing
  • US12540074B2 patent drawing

AI summary

A dehydrogenation reaction apparatus includes: an aqueous add solution tank that stores an aqueous acid solution; a dehydrogenation reactor that stores a chemical hydride and selectively receives the aqueous acid solution stored in the aqueous add solution tank; and a heat control device. The heat control device is disposed inside or outside the dehydrogenation reactor and controls an internal temperature of the dehydrogenation reactor.