Formic Acid Dehydrogenation Reactor With Tangential Recirculation

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Solution Overview

Problem

Existing methods for hydrogen production from formic acid often result in high carbon monoxide (CO) generation due to inadequate temperature control, leading to impure hydrogen production.

Innovation Solution

A system and method involving a reactor vessel with a temperature control arrangement outside the reactor space, a pump, and a tangentially directed inflow conduit to maintain uniform temperature and mixing, avoiding mechanical stirrers, and using a catalyst like Ru-based carbene complexes for dehydrogenation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If heating means is provided inside the reactor space to heat the mixture, then the reaction temperature can be controlled, but local high temperatures are generated leading to increased CO generation rate

Engineering Contradiction:
Improvereaction temperatureVSAvoidCO generation rate
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

Solution Approach 1:

The heating function is segmented from the reaction zone. The temperature control arrangement is positioned outside the reactor space, separating the heating function from the reaction zone to avoid local temperature spikes that promote CO generation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent introduces a temperature control arrangement as an intermediary component positioned outside the reactor. This intermediary controls the temperature of the formic acid feed without directly heating the reaction mixture inside the reactor, thereby preventing local overheating and CO generation.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Ease of operation

If mechanical stirrers are used to mix the catalyst and formic acid, then mixing efficiency is improved, but device complexity and cost increase

Engineering Contradiction:
Improvemixing efficiencyVSAvoidsystem complexity
Core Design Contradiction:
Ease of operationVSDevice complexity

Solution Approach 1:

The mechanical stirrer is completely removed from the system. Instead of using mechanical mixing, the patent extracts the mixing function and replaces it with a simpler system where formic acid is fed directly onto the catalyst in a configured reactor geometry, eliminating complex mechanical components.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The mechanical mixing system is replaced with a chemical/physical approach where the formic acid feed strategy and reactor geometry create effective mixing without mechanical stirrers, reducing device complexity while maintaining mixing efficiency.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If high temperature is used to increase hydrogen production rate, then productivity is improved, but CO generation increases reducing hydrogen purity

Engineering Contradiction:
Improvehydrogen production rateVSAvoidhydrogen purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent changes the temperature control parameter from high temperature to a more moderate temperature range (20-200°C). This parameter change slows down the reaction rate but prevents excessive CO generation, allowing for purer hydrogen production while maintaining acceptable productivity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates a controlled reaction environment that minimizes CO generation, effectively creating an 'inert' chemical environment regarding CO production. By controlling temperature and feed strategies, the system maintains an environment favorable for hydrogen production without significant CO contamination.

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

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

Produces relatively pure hydrogen by minimizing CO generation through precise temperature control and effective mixing, ensuring a robust and cost-effective process.

Implementation Method 1

hydrogen production by dehydrogenation of formic acid

Methodology Applied
Scientific EffectDehydrogenation:

Implementation Method 2

a catalyst provided in the fuel cells

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

heating and/or cooling, in use, said mixture withdrawn from said reactor space to a predetermined temperature range

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 4

precise temperature control

Methodology Applied
Scientific EffectThermal control:

Implementation Method 5

a pump, communicatively coupled for fluid flow, via said mixture inflow opening and said mixture outflow opening, to said reactor space

Methodology Applied
Scientific EffectFluid circulation: Pump

Implementation Method 6

said mixture, in use, is introduced in said reactor space, via said mixture inflow opening, in a predetermined direction having a tangential component, preferably arranged for stirring and/or mixing

Methodology Applied
Scientific EffectTangential flow mixing: Stirring

Data Source

PatentUS12497292B2System and method for hydrogen production by dehydrogenation of formic acid
Publication Date: 2025.12.16 DENS BV
  • US12497292B2 patent drawing
  • US12497292B2 patent drawing

AI summary

The system includes a reactor vessel having a reactor space bound by a reactor wall. The reactor vessel is arranged for holding a mixture of a catalyst and formic acid in the reactor space. The reactor vessel includes a mixture inflow opening for allowing the mixture to enter the reactor space and a mixture outflow opening for allowing said mixture to exit the reactor space, and a gas outflow opening for allowing hydrogen originating from the mixture to exit the reactor space. A method for hydrogen production includes: providing the formic acid and the catalyst into the reactor space; withdrawing the mixture from the reactor space; heating and/or cooling the mixture to a predetermined temperature range outside the reactor space; and introducing the heated and/or cooled mixture into the reactor space in a predetermined direction having a tangential component arranged for stirring said mixture in the reactor space.