Divided-Cell Electrochemical Hydrogenation for Selective Products

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Solution Overview

Problem

Existing electrochemical hydrogenation processes face challenges such as high complexity, high production costs, formation of undesired by-products, and the use of complex and potentially harmful electrolytes and electrodes that require frequent activation or replacement, leading to increased purification efforts.

Innovation Solution

The process employs a divided cell with sulfuric acid as the electrolyte, using electrodes made of graphite, nickel, or steel for the cathode and platinum, boron-doped diamond, ruthenium oxide, platinum oxide, or iridium oxide for the anode, and operates galvanostatically to minimize by-product formation and simplify electrode maintenance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional catalytic hydrogenation is used, then hydrogenation of organic compounds can be achieved, but high temperatures, high pressures and expensive catalysts are required

Engineering Contradiction:
Improvehydrogenation efficiencyVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent replaces the conventional thermal-catalytic hydrogenation system with an electrochemical system. Instead of using high temperatures and pressures with expensive metal catalysts, the invention uses electrochemical reduction at a cathode in aqueous electrolyte solutions, substituting mechanical/thermal energy with electrical energy for more efficient and selective hydrogenation

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

Solution Approach 2:

The patent changes the fundamental reaction parameters from thermal-catalytic conditions (high temperature, high pressure, expensive catalysts) to electrochemical conditions (moderate temperature, ambient pressure, electrode-based catalysis). This parameter transformation enables hydrogenation under milder and more economically viable conditions

Inventive Principle:
Principle #35Parameter changes

2Productivity

If ammonium acetate or ammonium chloride is used as electrolyte, then electrochemical hydrogenation can proceed, but the preparation and purification of materials become very complex and chlorine is released as a byproduct

Engineering Contradiction:
Improvehydrogenation rateVSAvoidpurification complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent employs inexpensive, readily available electrolytes such as sulfuric acid, sodium sulfate, or potassium sulfate that can be easily prepared and disposed of or regenerated without complex purification procedures. These simple electrolytes replace the complex ammonium-based electrolytes, significantly reducing material preparation and purification complexity while maintaining electrochemical hydrogenation efficiency

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent avoids using chloride-containing electrolytes that would generate harmful chlorine byproducts. By selecting sulfate-based or other non-chloride electrolytes, the process converts a potential harmful outcome (chlorine release) into a beneficial one (no harmful byproducts), eliminating the need for separate chlorine removal and treatment systems

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

3Device complexity

If undivided cells are used, then the process setup is simpler, but anodic reactions lead to formation of oxidative by-products and reduce selectivity

Engineering Contradiction:
Improvecell structureVSAvoidproduct selectivity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent divides the electrochemical cell into separate cathode and anode compartments using a separator or membrane. This segmentation prevents oxidative by-products formed at the anode from contaminating the reduction products at the cathode, thereby maintaining high product selectivity while keeping the overall cell structure relatively simple

Inventive Principle:
Principle #1Segmentation

4Productivity

If nickel skeleton catalyst is used on cathode, then electrocatalytic activity is enhanced, but the electrodes must be regularly activated and products become contaminated with nickel-containing material

Engineering Contradiction:
Improvecatalytic activityVSAvoidelectrode maintenance
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent employs cathode materials that are stable and do not require regular activation or replacement. By using electrodes such as stainless steel, nickel foam, or other stable substrates with appropriate catalytic properties, the system achieves self-maintaining operation without the need for periodic activation treatments, reducing maintenance complexity and preventing product contamination

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent uses stable, long-lasting electrode materials that eliminate the need for frequent replacement or activation. These durable electrodes provide sustained catalytic activity without degrading or contaminating products, replacing the problematic nickel skeleton catalyst with more reliable alternatives

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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 achieves high selectivity and efficiency with reduced by-products, lowers production costs, and simplifies electrode handling and purification, making it suitable for large-scale industrial applications.

Implementation Method 1

The protons required for the hydrogenation/reduction of organic compounds on the cathode side are preferably generated from water on the anode side

Methodology Applied
Scientific EffectElectrochemical hydrogenation: Electrolysis

Implementation Method 2

The protons required for the hydrogenation/reduction of organic compounds on the cathode side are preferably generated from water on the anode side

Methodology Applied
Scientific EffectWater electrolysis: Electrolysis

Implementation Method 3

In these, the two half-cells are separated by the use of a separator

Methodology Applied
Scientific EffectPhysical separation: Semipermeable Membrane

Data Source

PatentEP4621103A1Method for the electrochemical hydrogenation of organic compounds
Publication Date: 2025.09.24 EVONIK OPERATIONS GMBH
  • EP4621103A1 patent drawing
  • EP4621103A1 patent drawing

AI summary

The present invention relates to a process for the electrochemical hydrogenation of an organic compound selected from the group consisting of ketones, enones, aromatics and nitriles in a divided cell with H2O as hydrogen source and in the presence of H2SO4 in anolyte and catholyte, in which a pure material electrode made of a material selected from graphite, nickel and steel is used as the cathode and an electrode selected from solid-body and supported electrodes with an active material selected from platinum, graphite, boron-doped diamond, ruthenium oxide, platinum oxide and/or iridium oxide is used as the anode.