Oxocarbon Electrolyzer Gas Separation With Product Gas Recycle

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Solution Overview

Problem

Existing oxocarbon electrolyzers struggle to achieve near 100% conversion of oxocarbons to desired products, requiring inefficient and costly separation of unconverted oxocarbons, which are typically recycled upstream, leading to energy waste and reduced catalyst efficiency.

Innovation Solution

Recycle product gases from the output stream of oxocarbon electrolyzers back to the input, using a combination of membrane, temperature swing adsorption, pressure swing adsorption, cryogenic, and lean oil separators to enhance efficiency and purity, while minimizing excessive oxocarbon exposure to the catalyst.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If unconverted oxocarbon is separated and recycled upstream in traditional gas reactor processes, then conversion rate approaches 100%, but energy consumption increases and catalyst efficiency decreases

Engineering Contradiction:
Improveconversion rateVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

Instead of separating unconverted oxocarbon from product gases before recycling (traditional approach), this invention recycles the mixed output stream directly back to the electrolyzer input. This inversion of the separation-recycling sequence eliminates the need for energy-intensive separation steps while maintaining near 100% conversion through continuous recycling of the combined stream.

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

The invention extracts and eliminates the unnecessary separation step from the traditional process flow. By removing the separation stage that divides unconverted oxocarbon from product gases, the system directly recycles the mixed output stream, thereby eliminating the energy consumption and equipment complexity associated with separation while achieving complete conversion through recycling.

Inventive Principle:
Principle #2Taking out (Extraction)

2Productivity

If unconverted oxocarbon is recycled upstream, then conversion rate increases, but excessive oxocarbon exposure to catalyst forms undesirable byproducts

Engineering Contradiction:
Improveconversion rateVSAvoidundesirable byproducts
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The continuous recycling of the mixed output stream maintains a steady-state composition at the electrolyzer input where product gases and unconverted oxocarbon are continuously mixed. This continuous action prevents excessive accumulation of oxocarbon at the catalyst surface, thereby eliminating the formation of undesirable byproducts while achieving near 100% conversion.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

Product gases act as an intermediary substance that mixes with unconverted oxocarbon in the recycled stream. This intermediary product gas moderates the oxocarbon concentration at the catalyst surface, preventing excessive exposure and the formation of undesirable byproducts while still enabling complete conversion through the recycling loop.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If product gases are separated from feedstock gases before recycling, then product purity is maintained, but additional separation stages increase device complexity and cost

Engineering Contradiction:
Improveproduct purityVSAvoidseparation stages
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The invention extracts and removes the separation stage from the process flow. By eliminating the separation step that divides product gases from unconverted oxocarbon before recycling, the system simplifies the device structure and reduces equipment cost while maintaining product purity through the alternative approach of direct recycling followed by single-stage separation of the final product stream.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The invention applies separation only where necessary - at the final product output stage rather than at the recycling input stage. This localized application of separation maintains product purity for downstream processes while avoiding the complexity of separating streams before recycling, thereby optimizing both purity and device simplicity.

Inventive Principle:
Principle #3Local quality

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 increases electrolyzer efficiency by limiting excessive oxocarbon exposure, reduces energy consumption, and enhances product selectivity without additional separation stages, achieving higher purity and cost-effectiveness.

Implementation Method 1

membrane separators

Methodology Applied
Scientific EffectPermeation: Permeation

Implementation Method 2

temperature swing adsorption separators

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 3

pressure swing adsorption separators

Methodology Applied
Scientific EffectPressure swing adsorption: Pressure Swing Adsorption

Implementation Method 4

cryogenic separators

Methodology Applied
Scientific EffectCryogenics: Cryogenics

Implementation Method 5

lean oil separators

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Data Source

PatentUS12486586B2Separators for gaseous products in oxocarbon electrolyzers
Publication Date: 2025.12.02 DIOXYCLE
  • US12486586B2 patent drawing
  • US12486586B2 patent drawing
  • US12486586B2 patent drawing

AI summary

This disclosure relates to systems and methods for gas separation in oxocarbon electrolyzers. A disclosed method includes supplying an oxocarbon to an input stream of a cathode chamber of an oxocarbon electrolyzer, converting the oxocarbon to a product gas in the cathode chamber, obtaining an output stream, with the product gas and residual oxocarbon, from the oxocarbon electrolyzer, and recycling a portion of the product gas, from the output stream, to the input stream.