Electrolytic Scrubber CO2 Recovery via Off-Gas Recycle

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Solution Overview

Problem

Existing carbon capture systems in electrolytic regeneration processes are inefficient in increasing the uptake of carbon dioxide, leading to significant emissions and energy consumption.

Innovation Solution

A method and system that involves scrubbing gases with an alkaline, aqueous scrubbing liquid to dissolve CO2, regenerating the spent liquid in an electrolytic cell, and reintroducing a secondary stream of CO2-rich off-gas into the spent liquid to enhance carbon loading, optimizing pH and reducing energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If spent scrubbing liquid is regenerated in an electrolytic process with conventional off-gas release, then the scrubbing liquid is regenerated and CO2 is separated, but carbon capture efficiency is low and significant CO2 emissions occur

Engineering Contradiction:
Improvecarbon capture efficiencyVSAvoidCO2 emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent recovers CO2 from the anode off-gas that would otherwise be discarded, by injecting it back into the spent scrubbing liquid to enhance carbon loading before electrolytic regeneration

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The patent converts the harmful CO2 emissions in the anode off-gas into a beneficial resource by using it to increase carbon loading in the scrubbing liquid, thereby improving overall carbon capture efficiency

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

2Quantity of substance

If more scrubbing liquid is used to increase CO2 uptake capacity, then more CO2 can be absorbed, but the amount of liquid to be regenerated increases energy consumption

Engineering Contradiction:
ImproveCO2 uptake capacityVSAvoidenergy consumption for regeneration
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The patent changes the carbon loading parameter of the scrubbing liquid by injecting CO2-rich off-gas, thereby increasing CO2 uptake capacity without proportionally increasing the volume of liquid to be regenerated

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses CO2 from the off-gas to enhance carbon loading in the scrubbing liquid, creating a concentrated CO2 source that improves uptake capacity without requiring additional liquid volume

Inventive Principle:
Principle #26Copying

3Manufacturing precision

If CO2-rich off-gas is compressed and separated into pure CO2 and oxygen, then pure CO2 is obtained for downstream applications, but energy consumption for compression and separation increases

Engineering Contradiction:
ImproveCO2 purityVSAvoidenergy consumption for compression
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent uses the CO2-rich off-gas to enhance carbon loading in the scrubbing liquid itself, allowing the system to serve its own need for CO2 concentration without requiring external compression and separation energy

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent merges the CO2 separation function with the scrubbing liquid regeneration process by injecting off-gas directly into the liquid, combining what would be separate operations into one integrated step

Inventive Principle:
Principle #5Merging (Combining)

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

Enhances carbon capture efficiency by increasing the carbon load in the scrubbing liquid, reducing the amount of scrubbing liquid needed, and lowering energy requirements for compression and separation, while producing valuable hydrogen and oxygen for downstream applications.

Implementation Method 1

scrubbing the gas in a scrubber with a first alkaline, aqueous scrubbing liquid to dissolve carbon dioxide as hydrogen carbonate (HCO3−) and/or as carbonate (CO32−) in the first alkaline, aqueous scrubbing liquid

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Implementation Method 2

regenerating the first spent aqueous scrubbing liquid in the electrolytic cell (310) by electrolysis, depleting the first spent aqueous scrubbing liquid of hydrogen carbonate (HCO3−) and of carbonate (CO32−) in the anode chamber (313, the regeneration further comprising generating gaseous hydrogen in the cathode chamber (312) and a gaseous mixture of oxygen and carbon dioxide (CO2) in the anode chamber (313) by electrolysis

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 3

wherein carbon dioxide (CO2) and/or oxygen (O2) withdrawn from the anode chamber is compressed into liquid carbon dioxide and compressed oxygen (O2), in a compression unit

Methodology Applied
Scientific EffectCompression: Compression

Implementation Method 4

separating the liquid carbon dioxide from gaseous oxygen, in a gas separator, into a first stream comprising carbon dioxide, and a secondary stream comprising oxygen

Methodology Applied
Scientific EffectPhase separation: Phase Change

Data Source

PatentUS20250205644A1Method for increased carbon capture in an electrolytic process
Publication Date: 2025.06.26 ESTECH AS
  • US20250205644A1 patent drawing
  • US20250205644A1 patent drawing

AI summary

There is a method has the steps of (A) scrubbing the gas in a scrubber with a first alkaline, aqueous scrubbing liquid to provide a first spent aqueous scrubbing liquid; (B) feeding the first spent aqueous scrubbing liquid to an electrolytic cell having an anode chamber and a cathode chamber; (C) regenerating the first spent aqueous scrubbing liquid by electrolysis; and (D) withdrawing regenerated alkaline, aqueous scrubbing liquid from the cathode chamber and recirculating it to the scrubber. The method has a step of separating a liquid carbon dioxide from gaseous oxygen in a gas separator into (i) a first stream having carbon dioxide, and (ii) a secondary stream having oxygen containing less than 30% carbon dioxide. The secondary stream is introduced into at least a portion of the first spent aqueous scrubbing liquid prior to feeding the first spent aqueous scrubbing liquid into the anode chamber.