SOx Capture Using Cooled Alkaline Carbonate Solution

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Solution Overview

Problem

Conventional CO2 capture processes face efficiency losses due to the absorption of SOx and NOx contaminants, which lead to precipitation and reduced absorption capacity in alkaline solutions, requiring frequent solution bleeding and replacement, and generate waste products.

Innovation Solution

A process and system that integrates SOx removal from flue gases using a cooled alkaline carbonate solution, where the gas is contacted with an alkaline aqueous solution containing a carbonate of an alkali metal, allowing for SOx absorption and subsequent purification of the solution, reducing the need for frequent bleeding and waste disposal.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional alkaline absorption solutions are used for CO2 capture, then CO2 absorption capacity is achieved, but SOx and NOx contaminants are also absorbed causing precipitation and reduced absorption capacity

Engineering Contradiction:
Improveabsorption capacityVSAvoidabsorption solution stability
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

The absorption process is divided into two separate functional units: a gas conditioning unit for SOx/NOx removal and a CO2 absorption unit for carbon capture. This segmentation prevents contaminants from affecting the CO2 absorption solution, maintaining both absorption capacity and solution stability without requiring frequent bleeding or replacement.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A cooled alkaline carbonate solution is introduced as an intermediary medium in the gas conditioning unit. This intermediary selectively removes SOx and NOx contaminants from the flue gas before the cleaned gas enters the CO2 absorption unit, thereby protecting the CO2 absorption solution from contamination and precipitation issues.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Object-affected harmful factors

If SOx removal is performed using conventional technologies as auxiliary units, then SOx levels are reduced, but device complexity increases and integration with CO2 capture process is lacking

Engineering Contradiction:
ImproveSOx concentrationVSAvoidprocess integration
Core Design Contradiction:
Object-affected harmful factorsVSDevice complexity

Solution Approach 1:

The SOx removal function and CO2 absorption function are merged into a single integrated process system. The cooled alkaline carbonate solution serves dual purposes: it conditions the gas by removing SOx/NOx and prepares it for subsequent CO2 capture. This merging reduces device complexity compared to separate auxiliary units while effectively reducing SOx concentration.

Inventive Principle:
Principle #5Merging (Combining)

3Quantity of substance

If absorption solution bleeding is performed to maintain absorption capacity, then absorption solution quality is preserved, but loss of substance increases and operational costs rise

Engineering Contradiction:
Improveabsorption solution qualityVSAvoidabsorption solution consumption
Core Design Contradiction:
Quantity of substanceVSLoss of substance

Solution Approach 1:

SOx and NOx contaminants are removed in advance in the gas conditioning unit before the gas enters the CO2 absorption unit. This preliminary action prevents contamination of the absorption solution, eliminating the need for bleeding to maintain solution quality and thereby reducing absorption solution consumption and operational costs.

Inventive Principle:
Principle #10Preliminary action

4Productivity

If flue gas is cooled before CO2 absorption, then absorption efficiency is improved, but water vapour condensation occurs and may cause precipitation

Engineering Contradiction:
ImproveCO2 absorption efficiencyVSAvoidprecipitation formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

SOx and NOx contaminants are removed before the cooling and CO2 absorption steps. By eliminating these contaminants in advance, the harmful effect of precipitation formation during cooling is prevented, allowing the gas to be cooled efficiently to improve CO2 absorption without suffering from precipitation issues.

Inventive Principle:
Principle #10Preliminary action

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 enhances SOx removal efficiency, reduces the environmental impact, and minimizes the consumption of alkaline solutions, thereby improving CO2 capture performance and reducing operational costs by recycling waste streams and utilizing sulfates as a by-product.

Implementation Method 1

contacting, in a treatment unit, the gas with a cooled alkaline aqueous solution comprising water and a carbonate of an alkali metal... thereby causing... absorption of the SOx in the carbonate-containing solution

Methodology Applied
Scientific EffectChemical absorption: Absorption (physical)

Implementation Method 2

contacting, in a treatment unit, the gas with a cooled alkaline aqueous solution... having a temperature lower than the initial gas temperature, thereby causing cooling of the gas, condensation of some water vapour

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS11731078B2SO<sub>x </sub>capture using carbonate absorbent
Publication Date: 2023.08.22 SAIPEM SPA
  • US11731078B2 patent drawing
  • US11731078B2 patent drawing
  • US11731078B2 patent drawing

AI summary

A desulfurization gas process includes water vapor, CO2 and SOx (x=2 and/or 3). In a treatment unit, the gas contacts a cooled alkaline aqueous solution having a temperature lower than an initial gas temperature, water and a carbonate of an alkali metal, to cool the gas, condense some water vapor and absorb SOx in the carbonate-containing solution, produce an SOx-depleted gas and an acidic aqueous solution including sulfate and/or sulfite ions. The SOx-depleted gas and a portion of the acidic aqueous solution can then be withdrawn from the treatment unit. Carbonate of the alkali metal can be added to remaining acidic aqueous solution to obtain a made-up alkaline aqueous solution. This solution can be cooled and reused as the cooled alkaline aqueous solution. An SOx absorbent solution includes a bleed stream from a CO2-capture process, sodium or potassium carbonate, and an acidic aqueous solution obtained from desulfurization.