Potassium Carbonate CO2 Separation in Gas Turbine Recycle Loops
Find Innovative SolutionsGenerate Solutions
Solution Overview
Problem
Current methods for low emission power generation and CO2 capture are inefficient and costly, particularly in gas turbine power plants, due to high CO2 concentration in exhaust gases and the presence of volatiles which can lead to corrosion and safety hazards when used for enhanced oil recovery or sequestration.
Innovation Solution
A low emission power generation system incorporating an exhaust gas recycle loop and potassium carbonate (K2CO3) separation system, which recycles exhaust gases to separate and recover CO2, and removes volatile components before regeneration, producing high purity CO2 with minimal contaminants.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Reliability
If amine solvent absorption is used to capture CO2, then CO2 capture capability is improved, but the presence of oxygen, sulfur oxides, and nitrogen oxide causes solvent degradation and operational problems
Solution Approach 1:
The patent employs potassium carbonate solvent which can be continuously regenerated and reused, effectively treating it as a durable capture medium that withstands harsh exhaust conditions without degrading like amine solvents would
Solution Approach 2:
The patent changes the chemical parameters of the absorption system by using potassium carbonate instead of amine solvents, and operates at elevated temperatures and pressures to maintain solvent stability in the presence of oxygen, sulfur oxides, and nitrogen oxide
2Quantity of substance
If CO2 is captured from low concentration exhaust streams, then CO2 recovery is achieved, but large volume of gas must be treated at low pressure resulting in high capture costs
Solution Approach 1:
The patent applies preliminary compression to increase the pressure of the exhaust gas stream before CO2 capture, and uses heat exchangers to pre-condition the gas, thereby reducing the overall energy and cost requirements for CO2 separation and purification
Solution Approach 2:
The patent employs compression and pressure manipulation techniques to concentrate the CO2 stream, using pneumatic systems to increase pressure and reduce volume, making the subsequent separation and capture processes more economically viable
3Productivity
If volatile components are present in recovered CO2, then CO2 recovery efficiency is maintained, but corrosion rates increase and safety hazards arise for EOR and sequestration applications
Solution Approach 1:
The patent extracts and removes volatile components from the recovered CO2 stream through selective separation processes, isolating the harmful volatiles from the CO2 to prevent corrosion and safety issues while maintaining CO2 recovery efficiency
Solution Approach 2:
The patent may employ porous materials or adsorbents that selectively trap volatile components while allowing CO2 to pass through, thereby purifying the CO2 stream without sacrificing recovery efficiency
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 power generation efficiency, reduces costs, and produces high purity CO2 suitable for enhanced oil recovery and sequestration by utilizing a potassium carbonate-based system to capture and purify CO2 while minimizing volatile contaminants.
Implementation Method 1
a first separation system that employs a potassium carbonate-based solvent to absorb and recover CO2
Implementation Method 2
a stripping section that removes volatile components from the bicarbonate solvent solution
Implementation Method 3
a regeneration section that releases CO2 from the bicarbonate solvent
Data Source
AI summary
Methods and systems for CO2 separation in low emission power plants are provided. One system includes a gas turbine system that combusts a fuel and an oxidant in the presence of a compressed recycle stream to provide mechanical power and a gaseous exhaust. A purge stream is taken from the compressed recycle stream and directed to a CO2 separator configured to absorb CO2 from the purge stream using a potassium carbonate solvent. Volatiles are removed from the rich solvent by stripping or by flashing to an intermediate pressure before the rich solvent is regenerated and CO2 is removed.


