Hybrid process merges flue gas with reject brine using an amine mediator to resolve slow absorption rates and high capital costs.
A furan skeleton iminoguanidine derivative acts as an acidic gas absorbent with mild reaction conditions.
Divides tail gas into streams for acid-gas removal and fermentor recycling, resolving mass-transfer limitations that inflate reactor size.
Nickel composite catalyst minimizes coke formation and sulfidation to maintain activity during thermo-neutral reforming of heavy fuels.
Using insoluble metal oxide reactants to form dense SOD frameworks, eliminating large cages that reduce carbon dioxide adsorption.