Phase transitional absorption method

Chemistry of inorganic compounds – Modifying or removing component of normally gaseous mixture – Carbon dioxide or hydrogen sulfide component

Reexamination Certificate

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C423S226000, C423S228000, C423S234000, C423S242100, C423S242200, C423S242700, C423S243010, C423S243080, C423S243110, C423S243120, C423S24000R, C423S243060

Reexamination Certificate

active

07541011

ABSTRACT:
The present invention is directed to an improved method and system for separating and purifying gas using gas-liquid absorption. According to this invention, the method is carried out in an absorber, where a liquid absorbent, a gas mixture containing a gas to be absorbed were introduced from an inlet. During absorption, the second liquid phase was separated out from the absorbent. The absorbed gas was accumulated in one of liquid phases. After absorption, two liquid phases were separated. One of the liquids with rich absorbed gas was forward to regenerator. After regeneration, the liquid was cycled back to absorber. The liquid phase with lean absorbed gas was back to absorber directly to complete the cycle.

REFERENCES:
patent: 6969418 (2005-11-01), Hu
patent: 2007/0286783 (2007-12-01), Carrette et al.
Howard Herzog et al.; Co2 Capture, Reuse and Storage Technologies for Mitigating Global Climate Change; DOE Order No. DE-AF22-96PC01257; Jan. 1997; 70 pages; Cambridge, MA, US.
James T. Yeh et al.; Semi-batch Absorption and Regeneration Studies for Co2 Capture by Aqueous Ammonia; Fuel Processing Technology 86 (2005); pp. 1533-1546; Pittsburgh, PA, US.
Kevin P. Resnik et al.; Aqua Ammonia Process for Simultaneous Removal of Co2, So2, and NOx; International Journal of Environmental Technology and management vol. 4, Nos. 1/2, 2004; 19 pages; US.
Dr. R.H. Niswander et al.; A More Energy Efficient Product for Carbon Dioxide Separation; Separation Science and Technology, 28(1-3); 1993; pp. 565-578; Freeport, TX, US.

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