(87a) The Dry Gasification Oxy-Combustion (DGOC) Power Production Cycle Conference: AIChE Spring Meeting and Global Congress on Process SafetyYear: 2011Proceeding: 2011 AIChE Spring Meeting and Global Congress on Process SafetyGroup: Advanced Fossil Energy UtilizationSession: Carbon Capture/Separation From Gasification-Based Systems Time: Wednesday, March 16, 2011 - 8:00am-8:25am Authors: Walker, M. E., Illinois Institute of Technology Abbasian, J., Illinois Institute of Technology Chmielewski, D. J., Illinois Institute of Technology Castaldi, M. J., City College of New York Proposed is a novel coal conversion process, dubbed the “Dry Gasification Oxy Combustion Cycle” (DGOC), because of its unique two stage conversion process. Feed coal will be partially oxidized at very high pressures (60 bar) in an oxygen-blown gasification unit, using recycled flue gas as a gasification agent (≈62% CO2, 32% H2O b/v). This is in contrast to typical gasification systems that use steam as a gasification agent. In addition, the reducing environment of the gasifier will provide an opportunity to perform in situ sulfur removal through sorbent based capture. The second stage oxy-combustion unit will also utilize recycled flue gas; for flame temperature moderation. The oxy-combustion stage will provide energy to raise steam for power generation, while maintaining a process effluent that is very concentrated in CO2. This effluent stream, already at high pressure, will utilize ambient cooling to 1) flash out the water from the effluent stream and 2) condense remaining CO2 into a high purity liquid stream, ready for further compression and sequestration. Analysis of a preliminary design was carried out using process simulation models developed with Aspen Plus®. Results suggest that DGOC can achieve carbon capture and sequestration (CCS) goals with a 5.2% benefit to plant efficiency, when compared to oxy-combustion systems configured for this purpose. Results also suggest that DGOC will remain competitive against the IGCC process, in terms of efficiency and fresh water consumption.