Hello,
I am a student trying to use IECM to study economic analysis of Oxy-Combustion of Lignite coal in a Circulating Fluidized Bed and compare it with amine-based plants. My goal is to find out ways to simulate the oxy-CFB by IECM. So I have used available configuration of the oxy-PC system.
We found data on the relative cost of CFBR and PC, to be able to use retrofit and/or amortization factors to scale the PC costs appropriately. But, if we wanted to use CFBR, for example, efficiency, the amount of flue gas (equipment sizes), emissions or other similar parameters may have a different composition from the PC boiler system. Is there a way to account for these changes? which plant components are not significantly affected when simulating the oxy-CFB by IECM? How would we implement that if the setting is not available in the configuration?
Thank you.
19 Temmuz 2019 Cuma 15:28:35 UTC+3 tarihinde Karen Kietzke, Research Programmer, IECM, CMU yazdı: