Abstract:
The flowsheet simulation model of the cellulosic ethanol miniplant with the capacity of 1 kg/d ethanol production from corn stover and the physical property database were developed on the Aspen plus platform. The mass balance and energy balance of the miniplant process were calculated and the results show that, producing 1 kg cellulosic ethanol required 2.595 7 kg fresh water and 3.605 4 kg stream, 8.061 6 kg waste water under the maximum productivity of the cellulosic ethanol miniplant, which was lower than the consumption of the corn based ethanol process; required energy input 36.515 2 MJ and generated 53.574 9 MJ, which means that the energy generation was greater than the energy consumption; the integrated energy consumption was 1.826 9 kg standard coal, while the energy generation during this process was 1.828 0 kg standard coal, which suggested that there was an energy balance between the output and the input.