This paper addresses the optimal
design of a clean ammonia synthesis
system based on biomass gasification coupled with a Ca–Cu chemical
loop (CCL), where biomass is adopted as the feedstock and ammonia
is considered as the final product. In the proposed system, the processes
of biomass gasification for syngas production, CCL for CO2 capture, and ammonia synthesis are highly integrated via mass and energy flows. The optimal operating parameters are determined
after exploring the effects of key parameters on the performance of
the proposed system by combining process simulations with sensitivity
analysis. Then, a two-step heat integration strategy including heat
exchanger network synthesis and waste heat recovery is conducted to
maximize the energy utilization efficiency of the whole system. Results
show that the proposed clean ammonia synthesis system can not only
guarantee higher CO2 capture efficiency (96.4%) and ammonia
synthesis capacity (0.281 kg NH3/kg wet biomass) by using
biomass, steam, and air as raw materials but also achieve self-sustained
energy demand to a great extent. The economic evaluation shows that
the investment cost of the system accounts for more than 90% of the
total annual cost, which is about 10 times the operating cost. In
addition, the cost of ammonia production is 486.01 $/ton NH3, which depends largely upon the price of biomass.