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Steady-state analyses reveal that the fuel feed flow rate with fixed steam-to-carbon and air-to-carbon ratios is an ideal manipulated variable.
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The effect of increasing sweep flow rates on the oxygen permeation for constant fuel and feed flow rates is presented in Fig. 14.
The dimensionless parameter is proposed as a sharp a' priori waste 'fingerprint', determining the necessary increase or decrease of manipulated variables (recuperation ratio, excess air, auxiliary fuel feed rate, auxiliary air flow) in order to balance the HWI and maximize throughput under uncertainty in received wastes.
Improving a power unit efficiency results in a reduction in fuel and steam consumption per unit which involves a reduction in the mass flow of burned fuel, feed water and other combustion products: slag and ash.
The reactor performance was investigated under various operating conditions, such as ammonia flow rate in the decomposition channel, combustible feed flow rate, and fuel equivalence ratios.
The best operating conditions were obtained at ammonia flow rate of 0.4 NLPM, combustible feed flow rate of 0.8 NLPM, and fuel-rich operation corresponding to fuel equivalence ratio of 1.2.
This indicates that there is no significant impact of feed flow rate on the evaporation of fuel in the sweep side.
Figure 7 presents the variations in the maximum temperature obtained in the reaction with the rise in the feed flow rate, keeping the sweep and fuel flow rate constant.
The response of a fuel cell system depends on the air and hydrogen feed, flow and pressure regulation, and heat and water management.
The effect of increasing the feed flow rate on the oxygen permeation for constant fuel and sweep flow rate is presented in Fig. 6.
The model is used principally to account for the effect of variations in the furnace fuel flow rate and the influence of changes in the feed temperature and feed flow rate on the furnace effluent temperature.
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