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The system performance is evaluated as a function of the steam to carbon ratio, fuel cell temperature, anode off gas recycle ratio and CO2 adsorption percentage.
The tracer concentration ratio can be expressed as a function of the steam fraction and the vapor-liquid distribution coefficient of the tracers.
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Analysis is performed as a function of the heating steam temperature, salinity of the intake seawater, and number of effects.
An empirical expression to predict the kinetic rate as a function of the degree of conversion, temperature, steam concentration, and hydrogen concentration was developed.
Simulation under changed operating conditions is conducted through the use of expressions that correlate the temperature and enthalpy of the steam as a function of the extraction pressure.
With the absolute pressure (and temperature) known as a function of the displacement, we can determine from the steam tables the amount of water vaporizing with increasing pressure.
Three actively constrained regions as a function of the main disturbances, namely, the fuel and steam feed rates, are identified; each region represents different sets of active constraints.
The model gives the entrainment ratio as a function of the expansion ratio and the pressures of the entrained vapor, motive steam and compressed vapor.
The models presented enable a quantitative description of steam-side and flue gas-side oxidation as a function of the design and operational parameters of the heating surface.
Their results show that the maximum HCl content, as a function of temperature and steam fraction, can reach up to 200 mg/kg.
The pitting potential of the surface treated with steam was a function of the vapour pressure of the steam.
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