The effect of channel height, inlet steam-to-carbon ratio, wall thermal conductivity, catalyst, and flow rate were explored to provide guidelines for optimal design.
The influences of system parameters including the temperature, channel height, inlet velocity, and inlet pressure on the diffusion of oxygen in GDL are also examined systematically.
In this paper, we discuss seven types of exchangers (A, B, C, D, E, F and G), which vary in inlet nozzle configuration, header height, inlet pipe diameter and tube pass distribution.
In the present work the effects of three key parameters, the channel height, the inlet mass flux and the equivalence ratio of the inlet mixture on the interaction between the gas phase and surface reactions are explored.
Under two experimental conditions, i.e. with and without direct air intake in the cavity, the influence of the mainstream air flow velocity, the air intake velocity in the cavity, the height of inlet channel, the structure of holder and the structural proportion of the cavity on entrainment in the cavity is studied, respectively, through experiment at atmospheric temperature and pressure.
The effects of initial bed height and inlet gas velocity on the fuel mixing are investigated.
Finally, a new three-dimensional Bump-integrated IWI was tested in M = 6 wind tunnel, under a rather thick boundary layer upstream flow (37% height of inlet entrance).
Total pressure drop and average wall heat flux are calculated for different flow rates and the effects of changing the microchannel height, flow inlet angle, and working fluid are investigated.
The natural ventilation rate and heat transfer rate have been found to vary with the total heat input, heat distribution on the cavity walls, cavity width and height and inlet opening position.
In the structural modelling of the heat sink, channel width, fin width, channel height and inlet velocity are defined as the design variables, 'total thermal resistance' and the 'pressure drop' as the two objectives, subject to constraints of fixed length and width of the heat sink.
The results for different solution flow rates are shown for fixed bed height and inlet adsorbate concentration in Fig. 9a, b.
