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The films investigated in this study are grown by chemical bath deposition (CBD) at different temperatures and the doping was conducted for a fixed impurity concentration.
In order to calculate the reactor volume required for its cost evaluation, a one dimensional homogenous model, based on the chemical kinetics of tri-reforming reactions is conducted for a fixed bed reactor.
To this end, a mesh sensitivity study was conducted for a fixed transition size of a = 0.1 μm and mesh density ranging from 0.1 to 100 mesh elements per transition size (i.e. a unitless dimension) for contact angles of 10° to 85°.
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The MRS where the research was conducted used a fixed platform train driving simulator for training purposes.
For this purpose, the pyrolysis of biomass was conducted in a fixed bed reactor allowing a good control of pyrolysis conditions.
Pyrolysis was conducted in a fixed bed reactor.
Meta-analysis was conducted using a fixed effects model.
The curve fitting procedure was conducted simultaneously on a fixed number n of experimental thermograms.
Given this, OWSA was conducted for some of the fixed parameters such as the discount rate, number of follow-ups in a year.
For a fixed ({P_{m}^{max }}), we conduct the proposed scheme and the schemes proposed in [12, 16], respectively.
for a fixed integer.
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