By adding 5.0 wt% f-BN nanosheets, the maximum mass loss rate, peak heat release rate (pHRR), and smoke produce rate (SPR) were decreased by 20.8 %, 68.0%, and 53.6%, respectively.
It was verified that for any given catalyst mass flow rate, there exists an optimum value for the catalyst to oil mass flow rate ratio, COR, for maximum mass flow rate production of gasoline, or any other desired product.
The temperatures corresponding to the maximum mass loss rate were also increased with the increasing of heating rate (Table 2).
From Equation (21), it can be deduced that the fluid mass flow rate increases as the collector tilt angle increases; the maximum mass flow rate occurs at θ = 90° for any given length of the pipe.
At the fixed total chimney length, the air mass flow rate also varied with the length ratio of the vertical to inclined section, and the maximum mass flow rate can be achieved by choosing the longest vertical length within the restriction of the building code.
Instability maps were also constructed using the criterion of maximum mass transport rate per unit volume.
The ratio height/radius, maximum mass flow rate and maximum power under the constraints of a fixed area and volume are determined.
The values of maximum mass loss rate decreased roughly with increasing filler weight fraction, while the influence of the filler diameter and length diameter ratio on the maximum mass loss rate was insignificant.
As shown, virgin asphaltene decomposition started at approximately 310 °C and finished at approximately 660 °C with a maximum mass loss rate at approximately 448 °C.
The study of kinetics showed well applicability of pseudo second order kinetic model with maximum mass transfer rate in adsorption process.
