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Our results show that for a given chemical, a lower solution freezing point provides a larger driving force for diffusion and results in faster melting.
Thus, while higher transmembrane pressure provided a larger driving force for water transport, this driving force was counteracted by a higher resistance caused by cake layer compression.
The latter reaction, as compared to the first one, is driven by a larger driving force and thus the extent of the discontinuous transformation increases considerably with decreasing Cr/Mo-ratio.
The simulation results show that the multistage reactors have better mass and heat transfer, a lower rate of oxygen consumption, higher operating temperatures of the H2 membrane, and a larger driving force for hydrogen permeation, and hence can produce more than three times the amount of pure hydrogen than the single-stage reactor.
A larger driving force for ET would presumably seem to favor a sequential ET/PT mechanism.
This can be explained considering that the Cu3P → InP conversion requires a larger driving force in order to take place and optimized reaction conditions are necessary.
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The permeance method is used to obtain a large driving force for the actuator.
First, the addition of a small amount of NaBH4 solution results in a large driving force of redox reaction, and favors nucleation burst.
An average temperature difference of nearly 125 °C provides a large driving force for radiation heat transfer from the stack to the cylindrical enclosure surrounding the tube bundle.
We established that Zn has a large driving force (−0.19 eV atom−1) for segregation from the Al bulk to the asymmetrical grain boundary site, and its segregation reduces the grain boundary strength slightly.
Despite the urgency of creating a sustainable solution for End Of Life (EOL) concrete waste treatment, there has not been a large driving force for recycling it into prime grade materials.
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