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The mole fraction of hydrocarbons was about 0.02, while the mole fraction of imines was 0.09.
You decrease the mole fraction of the less volatile material in the gas phase.
The composition of the solution (i.e., the mole fraction of NaCl) is another independent variable.
The mole fraction of AMPS were 0.2674 and 0.4318, respectively, with the same BIS mole fraction of 0.013.
Through increasing the mole fraction of pyridine, the pure phase of complex 2 was obtained.
However, the viscosities increase with mole fraction of DEAE up to 0.4 and becomes lower.
Pressure and temperature diagrams were developed at different mole fraction of methanol (xMeOH).
The mole fraction of n-butane in the liquid phase had high recovery ratio of 90%.
The mole fraction of water in the permeate ranged from 98.7%too 99.2% at 70 °C.
Also, the viscosities of all range of mole fraction of DEAE decrease as temperature increases.
The maximum mole fraction of H2 and CO reached 9.32% and 8.18% respectively.
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