A fundamental
study on hydrate formation from an equimolar CO2–CH4 gas mixture has been carried out with
two focal points: accelerating the kinetics of hydrate formation and
enhancing the gas separation efficiency of the process. To this effect,
the impact of inducing different hydrate structures from the same
gas mixture by introducing suitable additives into the system has
been investigated, and experiments are being carried out in a horizontal
packed bed reactor at two different initial pressures, 3.5 and 5.0
MPa, to study the effect of driving forces on the kinetics of hydrate
formation and the separation efficiency of the process. sH hydrate
former cyclooctane (Cyclo-O) induces rapid nucleation of hydrate and
also yields significant gas uptake in hydrates, 29.55% higher compared
to the water system. This may be attributed to the simultaneous formation
of sH and sI hydrates when Cyclo-O is present in the system. It was
observed that the environmentally benign hydrophobic amino acid tryptophan
in low concentration (1 wt %) can effectively accelerate the kinetics
of hydrate formation, with 90% water to hydrate conversion being obtained
within the first 30 min of hydrate formation. Further, the use of
Cyclo-O and tryptophan together shows a synergistic effect, resulting
in the highest gas uptake among all the systems studied. Although
the problem of slow kinetics of hydrate formation from CO2–CH4 gas mixtures has been satisfactorily solved
through this work, there are still significant strides that need to
be made toward improving the separation efficiency of the process.
The formation of the mixed hydrate is unable to return a satisfactorily
high efficiency for gas separation.