Biogas is one of the green energy resources. To enhance
usage of
biogas (64.0 mol % CH4/CO2) and reduce the greenhouse
effect, CH4 purification by the hydrate-based gas separation
(HBGS) technology was studied in this work. Green solvent ionic liquid
[BMIm] Br and thermodynamic promoter tetrabutylammonium bromide (TBAB)
were added as hydrate additives to investigate their influence on
hydrate formation. [BMIm] Br has an inhibition effect on CH4 and CH4/CO2 hydrate phase equilibrium. The
combination of [BMIm] Br and TBAB decreased CH4/CO2 hydrate phase equilibrium pressure under identical temperature.
Kinetics of CH4 and CO2 hydrate formation in
[BMIm] Br solution were investigated. Gas uptake in the hydrate phase
increased when [BMIm] Br concentrations changed from 1000 to 2000
and 3000 ppm. The influence factors of gas–liquid ratio, temperature,
pressure, and concentration on biogas hydrate separation were studied.
Separation results were analyzed based on CH4 mole fraction
in the residual gas, CH4 recovery, separation factor, phase
equilibrium constant, and hydrate ratio of CH4 and CO2. CH4 in residual-phase gas can be enriched from
initial 64.00 to 79.13 mol %, and the maximum CH4 recovery
was 85.19%. For the combination of TBAB and [BMIm] Br on simulated
biogas hydrate separation study, the CH4 value in residual
gas was enhanced to 76.96 mol % and CH4 recovery was above
90%. The synergistic effect of TBAB + [BMIm] Br was not obvious compared
to the result in pure [BMIm] Br solution, and gas storage in the hydrate
phase decreased on the whole.