in Wiley Online Library (wileyonlinelibrary.com).Recently a homogeneous liquid-phase ethylene oxide (EO) process with nearly total EO selectivity, catalyzed by methyltrioxorhenium with H 2 O 2 as an oxidant, was reported. Fundamental mass transfer and kinetic studies of this reaction are reported in the present work. Volumetric expansion studies revealed that the liquid reaction phase (methanol þ H 2 O 2 / H 2 O) is expanded by up to 12% by compressed ethylene in the 20-40 C range and up to 50 bars. This represents an increase in ethylene solubility by approximately one-order of magnitude, attributed to the unique exploitation of nearcritical ethylene (P c ¼ 50.76 bar; T c ¼ 9.5 C). Interphase mass-transfer coefficients for ethylene dissolution into the liquid phase were obtained experimentally. Operating at conditions that enhanced the ethylene solubility and eliminated interphase mass-transfer limitations maximized the EO productivity (1.61-4.97 g EO/h/g cat), rendering it comparable to the conventional process. Intrinsic kinetic parameters, estimated from fixed-time semibatch reactor studies, disclosed the moderate activation energy (57 AE 2 kJ/mol). (a) Ethanol þ methanol binary system; (b) (ethylene þ methanol þ 50 wt % H 2 O 2 /H 2 O) ternary system. Initial composition of liquid phase ¼ 0.748 mol methanol þ 0.134 mol H 2 O 2 þ 0.253 mol H 2 O. Initial volume of liquid phase ¼ 15 mL. The size of the plotted data points represents the experimental uncertainty. Ethylene P ¼ 50 bars; T ¼ 40 C; MTO amount ¼ 0.361 mmol; methanol ¼ 0.748 mol; H 2 O 2 ¼ 0.116 mol; H 2 O ¼ 0.220 mol; acetonitrile ¼ 0.0191 mol; pyridine N-oxide ¼ 2.19 mmol; batch time ¼ 5 h; agitation speed (Ä : 1,200 rpm, h: 400 rpm).