Abstract Carbon dioxide (CO2) sequestration, storage and recycling will greatly benefit from
comprehensive studies of physical and chemical gas–liquid processes involving CO2. Over …

Thermophysical properties of fluid systems are highly desirable as they are used in many
industrial processes both from a chemical engineering point of view and to push forward the …

Based on the online method, the absorption kinetics and mass transfer of CO 2 in potassium
carbonate solution in a serpentine minichannel are studied. Three flow patterns are …

Characteristics of gas-liquid Taylor flow with different liquid viscosities are investigated in a
rectangular microchannel, aiming at providing knowledge and aid in the design of …

Heretofore, the microchannel junction angle θ dependent behavior on Taylor flow with a
vertical squeezing route lacks a comprehensive understanding. An experimental study was …

In industrial post-carbon capture processes, monoethanolamine (MEA) has been mainly
used as an absorption solvent. However, this approach generates significant amounts of …

We present a theoretical model to calculate the volume of non-wetting bubbles and droplets
in segmented microflows from given dimensions of the microchannel and measured lengths …

We investigate the coupled dynamics of fluid mixing and viscously unstable flow under both
miscible (single‐phase) and partially miscible (two‐phase) conditions, and in both …

Mass transfer occurs in many simple and complex processes. As mass transfer persists
across the interface separating immiscible fluids, the proper determination of the interfacial …

Two-phase liquid-gas Taylor flow triggered by blocking-squeezing mechanism was studied
with different junction angle θ microchannels, ie 20°, 45°, 90°, 135° and 160°, at various …