Multiphase CO2 Dispersions in Microfluidics: Formation, Phases, and Mass Transfer

TL;DR

This study investigates high-pressure CO2 microfluidic dispersions, revealing complex multiphase dynamics and quantifying CO2 mass transfer, which are vital for applications like carbon capture and microreactors.

Contribution

The paper introduces a high-pressure microfluidic method to analyze CO2 mass transfer and multiphase behavior near the phase boundary, providing new insights into CO2 dissolution processes.

Findings

Multiphase CO2 dispersions observed near phase boundary.

Quantified CO2 dissolution rate and volumetric mass transfer coefficient.

Identified factors influencing mass transfer such as specific area and dispersion speed.

Abstract

The dissolution and microfluidic mass transfer of carbon dioxide in water at high-pressure conditions are crucial for a myriad of technological applications, including microreactors, extractions, and carbon capture, utilization, and sequestration (CCUS) processes. In this experimental work, we use a high-pressure microfluidic method to elucidate the mass transfer process of CO2 in water at high pressure. An intriguing multiphase CO2 flow and dispersions are observed when operating at the pressure-temperature ($P$-$T$) condition close to the CO2 gas-liquid phase boundary ($P=6.5$ MPa and $T=23.5\pm 0.5~^{\circ}$C). We propose a series of strategies to unravel this complex multi-phase dynamics by calculating each phase's volume and mass change in a gas-liquid coexistent CO2 dispersion, estimating the possible CO2 concentration change in water, and comparing with the CO2 solubility data. Finally, we quantify the CO2 mass transfer by directly calculating the CO2 dissolution rate in water and estimating the volumetric mass transfer coefficient ($k_{L}a$). The results show that the mass transfer may be influenced by the specific area ($a$), CO2 concentration gradient in the water slug, and the traveling speed of a dispersion.