Abstract

Hollow fiber membrane contactors (HFMCs) can effectively separate CO from post-combustion flue gas by providing a high contact surface area between the flue gas and a liquid solvent. Accurate models of carbon capture HFMCs are necessary to understand the underlying transport processes and optimize HFMC designs. There are various methods for modeling HFMCs in 1D, 2D, or 3D. These methods include (but are not limited to): resistance-in-series, solution-diffusion, pore flow, Happel’s free surface model, and porous media modeling. This review paper discusses the state-of-the-art methods for modeling carbon capture HFMCs in 1D, 2D, and 3D. State-of-the-art 1D, 2D, and 3D carbon capture HFMC models are then compared in depth, based on their underlying assumptions. Numerical methods are also discussed, along with modeling to scale up HFMCs from the lab scale to the commercial scale.

Highlights

  • In 2018, the Intergovernmental Panel on Climate Change issued a report detailing the irreversible impact of a global temperature rise of 1.5 ◦ C [1]

  • A common geometric configuration used in post-combustion carbon capture (PCC) is the hollow fiber membrane contactor (HFMC), and this particular design will be the focus of this review paper

  • This paper offers a comprehensive review of modeling studies to date for gas-liquid HFMCs for PCC

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Summary

Introduction

In 2018, the Intergovernmental Panel on Climate Change issued a report detailing the irreversible impact of a global temperature rise of 1.5 ◦ C [1]. Energy is required to strip CO2 from the solvent in a regeneration process, gas-liquid membrane contactors have several competitive advantages over other membrane configurations: no need to pressurize the flue gas (which requires a lot of energy), higher CO2 fluxes, no selective layer, and independent flow regulation [8]. Gas-liquid membrane contactors used in post-combustion carbon capture (PCC) are the focus of this review paper. A common geometric configuration used in PCC is the hollow fiber membrane contactor (HFMC), and this particular design will be the focus of this review paper. Experiments conducted in this field are often tailored to a unique set of membrane materials and operating conditions This makes it challenging to compare reported experimental results or determine the optimal membrane contactor design. Numerical approaches and modeling to assist scaling up HFMC technology are discussed

Fundamental Theory
Constitutive Laws
Governing Equations
One-Dimensional Modeling
Modeling Chemical Reactions in RIS
Modeling Membrane Wetting in RIS
Solution-Diffusion Model
Pore Flow Model
Two-Dimensional Modeling
Governing Equations for a 2D-Axisymmetric HFMC Fiber
Benefits of 2D Axisymmetric Modeling
Three-Dimensional Modeling
HFMC Modeling Road Map
Applications and Challenges
Applications of 1D Models
Applications of 2D Models
Applications of 3D Models
Software Implementations
Modeling Challenges
Scale-up Modeling from Lab Scale to Commercial Scale
Findings
10. Conclusions and Recommended Future
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