Mass transfer coefficients are crucial in understanding how substances move between phases. They help quantify the rate of transfer, accounting for resistances in bulk phases and at interfaces. This knowledge is key for designing and optimizing separation processes in various industries.
Overall mass transfer coefficients combine individual phase resistances, simplifying complex transfer phenomena. By using these coefficients, engineers can predict transfer rates, design equipment, and improve process efficiency in applications like absorption, extraction, and membrane separations.
Overall Mass Transfer Coefficients
Definition and Interpretation
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Gas–liquid phase equilibrium of a model Langmuir monolayer captured by a multiscale approach ... View original
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Gas–liquid phase equilibrium of a model Langmuir monolayer captured by a multiscale approach ... View original
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Gas–liquid phase equilibrium of a model Langmuir monolayer captured by a multiscale approach ... View original
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Overall mass transfer coefficients represent the combined resistance to mass transfer across multiple phases or layers (gas-liquid or liquid-liquid interfaces)
Account for the individual mass transfer resistances in series, including the resistances in the bulk phases and the interface
Expressed in units of per unit (mol/(m²·s) or kg/(m²·s))
Depend on the specific system and operating conditions
Driving force for mass transfer typically expressed as a concentration difference or partial pressure difference between the bulk phases
Application and Significance
Used to quantify the rate of interphase mass transfer
Essential for the design and analysis of mass transfer equipment (absorption columns, extraction columns, membrane contactors)
Determine the required interfacial area or contact time to achieve a desired separation or purification performance
Calculated from experimental data (inlet and outlet concentrations, flow rates) to assess the performance and identify potential improvements
Used in the scale-up and optimization of mass transfer processes, investigating the effects of process variables (temperature, pressure, flow rates) on the overall mass transfer rate
Deriving Overall Mass Transfer Coefficients
Resistance-in-Series Model
derived by considering the individual mass transfer resistances in series, similar to electrical resistances in series
For a two-phase system (gas-liquid or liquid-liquid), the overall mass transfer coefficient is related to the individual phase mass transfer coefficients by: 1/K=1/k1+1/k2
K is the overall mass transfer coefficient
k1 and k2 are the individual phase mass transfer coefficients
Individual phase mass transfer coefficients (k1 and k2) estimated using appropriate correlations or models (, , surface renewal theory)
When one phase resistance is significantly larger than the other, the overall mass transfer coefficient is primarily determined by the limiting phase resistance, and the expression can be simplified accordingly
Equilibrium Relationships
Derivation of the overall mass transfer coefficient requires knowledge of the equilibrium relationship between the phases
Gas-liquid systems: Henry's law
Liquid-liquid systems: partition coefficients
Equilibrium relationships are essential for determining the driving force for mass transfer and relating the concentrations in different phases
Calculating Overall Mass Transfer Coefficients
Gas-Liquid Systems
Individual gas-side and liquid-side mass transfer coefficients (kg and kl) determined using appropriate correlations or experimental data
Overall mass transfer coefficient expressed in terms of the gas-side or liquid-side concentrations, depending on the controlling resistance and the equilibrium relationship (Henry's law)
Example: Absorption of a solute from a gas phase into a liquid phase, where the liquid-side resistance is controlling and Henry's law applies
Liquid-Liquid Systems
Individual liquid-phase mass transfer coefficients (k1 and k2) and the partition coefficient (m) between the two liquid phases are used
Partition coefficient (m) represents the equilibrium distribution of the solute between the two liquid phases and is determined by the solute's solubility in each phase
Example: Extraction of a solute from an aqueous phase into an organic solvent phase, where the partition coefficient determines the equilibrium distribution of the solute
Unit Consistency and Driving Force
Calculation of overall mass transfer coefficients requires consistent units for the individual phase mass transfer coefficients, concentrations, and partition coefficients
Appropriate driving force expression must be used, depending on the system and the equilibrium relationship
Driving force can be expressed as a concentration difference or partial pressure difference between the bulk phases
Applying Overall Mass Transfer Coefficients
Equipment Design
Overall mass transfer coefficients are essential for the design of various mass transfer equipment (absorption columns, extraction columns, membrane contactors)
Used to determine the required interfacial area or contact time to achieve a desired separation or purification performance
Overall mass transfer coefficient, along with the driving force and interfacial area, determines the rate of mass transfer and the overall efficiency of the mass transfer process
Design requires knowledge of the system geometry, flow patterns, and operating conditions, as well as the appropriate mass transfer correlations and models
Process Analysis and Optimization
Overall mass transfer coefficient can be calculated from experimental data (inlet and outlet concentrations, flow rates) to assess the performance of existing mass transfer equipment and identify potential improvements
Used in the scale-up and optimization of mass transfer processes
Effects of process variables (temperature, pressure, flow rates) on the overall mass transfer rate are investigated and optimized
Example: Optimizing the operating conditions of an absorption column to maximize the removal efficiency of a pollutant from a gas stream, considering the effects of temperature, pressure, and liquid-to-gas ratio on the overall mass transfer coefficient and the driving force