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Mass and energy balance equations are used to model the membrane enhanced steam reformer.
A simplified analytical first-order mode is chosen to model the membrane oscillation.
A gradient-augmented level set method is used to model the membrane motion.
In our model, the membrane is viewed as an entangled network of chains interacting at their backbone and ionic groups.
The design is formulated as a nonlinear programming problem where the set of algebraic and differential equations that model the membrane separation processes are included as equality constraints.
To increase lipid dynamics while preserving the atomistic detail of protein lipid interactions, in the highly mobile membrane-mimetic (HMMM) model the membrane core is replaced by an organic solvent, while short-tailed lipids provide a nearly complete representation of natural lipids at the organic solvent/water interface.
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In the equilibrium model, the membranes and CO2 removal are located in separate vessels downstream of the reformer.
According to the most probable docking model, the membrane-distal end of the lipid-transfer tunnel is in the vicinity of the hydrophobic pocket in VP1.
A hypothetical chemisomotic model of azo respiration is shown in Fig. 1 In this model the membrane-associated, cytoplasmic-oriented formate dehydrogenase or hydrogenase is the primary dehydrogenase.
The Hodgkin–Huxley nerve fiber model is used for modeling the membrane potential behavior.
Regression equations fitted to solutions of differential equations are employed for modeling the membrane modules.
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