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MESH Material balance, Equilibrium. Summation

These four equations are the so-called MESH equations for the stage Material balance, Equilibrium, Summation and Heat (energy) balance, equations. MESH equations can be written for each stage, and for the reboiler and condenser. The solution of this set of equations forms the basis of the rigorous methods that have been developed for the analysis for staged separation processes. [Pg.498]

MESH equations A set of equations used for calculating the material, energy, and thermodynamic profiles within a distillation column. They combine material balances, equilibrium conditions, summation conditions, and heat balances, which are required to... [Pg.235]

Tne MESH Equations (the 2c + 3 Formulation) The equations that model equilibrium stages often are referred to as the MESH equations. The M equations are the material balance equations, E stands for equilibrium equations, S stands for mole fraction summation equations, and H refers to the heat or enthalpy balance equations. [Pg.30]

Simulation of multicomponent rectification is based on the so-called MESH equations (M = material balances, E = equilibrium, S = summation of mole fractions, H = heat balance) formulated for a single equilibrium stage (Fig. 5.2-33) as follows ... [Pg.281]

Rigorous models of staged distillation processes are formulated by setting up material balance equations, equilibrium relations, summation equations, and enthalpy balance equations (MESH equations). In these models, the extent of nonlinearity may be very severe, particularly for azeotropic and reactive distillation systems. MESH system based mathematical models can thus yield multiple solutions (multiple steady states), a fact which has been observed by many researchers. [Pg.617]


See other pages where MESH Material balance, Equilibrium. Summation is mentioned: [Pg.149]    [Pg.149]   


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Material balance

Material balancing

Meshes

Summation

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