Dynamic Tray Model for Separation Processes in Mosaic System
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Explore the definition of system boundaries, equations, and variables in a dynamic tray model for separation processes using Mosaic system. This model includes mass, energy, component, and momentum balances, as well as auxiliary equations for phase equilibrium.
Dynamic Tray Model for Separation Processes in Mosaic System
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Presentation Transcript
Definition of the system boundaries Lj-1 Xi,j-1 Lj-2 Yi,j Vj Vj-1 j-1 hj-1L j hjV Tj ; pj Vaporphase Liquidphase Vj Lj-1 j Vaporphase hjF Fj Vaporphase Interficial Area Feed Liquidphase Liquidphase Z(Y or X)i,j Lj j+1 Vj+1 Lj Vaporphase hjL Vj+1 hj+1V Xi,j Liquidphase Yi,j+1 . . . Lj+1 Vj+2 Distillate Qj Feed One Tray: Qj Bottom product
Definition of the system boundaries Lj+1 Xi,j+1 Lj+2 Yi,j Vj Vj+1 j+1 hj+1L j hjV Tj ; pj Vaporphase Liquidphase Vj Lj+1 j Vaporphase hjF Fj Vaporphase Interficial Area Feed Liquidphase Liquidphase Z(Y or X)i,j Lj j-1 Vj-1 Lj Vaporphase hjL Vj-1 hj-1V Xi,j Yi,j-1 Liquidphase . . . Lj-1 Vj-2 Distillate Qj Feed One Tray: Qj Bottom product
Equation system of a tray 1. Mass balance 2. Energy balance 3. Component balance 4. Momentum balance? 5. Auxiliary equations(e.g. Phase equilibrium) yj,i Lj+1 xj+1,i Vj pj+1 Tray j: hj+1L Tj+1 hjV Fj hFj Qj Tj pj HUj xFi,j Connector: V=G F=Feed In MOSAIC not theposition of Indices areimportentonly thename Vj-1 hjL Tj-1 Lj yj-1,i xj,i pj-1 hj-1V
Literature: Component Material balance 0 = Lj+1 + Gj-1 - Lj - Gj 0 = Lj+1 xLj+1,i + Gj-1 xVj-1,i - LjxLj,i - GjxVj,i + FjxF,j,i 0 = Lj+1 hLj+1,i + Gj-1 hVj-1,i - LjhLj,i - GjhVj,i + FjhF,j,i ∑ x j,i -1 = 0 ∑ y j,i -1 = 0 y j,i= Kj,ixj,i
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