Question: Verify the values given in Table 5.3 for NV, NE, and ND for a partial reboiler and a totalcondenser. Ng. Independent Relationships Ny, Total Number

Verify the values given in Table 5.3 for NV, NE, and ND for a partial reboiler and a totalcondenser. Ng. Independent Relationships Ny, Total Number of No. Degrees of Freedom Element

Ng. Independent Relationships Ny, Total Number of No. Degrees of Freedom Element or Unit Name Variables Schematic (C + 3) Total boiler (reboiler) (C + 4) (2C + 7) (a) (C + 4) Total condenser (2C + 7) (C + 3) (b) (2C + 6) (C+ 4) Partial (equilibrium) boiler (reboiler) (3C + 10) (c) "Lout (C+ 4) (2C + 6) Partial (equilibrium) (3C + 10) (d) condenser (2C +7) (2C + 5) Adiabatic equilibrium stage (4C + 12) (e) Vaut fin Vin lgun (2C +7) Equilibrium stage with (4C + 13) (2C +6) Vaun lin heat transfer Vin Lau Equilibrium feed stage (2C + 8) (3C + 8) (5C + 16) (8) Vaut lin with heat transfer and feed Vin Laun Equilibrium stage with heat transfer and (SC + 16) (3C + 9) (2C +7) (h) Veut kin sidestream Vin Fut (7N + 2NC + 20 + 7) (i) N-connected (SN + 2NC + 2) (2N + 2C + 5) V equilibrium stages with heat transfer Stage N 0n ON-1 Stage 1 Q Va lut (2C +6) Stream mixer (C + 4) (3C + 10) (k) Stream divider (3C + 10) (2C + 5) (C +5)

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