Verify the values given in Table 5.3 for NV, NE, and ND for a stream mixer and a streamdivider.

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Ne Independent Relationships No. Degrees Element or Unit Name Ny, Total Number of of Freedom Variahles Schematic (C + 3) Total boiler (reboiler) (C+ 4) (2C + 7) (a) (C+ 4) (C + 3) Total condenser (2C +7) (b) (2C +6) (C+4) Partial (equilibrium) boiler (reboiler) (3C + 10) (c) "Lout (3C + 10) (2C +6) (C+4) Partial (equilibrium) (di Va condenser (2C +5) Adiahatic equilibrium (2C +7) (4C + 12) (e) Vaut ln stage Vin aun (2C +7) (2C +6) Equilibrium stuge with (4C + 13) Vaun lin heat transfer Vin, Laun (2C + 8) (3C +8) Equilibrium feed stage (5C + 16) (e) with heat transfer and feed Vin Lau (h) Equilibrium stage with beat transfer and (SC + 16) (3C +9) (2C +7) Veut hin sidestream Vin Lu (2N + 20 +5) (7N +2NC + 2C + 7) (SN + 2NC + 2) (i) N-connected equilibrium stages with heat transfer Stage N 0, Qu-1 Stage 1 Va laut Stream mixer (C+4) (2C + 6) (3C + 10) (2C +5) (k) Srearn divider (3C + 10) (C +5)