Distillation Column External Balance Lecture 10 1 Column

Distillation Column – External Balance Lecture 10 1

Column Distillation – Typical Specified Variables o Column pressure, Pc. o Feed flow rate, F. o Feed composition, z. o Feed temperature, TF; enthalpy, h. F; or quality, q = L/F. o Reflux temperature, TR; or enthalpy, h. D. o Reflux ratio, L/D; or distillate composition, x. D. o Bottoms composition, x. B. Lecture 10 2

Column Distillation – Tools for Solution o Equilibrium relationships o Mass balances o Energy balances Lecture 10 3

Column Distillation – External Balance o Column o Condenser o Reboiler Lecture 10 4

Distillation Column – External Balance Lecture 10 5

External Column Balances o Overall Eq. (4 -1) o Component Eq. (4 -2) o Energy Eq. (4 -5) Lecture 10 6

Distillate and Bottom Streams o Distillate Stream D Eq. (4 -3) o Bottoms Stream B Eq. (4 -4) Lecture 10 7

Condenser Conditions o o Partial – only part of the incoming vapor stream, V 1, is condensed. We have both vapor and liquid streams at saturated conditions. D is taken as a saturated vapor and the liquid reflux, Lo, is returned to the column as a saturated liquid. Both must be at saturated conditions since we have equilibrium – in fact the partial condenser is an additional equilibrium stage. We will look at partial condensers later. Total – all of the incoming vapor stream, V 1, is condensed to liquid. We then split the resulting liquid outlet into the distillate stream, D, and the reflux Lo, which is returned to the column. We will consider only total condensers for now. Lecture 10 8

Partial Condenser Lecture 10 9

Distillation Column – Total Condenser Lecture 10 10

Total Condenser – Important Note o The important thing to note for a total condenser is that the mole fraction, y 1, of the vapor stream from the top of the column is equal to both the mole fractions, x. D and xo, of the liquid streams! y 1 = x. D = x o o Eq. (4 -7) The condition of the outlet of the condenser has to be specified as either a saturated liquid or a subcooled liquid in order to use the energy balance. The state of the liquid determines the heat duty of the condenser. Lecture 10 11

Total Reboiler Lecture 10 12

Distillation Column – Partial Reboiler Lecture 10 13

Reboiler Conditions o o Partial – only part of the incoming liquid stream, L, is vaporized. We have both vapor and liquid streams exiting the reboiler at saturated conditions. B is taken as a saturated liquid and the boilup, Vn+1, is returned to the column as a saturated vapor. Both streams must be at saturated conditions since we have equilibrium in the reboiler – in fact the partial reboiler is an additional equilibrium stage. Total – the incoming liquid stream, L, is split first to obtain our bottoms stream, B, as a saturated liquid. It has to be a saturated liquid since it leaves the equilibrium stage at the bottom of the column. We then reboil all of the remaining liquid and return it to the column as a vapor stream, V. Lecture 10 14

Total Reboiler – Important Note o The important thing to note for a total reboiler is that the mole fraction, x. N, of the liquid stream from the bottom of the column is equal to the mole fraction, x. B, of the bottom liquid stream and that fed to the partial reboiler! x. B = x. N o The condition of the outlet of the reboiler has to be specified as either a saturated vapor or a superheated vapor in order to use the energy balance. The state of the vapor determines the heat duty of the reboiler. Lecture 10 15

Total-Condenser Mass Balance o Total Eq. (4 -8) o Component Lecture 10 16

Total Condenser Mass Balance Lecture 10 17

Reflux Ratio – Lo/D o External reflux ratio Eq. (4 -9) Lecture 10 18

Total-Condenser Energy Balance Eq. (4 -10) Eq. (4 -14) Lecture 10 19

Partial-Reboiler Energy Balance Eq. (4 -15 a) Eq. (4 -15 b) Eq. (4 -16) Lecture 10 20