Distillation Theory and its Application to Optimal Design of Separation Units

| A | separation work |
| A | stationary point of bond chain |
| A | vertex of product simplex |
| B | bottom stream (flow rate), kmol/sec |
| C ( k) | k-component boundary element of concentration simplex |
| C n | concentration simplex for n-component mixture |
| d | dimension of trajectory bundle |
| D | overhead stream (flow rate), kmol/sec |
| E | entrainer stream (flow rate), kmol/sec |
| F | feed stream (flow rate), kmol/sec |
| h | enthalpy of liquid, kJ/kg or kcal/kg |
| H | enthalpy of vapor, kJ/kg or kcal/kg |
| h | heave key component |
| i D : i B | split in column ( i D and i B components of overhead and bottom products respectively) |
| i : j | split in section ( i and j present and absent component of section product or pseudoproduct respectively) |
| K | equilibrium ratio |
| k | number of product components at sharp distillation |
| k | key component |
| k | key stationary point (pseudocomponent) |
| | equilibrium ratio of component j at infinite dilution |
| K t | equilibrium ratio in tear-off point |
| l | light key component |
| L | liquid stream (flow rate), kmol/sec |
| m | number of product components at sharp distillation |
| m | number of stationary points of bond chain |
| n | number of components in a mixture |
| N | number of equilibrium stages |
| N + or N ? | stable or unstable node respectively |
| | stable or unstable node of overhead boundary element... |