distillation - oil india · distillation types . 1. flash distillation. 2. batch distillation. 3....
TRANSCRIPT
Distillation
oPtiMiZation FoR MaXiMisation PResenteD by : nabanita Deka lPG DePaRtMent
oil inDia liMiteD DateD-04.03.2011
Basics of mass transfer
Mass transfer : Transfer of material from one homogeneous phase to another. The driving force for mass transfer is concentration difference or difference in activity coefficient.
Mass transfer operation involves changes in
composition of solution & mixtures. Transfer of substance through another on a molecular scale.
Mass transfer coefficient : Rate of mass transfer per unit area per unit conc. difference. It depends on diffusivity,viscosity,density,velocity
& linear dimension D. Why Mass transfer operation: Any chemical process requires : 1. Purification of raw material. 2. Separation of product from byproduct
Types of Distillation
Distillation Types 1. Flash distillation. 2. Batch Distillation. 3. Steam Distillation. 4. Azeotropic & Extractive Distillation Flash Distillation : Vaporising a definite fraction of
the liquid in such a way that the evolved vapor is in equilibrium with residual Liquid.
Batch Distillation : Used for Feed composition may change from batch to
batch.Negligible hold up in the column & condenser relative to that in receiver & kettle.
Types of Distillation
Steam Distillation : 1. Possible to distill an organic compound at much lower
temp. 2. At constant system pr.PT ,steam lowers the partial &
vapor pressure of organic compound & its corresponding boiling pt. Due to immiscibility of water ,it can be separated from
product by simple condensation & followed by decanting.
Application : Purification of heat sensitive material as an alternative to vacuum distillation.
Azeotropic & Extractive Distillation. Very close boiling mix can be separated economically by
this technique.
Solvent for Distillation
Solvent when added will increase the difference between
volatilities of light & heavy component. The attraction of solvent to one of the component reduces the volatility of solvent & the component to which it is attracted.
Solvent for Distillation should be Non-corrosive. Should not react with feed to form undesirable product. Non-toxic. Azeotropic solvent should have volatility near the major
component desired in overhead product & in Extractive distillation its volatility should be lower than major component to be withdrawn at bottom.
Points of discussion
Distillation is the dominant process for separating large multi-component streams into high purity products.
Through today’s presentation we would try to understand the following optimization goals for sieve trayed columns:
1. Maximizing theoretical stages per height of section or
column. 2. Minimizing pressure drop per theoretical stage. 3. Maximizing the operational range, turn down or turn
up.
Trayed columns
In a trayed column liquid flows down the column through the dowcomers and then across the tray deck, while vapour flow upward through the liquid inventory on the tray.
Types of trays based on the flow pattern: 1. Cross flow (most common & least expensive) 2. Parallel flow (if designed properly would give 10%
higher efficiency) As column diameter increases, the ratio of weir length
to throughput decreases. So, for larger dia columns multiple pass (no. of downcomer per tray) trays are used to increase the weir length.
Factors affecting tray efficiency
Flow pattern: As column diameter increases, the ratio of weir
length to throughput decreases. So, for larger dia columns multiple pass (no. of downcomer per tray) trays are used to increase the weir length.
Tray deck type: Sieve trays are the most commonly used whereas
bubble cap trays are used less frequently.
Factors affecting tray efficiency
Pressure drop Throughput (weeping and flooding)
Steps towards higher efficiency
To maximize the number of theoretical stagesfor a given section height (For sieve trays)
1. Keep the fraction open area low, in the range of 5% 2. Use the smallest practical perforation diameter. 3. Consider parallel flow trays To minimize the pressure drop per theoretical stage
(For sieve trays) 1. Use the largest fraction open area that will not result in
weeping 2. Use the smallest practical perforation diameter. 3. Specify a low outlet weir (<50mm) 4. Consider parallel flow trays
Steps towards higher efficiency
To maximize the operating range (For sieve trays): 1. Lower open area 2. Use the smallest practical perforation diameter. 3. Maximize the tray spacing 4. Decreasing the liquid inventory by increasing the
number of tray passes or lowering the weir height.
Thank you