Introduction to Distillation[1]

7/31/2019 Introduction to Distillation[1]

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Introduction to Distillation

1Binous - Introd. to Distillation


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Exploits differences in boiling point, or volatility

Requires the input of energy

Handles a wide range of feed flow rates

Separates a wide range of feed concentrations

Produce high product purity



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vapor becomes richer in the more volatile components



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thermodynamic vapor-liquid equilibrium considerations



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K-values

Wilson model for iEOS for fugacity coefficients

Relative volatility



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a single equilibrium stage can only achieve

a limited amount of separation 7Binous - Introd. to Distillation


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CMO assumption

When CMO is true?

(1) sensible heat effects are small

(2) molar latent heats of vaporization are equal

(3) heat of mixing is negligible

(4) there are no heat losses or gains.



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Cascade of Separation Stages



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Assume CMO:

Mass balance:



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We need vapor and liquid to

feed the bottom and top of

the cascade.

The feed to the process is

introduced at an intermediate

stage.



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Liquid is prevented from weeping through the holes

in the plate by the upflowing vapor. In this way the

vapor and liquid are contacted.

The liquid from the first tray flows over a weir and

down a downcomer, to the next stage and so on.



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Sieve trays

Valve trays

Bubble-cap trays

In practice, the column will need more trays than the

number of equilibrium stages as mass transfer limitations

prevent equilibrium being achieved on a tray.



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packed columns:

Here the column is filled with a solid material which has a high

voidage (random packing material such as Pall rings, Ceramic

Intalox saddles... or structured packing such as Glitsch grid) .

Liquid trickles across the surfaces of the packing and vapor

flows upward through the voids in the packing, contacting the

liquid on its way up the column.



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design of a distillation column involves:

1. Set the product specifications.

2. Set the operating pressure.

3. Determine the number of theoretical stages required and the energy

requirements.

4. Determine the actual number of trays or height of packing needed and the

column diameter.

5. Design the column internals, which involves determining the specificdimensions of the trays, packing, liquid and vapor distribution systems, etc.

6. Carry out the mechanical design to determine wall thicknesses, internal

fittings, etc.



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Binary Distillation



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Reflux ratio



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The construction is started by plotting the operating lines for the

rectifying and stripping sections. The q-line intersects the

operating lines at their intersection.



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The intersection of the operating lines is the correct feed

stage, i.e. the feed stage necessary to minimize the overallnumber of theoretical stages.

The construction steps off between the operating lines and

the equilibrium lines.

The construction can be started either from the overhead

composition working down or from the bottom composition

working up.



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Choice of Operating Parameters

The operating parameters to be selected by the designer include:

1. operating pressure

2. reflux ratio

3. feed condition

4. feed stage location

5. type of condenser



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operating pressure

Pressure has an important effect on all aspects of thedistillation column design.



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As pressure increases, the relative volatility decreases,

making separation more difficult.

Minimum reflux ratio also increases with increasing

pressure, as does the minimum number of stages.

All of these trends point to operating the distillation

columns at a pressure as low as possible.



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Latent heat decreases with increasing pressure; this would have

the effect of decreasing the reboiler duty as pressure increases.

Finally, both the condenser and the reboiler temperature

increase as pressure increases.



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Reflux Ratio



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Feed Condition

The feed condition affects vapor and liquid flow rates in the

column, and in turn:

1. reflux ratio, heating and cooling duties

2. column diameter

3. most appropriate location of the feed stage

Heating or cooling the feed can reduce energy cost

by reduction of utility consumption.


C li h f d


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Cooling the feed:

1. decreases the number of stages in the rectifying section but

increases the number of stages in the stripping section.

2. requires more heat in the reboiler but decreases the cooling

duty of the condenser.

Heating the feed:

1. increases the number of stages in the rectifying section but

decreases the number of stages in the stripping section.

2. decreases the heat requirement of the reboiler but increases

the cooling duty of the condenser.



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Feed Stage Location

When choosing the feed stage location, our objective is to find a

stage in the column for which the composition matches as closely

as possible that of the feed.

Mismatches between the composition on the feed stage and that

of the feed create inefficiencies in the distillation. This leads to an

increase in the number of stages required for the same

separation, or more reflux, which means increased energy

requirements, or a combination of both.



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Distillation Equipment

Sieve tray, is the most common arrangement used. It is

cheap, simple, and well understood in terms of its

performance.

Valve arrangement offer more flexibility to cope with wider

range of liquid and vapor flow rates.



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The difference between the performance of an ideal stage and

a real tray results from the fact that equilibrium is not

achieved on a real tray because of mass transfer limitations.

We therefore define an efficiency to convert from the

theoretical stages to real trays.



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Three different efficiencies can be defined:



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1. flooding: liquid cannot flow down the column

2. entrainment: liquid drops are carried up the column by the

vapor flow

3. downcomer backup: liquid backs up in the downcomers

4. weeping: vapor flow is too low to maintain liquid on the tray

5. coning: poor vapor-liquid contact occurs due to the vapor

forming jets



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Packing



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Column Diameter Calculation



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Column Sequences

If a feed mixture needs to be separated into more than two

products, then more than one distillation column will be required.



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Introduction to Distillation[1]

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