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Department of Chemical Engineering SRM University CH0401 Process Engineering Economics Lecture 4a Balasubramanian S

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Page 1: CH0401 Process Engineering Economics Lecture 4a ...balasubramanian.yolasite.com/resources/Introduction Economics... · CH0401 Process Engineering Economics Lecture 4a Balasubramanian

Department of Chemical Engineering SRM University

CH0401 Process Engineering Economics

Lecture 4a

Balasubramanian S

Page 2: CH0401 Process Engineering Economics Lecture 4a ...balasubramanian.yolasite.com/resources/Introduction Economics... · CH0401 Process Engineering Economics Lecture 4a Balasubramanian

Balasubramanian S Department of Chemical Engineering 2

Process Engineering Economics

1

2

Economic Analysis

Economic Balance in Cyclic Operation

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Balasubramanian S Department of Chemical Engineering 3

Process Engineering Economics

1

2

Economic Analysis

Economic Balance in Cyclic Operation

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Balasubramanian S Department of Chemical Engineering 4

Process Engineering Economics – Economic Analysis

Optimum proportions for a

cylindrical container

The surface area (A) of the cylinder (closed) is given as the sum of the area of Sides, top and bottom covers of the cylinder i.e. A = (! !D ! L)+ !

4D2"

#$%&' +

!4D2"

#$%&'

A = (! !D ! L)+ 2 !4D2"

#$%&'

Where D = Vessel Diameter L = Vessel Length (or Height)

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Balasubramanian S Department of Chemical Engineering 5

Process Engineering Economics – Economic Analysis

A = (! !D ! L)+ 2 !4D2"

#$%&'

The above equation is minimized, simplified and solved to identify the

minimum surface area required for cylinder with a given volume

f (D ! L) = (D ! L)+ D2

2"#$

%&'( ( ( (A)

For a given volume (V), the diameter and length are related by

V = !4!D2 ! L"

#$%&'

L = 4V!D2

!"#

$%& ' ' ' ' ' '(B)

and

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Balasubramanian S Department of Chemical Engineering 6

Process Engineering Economics – Economic Analysis

Now the equation (A) becomes

f (D) = 4V!D

!"#

$%& +

D2

2!"#

$%&

Differentiating the above function and setting it to zero will give the optimum

value for D

! 4V!D2

"#$

%&' + D = 0

D = 4V!

3

From equation (B), the corresponding length will be

L = 4V!

3

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Balasubramanian S Department of Chemical Engineering 7

Process Engineering Economics – Economic Analysis

Therefore, for a cylindrical container the minimum

surface area to enclose a given volume is obtained

when length is made equal to the diameter.

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Balasubramanian S Department of Chemical Engineering 8

Process Engineering Economics – Economic Analysis

Example Problem: It is required to determine the optimum diameter to

height ratio for a large oil storage vessel, so that the total cost is minimum.

Following data may be used for the calculation

Cs = cost of sides per square meter

Ch = cost of the head or top per square meter = 1.5 Cs

Cb = cost of the bottom per square meter = 0.75 Cs

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Balasubramanian S Department of Chemical Engineering 9

Process Engineering Economics – Cyclic Process

The surface area (A) of the cylinder (closed) is given as the sum of the area of Sides, top and bottom covers of the cylinder i.e. A = (! !D !H )+ !

4D2"

#$%&' +

!4D2"

#$%&'

Let CT = total cost of the vessel D = Vessel Diameter

H = Vessel Height

then

CT = Cs (! !D !H )+Cb!4D2"

#$%&' +Ch

!4D2"

#$%&' ( ( ( ( ( ((1)

CT = Cs (! !D !H )+ (Cb +Ch )!4D2"

#$%&' ( ( ( ( ( ((2)

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Balasubramanian S Department of Chemical Engineering 10

Process Engineering Economics – Cyclic Process

V = !4!D2 !H"

#$%&'

H = 4V!D2

!"#

$%&

(or)

Substituting for equation H in equation (2) shown in slide 09

CT = Cs 4VD

!"#

$%& + (Cb +Ch )

!4D2!

"#$%& ' ' ' ' ' '(3)

Differentiating with respect to design variable D and equating to zero

dCT

dD= !4CsV

D2 + (Cb +Ch )!D2

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Balasubramanian S Department of Chemical Engineering 11

Process Engineering Economics – Cyclic Process

D3 = Cs

Cb +Ch

!

"#

$

%& '8V!

( ( ( ( ( ((4)

Substituting for the volume in (4) in terms of D and H gives the following

optimum D to H ratio for the minimum cost of the vessel.

DH

= 2Cs

Cb +Ch

! ! ! ! ! !(5)

Substituting for Cb and Ch in terms of Cs gives the optimum D to H

DH

= 2Cs

(0.75+1.5)Cs

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Balasubramanian S Department of Chemical Engineering 12

Process Engineering Economics – References

•  Herbert E. Schweyer. (1955) Process Engineering Economics, Mc Graw Hill •  Max S. Peters, Kaus D. Timmerhaus, Ronald E. West. (2004) Plant

Design and Economics for Chemical Engineers, 5th Ed., Mc Graw Hill

•  Max Kurtz. (1920) Engineering Economics for Professional Engineers’ Examinations, 3rd Ed., Mc Graw Hill

•  Frederic C. Jelen, James H. Black. (1985) Cost and Optimization Engineering, International Student edition, Mc Graw Hill

•  Grant L. E, Grant Ireson. W, Leavenworth S. R. (1982) Principles of Engineering Economy, 7th Ed., John Wiley and Sons.