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CM 4710, Biochemical Processes Fall 2007 Homework #8 Fri. 09 Nov., 2007 1. Adsorption Separation of Immunoglobulin G using Modified Dextran (adapted from Belter, Cussler, & Hu, pg 153). The equilibrium between immunoglobulin G and a modified dextran (the adsorbent) can be described by the Langmuir isotherm. Dextran will adsorb up to 7.8x10 -6 moles of immunoglobulin G per cm 3 of adsorbent and the Langmuir constant, K L , is 1.9x10 -5 moles/liter. The adsorbent density is 1 gram of adsorbent per cm 3 of adsorbent and the void fraction of a column packed with this adsorbent is 0.40. a) What is the total adsorption capacity of a column packed with modified dextran if the feed concentration of immunoglobulin G is 2x10 -5 moles/liter? (use column data from b)) b) What is the mean retention time for immunoglobulin G in a column of diameter equal to 5 cm with a feed flow rate of 1 liter per minute, feed concentration of 2x10 -5 moles/liter, and a length of 1 meter? c) How many columns would have to be employed to recover immunoglobulin G from a feed tank of 10,000 Liter volume assuming the same feed concentration? 2. Travel Distance of Solutes A and B in a Chromatographic Column. Problem 11.6 of the text, parts a and b. Assume that C A = 0.10 mg/ml and C B = 0.05 mg/ml in the liquid phase of the column at equilibrium with the adsorbed solute. 3. Determining Time to Elute a Solutes A and B from a Chromatographic Column. Problem 11.7 of the text Due Fri. 16 Nov., 2007.

CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

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Page 1: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

CM 4710, Biochemical Processes Fall 2007 Homework #8 Fri. 09 Nov., 2007

1. Adsorption Separation of Immunoglobulin G using Modified Dextran (adapted from Belter, Cussler, & Hu, pg 153).

The equilibrium between immunoglobulin G and a modified dextran (the adsorbent) can be

described by the Langmuir isotherm. Dextran will adsorb up to 7.8x10-6 moles of

immunoglobulin G per cm3 of adsorbent and the Langmuir constant, KL, is 1.9x10-5

moles/liter. The adsorbent density is 1 gram of adsorbent per cm3 of adsorbent and the void

fraction of a column packed with this adsorbent is 0.40.

a) What is the total adsorption capacity of a column packed with modified dextran if the feed

concentration of immunoglobulin G is 2x10-5 moles/liter? (use column data from b))

b) What is the mean retention time for immunoglobulin G in a column of diameter equal to 5

cm with a feed flow rate of 1 liter per minute, feed concentration of 2x10-5 moles/liter, and

a length of 1 meter?

c) How many columns would have to be employed to recover immunoglobulin G from a feed

tank of 10,000 Liter volume assuming the same feed concentration?

2. Travel Distance of Solutes A and B in a Chromatographic Column.

Problem 11.6 of the text, parts a and b. Assume that CA = 0.10 mg/ml and CB = 0.05 mg/ml in

the liquid phase of the column at equilibrium with the adsorbed solute. 3. Determining Time to Elute a Solutes A and B from a Chromatographic Column. Problem 11.7 of the text

Due Fri. 16 Nov., 2007.

Page 2: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
drshonna
Text Box
Problem 1
Page 3: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
Page 4: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
Page 5: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
Page 6: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
drshonna
Text Box
Problem 2
Page 7: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003
Page 8: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

CM 4710, Biochemical Processes Fall 2003Homework #7 Solution Fri. 7 Nov., 2003

3. Determining Time to Elute a Solutes A and B from a Chromatographic Column.

Problem 11.7 of the text

The fundamental eqn. For gel chromatography is

Ve = Vo + KD Vi

For A: Ve = 20 cm3 + 0.5(30 cm3) = 35 cm3

TA = 35 cm3/100 cm3/hr = 0.35 hr

For A: Ve = 20 cm3 + 0.15(30 cm3) = 24.5 cm3

TA = 24.5 cm3/100 cm3/hr = 0.245 hr

Page 9: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

CM 4710, Biochemical Processes Fall 2003 Homework #8 Fri. 4 Nov., 2005

1. Adsorption Separation of Immunoglobulin G using Modified Dextran (adapted from Belter, Cussler, & Hu, pg 153).

The equilibrium between immunoglobulin G and a modified dextran (the adsorbent) can be

described by the Langmuir isotherm. Dextran will adsorb up to 7.8x10-6 moles of

immunoglobulin G per cm3 of adsorbent and the Langmuir constant, KL, is 1.9x10-5

moles/liter. The adsorbent density is 1 gram of adsorbent per cm3 of adsorbent and the void

fraction of a column packed with this adsorbent is 0.40.

a) What is the total adsorption capacity of a column packed with modified dextran if the feed

concentration of immunoglobulin G is 2x10-5 moles/liter? (use column data from b))

b) What is the mean retention time for immunoglobulin G in a column of diameter equal to 5

cm with a feed flow rate of 1 liter per minute, feed concentration of 2x10-5 moles/liter, and

a length of 1 meter?

c) How many columns would have to be employed to recover immunoglobulin G from a

feed tank of 10,000 Liter volume assuming the same feed concentration?

2. Travel Distance of Solutes A and B in a Chromatographic Column.

Problem 11.6 of the text, parts a and b. Assume that CA = 0.10 mg/ml and CB = 0.05 mg/ml in

the liquid phase of the column at equilibrium with the adsorbed solute. 3. Determining Time to Elute a Solutes A and B from a Chromatographic Column. Problem 11.7 of the text

Due Fri. 11 Nov., 2005.

Page 10: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

1. Adsorption Separation of Immunoglobulin G using Modified Dextran (adapted

from Belter, Cussler, and Hu, pg 153) Information

( ) 40.0fraction void

1

/109.1

3mol/IG/cm^ 6-7.8E toup adsorb llDextran wi

isothermLangmuir

3

5

=

=

×=

=+

=

ε

ρcm

g

LmolK

C

CK

CCC

adsorbent

L

SMAX

LL

LSMAXS

Solution a) Adsorption capacity of the column

( )( )( )( )( )

( )

( )( ) molcm

molcm

cm

mol

L

mol

L

molL

mol

cm

mol

C

cmcmcm

C

L

molC

cmmL

cmD

S

S

L

33

63

36

55

53

6

32

5

10712.41045.196340.01:column theofCapacity

104102109.1

102108.7

5.19631002

5column theof Volume

column theof volume1column theofCapacity

adsorbenton ion concentrat soluteadsorbent of volumecolumn theofCapacity

102

1001

5

−−

−−

−−

×=

×−

×=×+×

×

×

=

=

=

−==

×=

===

π

ε

Page 11: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

b) Mean retention time

( )

( )( )

min574.1154359.9740.0

40.0111

min324.127

100

4359.97102

097436.0

102109.1

109.1108.7102

min324.127

2

540.0

min1000

1

min1000

min1

100

11

3

3

3

3

35'

3255

53

6

5'

2'

2

3

3

3

'

=

+=

=

×

=

×+×

×

×

=

×

+=

+

=

=

==

=

==

=

−+=

−−

−−

ADSORBENT

SOLUTION

ADSORBENT

SOLUTION

ADSORBENT

SOLUTION

LL

LSMAX

LL

LSMAX

LL

i

adsorbent

Li

cm

cm

cm

gcm

cmt

cm

cm

L

molf

cm

L

L

mol

L

mol

L

mol

cm

mol

L

molf

CK

KC

CK

CC

dC

dCf

cm

cm

cm

A

FU

cm

g

cmLF

cmL

CfU

Lt

πε

ρ

εερ

c) Number of columns to recover product in 10000 L

( )columns 4344.42

10712.4

10210000columns ofNumber

3

5

≈=×

×

= −

mol

L

molL

Page 12: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

2. Travel distance of solutes A and B in a chromatographic column. Information

Solution a) Position of each band in the column

( )

mlV

k

k

k

k

BAi

ck

ckcf

B

B

A

A

ii

iii

50

6cmA

0.35

150ml volumeBed

3000mg3gadsorbent of mass

liquid solute/ml mg 0.02

adsorbent gadsorbed/m B solute mg 0.05

liquid solute/ml mg 0.1

adsorbent gadsorbed/mA solute mg 0.2

,

m

2

2

1

2

1

2

1i

=∆=

==

======

=+

==

ε

Page 13: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

( )( )

( )( )

( )

( )cm

mg

ml

ml

mg

mX

cm

mg

ml

ml

mg

mlX

ml

mgmgM

mg

mlmgf

mg

mlmgf

ck

kk

ck

ck

dc

dCf

M

CMfA

VX

adsorbent

B

adsorbent

A

adsorbent

adsorbent

ii

ii

ii

ii

iL

L

77494.2

204082.01335.06cm

50

21655.1

5.01335.06cm

50

13

.35-1

1503000

204082.0ml

B 05.0

BFor

5.0ml

A 1.0

AFor

(mg/ml)column of eunit volumper adsorbent ofamount theis

2

2

'

'

22

21

2

1'

'

=

+

=∆

=

+

=∆

=

=

=

=

+=

+

=

+∆=∆

ε

b)

117.0

ml

B 05.0

051.0

ml

B 1.0

438.0

'

'

=

+

=

=

+

=

=∆∆

=

mgfM

R

mgfM

R

X

X

L

L

fB

fA

B

A

B

A

ε

ε

ε

ε

Page 14: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

3. Determining Time to Elute Solutes A and B from a Chromatographic Column Information

h

cmF

cmV

cmV

cmV

K

K

column

i

DB

DA

3

3

3

30

100

60

30

20

15.0

5.0

=

=

=

=

==

Solution Estimate exit time of A and B

Page 15: CM 4710, Biochemical Processes Fall 2007 …drshonna/cm4710f07/homework/hw8...3 + 0.15(30 cm3) = 24.5 cm3 TA = 24.5 cm 3/100 cm3/hr = 0.245 hr CM 4710, Biochemical Processes Fall 2003

( )( )

( )( )h

h

cm

cmcmt

h

h

cm

cmcmt

F

VKVt

B

A

iD

245.0

100

3015.020

35.0

100

305.020

3

33

3

33

0

=+=

=+=

+=