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Tutorial 3
Protein Lab: Simulation of protein purification
Section Tuesday afternoon
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Protein #1
I had to isolate protein #1, its enzyme activity is stable for several hours at a
temperature 40 °C. The enzyme activity of protein had pH values of 2.5 and 9.5
Table 1 Default mixture
Method
protein
Initial
511
Enzyme
4000
Yield
100%
Cost
0
Theory
I began purifying my protein by the method of ion exchange chromatography. Ion
exchange chromatography; is when the polymer resin is negatively charged or
positively charged, it allows for a separation, as if we have an anionic resin, it will
attract positively charged ions that are loaded into the ion exchange
1 Agbooth
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chromatography2. The higher the pH the less protonated the protein will become,
basically it separates proteins by their charge The ion exchange chromatography
was done at a fraction range of 10-35. Secondly, to purify my protein further, I
conducted a gel filtration. I started off with my protein at a pH of protein 1 above 8,
with a Mz of about 50k. I started off by doing an ion exchange chromatography. This
ion chromatography took place in Q-Sepharose with a pH gradient of 2.5-7.9. This
ion exchange was done with a buffer of pH 7.
Results
Table 2. Results of protein 1
Total Protein
Total enzyme
Enrichment
Yield
Cost(hours/10
0 units)
43.mg
3999 Units
11.9
100%
0.175
Discussion
I preceded by the means of ion chromatography. This was done in a ion exchange
media of Q- sepharose at a fraction of 10-30. This allowed for the protein to be
positive and to isolate my protein at pH of 8.1, in one step. It was successful as it I
managed to keep the full yield of product, without any lose. I also received a protein
enrichment of 11.9, which is a pretty high value. Enrichment; 3 is a technique in
which allows for concentration of proteins to improve within analysis. This method
of separation is also verily cheap as it only costs 0.175, in which the cost comes out
to hours/100 units. Additonally, I only lost 1 unit of enzyme, which is slim to none .
Q-sepharose was used, as its matrix type is a strong 4anion exchanger, unlike ssepharose that is a cation exchanger. The purpose of using this media is that it
causes for the protein to be positive. I also in the end did a gel filtration to see if
there was any effect, but it stayed the same
2 Chemlibre
3
4 J. Powlowski
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I tried using many other separation methods, however they always caused for an
immediate loss in yield. When trying to do use Ammonium sulphate, my yield
dropped to 41.3%, which isn’t good as were supposed to keep a yield of over 90%.
Heat treatment did not work either; there was no loss in yield, however this
separation method did not purify my protein at all, it was if I didn’t apply any
separation method at all.
Protein #4
Theory
I once gain started with the method of ion exchange chromatography. As explained
above once again, ion exchange chromatography; is when the polymer resin is
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negatively charged or positively charged, it allows for a separation, as if we have an
anionic resin, it will attract positively charged ions that are loaded into the ion
exchange chromatography. Where the whole goal is to separate proteins by charge.
Secondly I did hydrophobicity5; the purpose of this separation technic is that it
separates proteins from one another by hydrophobicity. A salt can be used to
decrease the amount hydrophobicity among proteins. Gel filtration6; the sample is
loaded into the gel filtrate, where it has porous polymer beads; typically made of
carbohydrates. This separation method is driven by the size of the protein, where
small proteins will be caught in the polymer beads, while large proteins will come
out of the gel filtration, as they cannot be caught in the polymer. Lastly, Ammonium 7
sulphate fractionation was done. This is when proteins are separated by their
solubility, when a salt is present.
Table 3. Initial data for protein 4
Inital
511
Eznyme
7000
yield
100%
Enrichment
1.0
cost
Results
Table 4. Results for protein 4
Initial
Ion Exchange
Ammonium
Protein (mg)
330
239
Enzyme
7000
6997.6
Yield
100
100
Cost
0.100
0.129
sulfate
Hydrophobic
207
6980.5
99.7
.229
interaction
Gel filtration
101.9
69.59.1
99.4
.704
Discussion
5 Chem Libre
6 Lehman
7 Chem Libre
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The enzyme of of protein 4 can be heated for several hours at a temperature of 40 °C.
It has pH values between 4.5 and 10. It has a Mr of about 40K, at about a pH of 6.1.
To start off I had a very difficult time trying to purify my protein, I did this for about
five hours and tried many combinations of separation to try to get it down to one
protein but it just seems not to work out for me. I got down to 4 proteins including
my protein. I started off the experimental procedure by putting my protein solution
through ion chromatography in a Q-sepharose media using a salt gradient from 01.5, I fractioned this at 40-54. I then proceeded to do an ammonium sulphate
fractionation. This salting out affects the solubility, of large groups of proteins
therefore purifying further. I then followed this step with a hydrophobic interaction
Chromatography to separate them by their hydrophobicity. I did this in a PhenylSepharose CL-4B media that was fractioned from 45-69. The last step was Gel
filtration with a polyacrylamide/agarose gel type; specifically Ultro gel AcA 34b,
fractioning between 46-59. This purified my protein as much I could. The
Enrichment increased the more separation methods,that were done. I ended with
101.9g of protein as I started with 511 mg. I ended with a cost of 0.704 for all the
separation methods
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Reference
J.Powlowski, M.J. Kornblatt, P.Joyce, J. Turnbull and Mihai Ciortea Chemistry 271
Laboratory and Turorial Manual edition 1.15 Concordia , 2019
John W. Lehman Operational Organic Chemistry: A Problem Solving Approach to the
Laboratory Course 4th Edition, Pearson Prentice Hall, Upper Saddle River,NJ
Lisa Nichols. Libre Texts: Organic Chemistry Laboratory Techniques, Butte Community
College, 2019
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