Quantification of cellulase activity
Where P is the pressure (MPa); v is the activity of the
-
1
-1
enzyme (mmol min mL ); Va is the activation volume
◦
Cellulase activity was determined at 30 C by the spectrophoto-
metric quantification of the reducing sugars produced, using the
3
-1
(
(
cm mol ); T is the absolute T/K, A is a constant, and R
3
-1
-1
-1
8.314 cm MPa mol K ) is the universal gas constant. The
29
3
,5-dinitrosalicylic acid (DNS) method, as glucose equivalents,
activation volumes were calculate by linear regression analysis.
2
by means of a standard curve of glucose (R = 0.996). Previous
experiments confirmed a linear relation between activity and
enzyme concentration and reaction time. A solution of 1% CMC
was used as a substrate, which was dissolved under continuous
stirring, in the acetate buffer solution at room temperature
during 45 min. To 450 mL of substrate solution, 35 mL of
buffer were added and the reaction started by the addition
of 15 mL of enzyme solution (2.5 mg mL ). After 20 min the
reaction was stopped by the addition of 1.0 mL DNS, followed
by boiling during 5 min, cooling, addition of 1.0 mL water
and measurement of absorbency at 540 nm using a Shimadzu,
UV/VIS 1240 spectrophotometer (Kyoto, Japan). In the case of
activity of cellulase in [bmim]Cl, the substrate solution consisted
of 1% cellulose dissolved in mixtures of buffer and 5–20%
References
1 Y. Sun and J. Cheng, Bioresour. Technol., 2002, 83, 1–11.
2
R. Rinaldi, R. Palkovits and F. Schuth, Angew. Chem., Int. Ed., 2008,
4
7, 8047–8050.
3
M. B. Turner, S. K. Spear, J. G. Huddleston, J. D. Holbrey and R. D.
Rogers, Green Chem., 2003, 5, 443–447.
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Y. G. Ding and G. Wu, Green Chem., 2006, 8, 325–327.
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1
0, 44–46.
8
9
B. Kosan, C. Michels and F. Meister, Cellulose, 2008, 15, 59–66.
C. Cuissinat, P. Navard and T. Heinze, Cellulose, 2008, 15,
75–80.
[bmim]Cl. Previous experiments indicated that there was no
1
1
0 R. P. Swatloski, S. K. Spear, J. D. Holbrey and R. D. Rogers, J. Am.
effect caused by the presence of [bmim]Cl on the quantification
of reducing sugars.
Chem. Soc., 2002, 124, 4974–4975.
1 H. Zhao, C. I. L. Jones, G. A. Baker, S. Xia, O. Olubajo and V. N.
Person, J. Biotechnol., 2009, 139, 47–54.
Cellulase activity under high pressure
12 A. P. Dadi, S. Varanasi and C. A. Schall, Biotechnol. Bioeng., 2006,
9
5, 904–910.
Activity of cellulase under high pressure was carried out using
a hydrostatic press from Unipress Equipment, Model U33
13 N. Kamiya, Y. Matsushita, M. Hanaki, K. Nakashima, M. Narita,
M. Goto and H. Takahashi, Biotechnol. Lett., 2008, 30, 1037–1040.
4 D. Prieur and V. T. Marteinsson, Advances in Biochemical
Engineering/Biotechnology, Springer, Berlin, 1998.
1
1
(
Warsaw, Poland), with a pressure vessel of 100 mL (35 mm
diameter and 100 mm height), surrounded by an external jacket,
connected to a thermostatic bath to control the temperature.
Prior to the experiments the temperature of the pressure vessel
5 B. B. Boonyaratanakornkit, C. B. Park and D. S. Clark,
Biochim. Biophys. Acta, Protein Struct. Mol. Enzymol., 2002, 1595,
2
35–249.
1
1
6 J. A. Torres and G. Velazquez, J. Food Eng., 2005, 67, 95–112.
7 K. Heremans and L. Smeller, Biochim. Biophys. Acta, Protein Struct.
Mol. Enzymol., 1998, 1386, 353–370.
◦
was equilibrated at 30 C. The enzymatic reaction was initiated at
atmospheric pressure as described above, and immediately after
two 400 ml eppendorf tubes were filled with the reaction mixture
and capped. The two tubes were then packaged on a heat sealed
plastic bag, without air, that was introduced in the pressure vessel
and pressure build up was initiated. After the desired pressure
had been achieved, the enzymatic reaction continued for 10 min
under pressure and then decompression took place. The bag was
taken out of the pressure vessel and transferred to the water bath
1
1
8 S. M. Castro, A. Van Loey, J. A. Saraiva, C. Smout and M.
Hendrickx, Enzyme Microb. Technol., 2006, 38, 831–838.
9 M. M. C. Sun and D. S. Clark, Hyperthermophilic Enzymes, Elsevier
Academic Press Inc, San Diego, 2001.
20 J. B. Kim and J. S. Dordick, Biotechnol. Bioeng., 1993, 42, 772–776.
2
1 D. B. Northrop, Biochim. Biophys. Acta, Protein Struct. Mol.
Enzymol., 2002, 1595, 71–79.
2 P. Lozano, T. De Diego, D. Carrie, M. Vaultier and J. L. Iborra,
J. Mol. Catal. A-Chem., 2004, 214, 113–119.
2
◦
at 30 C to complete the 20 min reaction time, after which the
23 P. Lozano, T. de Diego, S. Gmouh, M. Vaultier and J. L. Iborra,
Biotechnol. Prog., 2004, 20, 661–669.
reaction was stopped and the activity quantified at atmospheric
pressure.
2
2
2
4 M. D. Bermejo, A. J. Kotlewska, L. J. Florusse, M. J. Cocero, F. van
Rantwijk and C. J. Peters, Green Chem., 2008, 10, 1049–1054.
5 M. F. Machado and J. M. Saraiva, Biotechnol. Lett., 2005, 27, 1233–
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Activation volume calculation
6 P. Halling, Trends Biotechnol., 1989, 7, 50–52.
The effect of pressure on the velocity of the enzyme catalysed
reaction is described by the activation volume (Va) calculated by
the Eyring equation:
27 J. A. Laszlo and D. L. Compton, Biotechnol. Bioeng., 2001, 75, 181–
1
86.
2
2
8 S. Murao, Y. Nomura, M. Yoshikawa, T. Shin, H. Oyama and M.
Arai, Biosci., Biotechnol., Biochem., 1992, 56, 1366–1367.
9 D. Johnston, in Handbook of Food Enzymology, ed. J. R. Whitaker,
A. G. J. Voragen and D. W. S. Wong, Marcel Dekker Inc, Wyndmoor,
2003, pp. 761-770.
PVa
ln
(
V
)
= ln
(
A
)
−
(1)
RT
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Green Chem., 2010, 12, 632–635 | 635