M. Zhang, et al.
BioresourceTechnology281(2019)374–381
defined as the amount of enzyme catalyzing the oxidation of 1 μmol of
NADPH per minute at the assay conditions.
2.7. Determination of inhibitory concentrations and inhibition mechanisms
of lignocellulose-derived by-products (LDBs)
Previously reported representatives of lignocellulose-derived in-
hibitory compounds, ferulic acid, vanillin, formic acid, acetic acid,
benzonic acid, coumaric acid, cinnamic acid and gallic acid, were used
to evaluate their inhibitory effect on XRTL. Their half maximal in-
hibitory concentrations (IC50) were determined by measuring XRTL
activities at varying gradients of increasing LDBs concentrations at
50 °C, pH 6.5 (100 mM of Tris-HCl buffer). The potent phenolic and
non-phenolic inhibitors were selected and their inhibition kinetics was
studied using the standard mixed inhibition model of Michaelis–Menten
equation:
2.5. Characterization of recombinant XRTL
2.5.1. Effect of pH and temperature and the thermal denaturation kinetics
To study the effect of pH on the enzyme, the activity was measured
at 50 °C, using 100 mM sodium citrate (pH 4.0–5.5); potassium phos-
phate (pH 6.0–8.0); and glycine-NaOH (pH 9.0–10). To determine the
optimum temperature, the XRTL activity was measured between 30 °C
and 80 °C at optimal pH. Thermostability and pH stability were in-
vestigated by incubating the enzyme at 40–70 °C in 20 mM phosphate
buffer (pH 7) and at pH 4–10 at 50 °C, respectively. Samples were
withdrawn every 15 min to calculate the residual enzyme activities.
The thermal denaturation kinetics of XRTL was studied in the range
of 50–70 °C using the standard first-order enzyme deactivation kinetics.
Change in enthalpy (ΔH, kJ/mol), change in free energy (ΔG, kJ/mol),
and change in entropy (ΔS, J/mol-K) for thermal denaturation of XRTL
Vmax [S]
v0 =
[I]
[I]
Km 1 +
+ [S] 1 +
(
)
(
)
K
K
(6)
i
i
Ki values were estimated by the nonlinear regression analysis of
Graphpad Prism 6.0 (GraphPad Software, Inc.).
2.8. Xylitol production by recombinant S. cerevisiae Y294 with the XRTL
gene
KbT
h
kd
e
(−ΔH/RT)e(−ΔS/RT)
⎛
⎝
⎞
⎠
(1)
(2)
Shake-flask fermentations were performed to determine xylitol
production by S. cerevisiae Y294 harbouring the XRTL gene (S. cerevisiae
Y294-XRTL). Two pre-inoculation steps were used. During the first pre-
inoculation step, a single colony of S. cerevisiae Y294-XRTL was grown
in 25 ml YPD medium at 30 °C and 200 rpm. After 72 h, 1 ml of culture
was transferred into 50 ml fresh SC minimal medium and incubated at
30 °C and 200 rpm. This secondary pre-inoculation culture (0.5 ml)
were transferred into 50 ml of SC minimal medium with an additional
2% xylose (produced from sugarcane bagasse, data not shown). The
initial cell concentration was the same as that of the controlled ex-
periments with S. cerevisiae Y294 without XRTL gene. Glucose, xylose,
and xylitol concentrations were determined by the LCMS-2020 liquid
chromatography system (Shimadzu) using an Aminex HPX 87-H
column (Bio-Rad) and an ELSD-LT II detector (Shimadzu). The samples
on the column were eluted at 50 °C with water as the mobile phase, at a
flow rate of 0.5 ml/min.
ΔH = Ed − RT
Kdh
⎛
⎞
⎜
ΔG = −RTln
KbT
(3)
(4)
⎝
(ΔH − ΔG)
ΔS =
T
where kd = thermal inactivation rate constant; E0 and Et were the initial
(at t = 0) and residual (at t = t) XRTL activities; (Ed) = activation en-
ergy for denaturation of XRTL; Kb [Boltzmann’s constant (R/
N)] = 1.38 × 10−23 J/K; h (Planck’s constant) = 6.63 × 1034 J s; N
(Avogadro’s number) = 6.02 × 1023 per mol and
R (gas con-
stant) = 8.314 J/mol-K.
2.5.2. Effect of metal ions, additives and salts on purified recombinant
XRTL
The effects of metal ions (Ca2+, Cu2+, Fe2+, Mg2+, Mn2+, and
Zn2+) and reducing agents (EDTA and DTT) were studied by determi-
nation of XRTL specific activity in the presence of three concentrations
of these compounds (0.5, 1 and 2 mM). The experiments were done in
triplicate under optimal conditions and activity without any additive
was considered as 100%. Similarly, the effect of 0–1 M NaCl and KCl on
XRTL activity was determined under optimal conditions and activity
without any additive was considered as 100%.
3. Results and discussion
3.1. Expression, production and purification of XRTL
The expression plasmids, XRTL-pPIC9K and 19up-TEF1-XRTL-CYC-
down-pAUR135 were successfully constructed by subcloning the XRTL
gene from T. lanuginosus into pPIC9K and 19up-TEF1- CYC-down-
pAUR135 under control of the AOX1 and TEF1 promoters, respectively.
P. pastoris GS115 was used as a host for extracellular expression of the
XRTL protein for characterization and purification purposes as pur-
ification allowed testing of xylose reductase activity on the absence of
host aldo-keto reductase or its isozymes, while S. cerevisiae Y294 was
used to study the effect of intracellular expression of XRTL on xylitol
production. The XRTL gene sequence was deposited in the NCBI gene
bank with accession number MG437302.
2.6. Enzyme kinetics in the presence of different substrates and cofactors
Kinetic parameters of the purified recombinant XRTL were de-
termined against D-erythrose, D-ribose, D-arabinose, D-xylose, D-lyxose,
D-allose, D-altrose, D-glucose, D-mannose, L-gulose, D-idose, D-galactose,
D-talose, fructose, sucrose, maltose, lactose, cellobiose and xylobiose by
measuring the initial velocities at constant NADPH (0.15 mM) and
different concentrations of substrates ranging from 5 to 175 mM. The
specific activity data was used to estimate the kinetic constants by fit-
ting to the Michaelis–Menten equation:
The P. pastoris transformants grown on YPD plates containing 2 mg/
ml Geneticin were selected for XRTL production. Maximum XRTL ac-
tivity of 5.23
0.21 U/ml was achieved after 96 h of methanol in-
duction. The recombinant enzyme was purified to homogeneity with an
overall 13.77-fold increase in specific activity, through conventional
ammonium sulfate precipitation (29.76 U/mg), ion-exchange chroma-
tography (55.61 U/mg) and gel filtration chromatographic (78.06 U/
mg) steps. The purified protein had an apparent molecular mass of
∼39 kDa on SDS-PAGE gels (Fig. 2) and appears to migrate as a
monomer during Superdex gel filtration chromatography (data not
shown). A slightly higher molecular weight than the theoretically-
Vmax [S]
v0 =
[S] + Km
(5)
where Vmax is the maximal velocity; Km is the Michaelis-Menten con-
stant; S is the substrate concentration, and v0 is the mean initial velo-
city. The Michaelis-Menten model was also used to study the enzyme
specificity against 20–200 µM NADPH and NADH (disodium salt) as the
known cofactors.
376