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ORIGINALS ORIGINALARBEITEN
Nano-zycosil in MDF: gas and liquid permeability
Hamid Reza Taghiyari
Received: 12 October 2012 / Published online: 7 April 2013
� Springer-Verlag Berlin Heidelberg 2013
Abstract Effects of zycosil nanoparticles, with size range
from 20 to 80 nm, on liquid and gas permeability of
medium density fiberboard were studied. Nanozycosil was
used at four consumption levels of 0, 50, 100, and 150 g/kg
dry wood fibers. Density of all treatments was kept con-
stant at 0.67 g/cm3. The obtained results indicated that
addition of zycosil to the mat resulted in a significant
increase in gas permeability due to the lower fiber-content
in the nanozycosil-treated specimens and the consequent
micro-cavities that were formed in the boards. However,
the water-repellant property of zycosil nanoparticles com-
pensated for the micro-cavities to some extent. High cor-
relation was observed between gas and liquid permeability.
The consumption level of 50 g of nanozycosil/kg can be
recommended to improve the impermeability property of
medium density fiberboard to water.
Einfluss von Nano-Zycosil auf die Gas- und Flussig-
keitsdurchlassigkeit mitteldichter Faserplatten
Zusammenfassung Untersucht wurde der Einfluss von
Zycosil-Nanopartikeln mit einer Partikelgroße zwischen 20
und 80 nm auf die Flussigkeits- und Gasdurchlassigkeit von
mitteldichten Faserplatten. Nano-Zycosil wurde in den vier
Dosierungen 0, 50, 100 und 150 g/kg Spantrockengewicht
verwendet. Die Dichte wurde bei allen Behandlungen mit
0,67 g/cm3 konstant gehalten. Die Ergebnisse zeigten,
dass durch Zugabe von Zycosil zum Spankuchen die
Gaspermeabilitat signifikant anstieg. Dies ist auf den
niedrigeren Spananteil in den mit Nano-Zycosil behandelten
Prufkorpern sowie die dadurch in den Platten entstandenen
Mikrohohlraume zuruckzufuhren. Die Mikrohohlraume
wurden zum Teil durch die wasserabweisende Eigenschaft
der Zycosil-Nanopartikel kompensiert. Die Gas- und
die Flussigkeitsdurchlassigkeit waren hoch korreliert. Zur
Verbesserung der Wasserundurchlassigkeit mitteldichter
Faserplatten konnen 50 g/kg Nano-Zycosil empfohlen
werden.
1 Introduction
Wood is frequently modified by engineering processes to
give stiffness or homogeneous mechanical properties
because few species sustain their hygroscopicity level
(Borrega and Karenlampi 2010) or offer radial and axial
uniformity in their produced wood (Akhtari et al. 2012;
Ghorbani et al. 2012; Papadopoulos 2012); the quality of
wood can also be affected by rotation period, mono- or
mixed-species cultivation, light and soil, as well as inter-
action between clone-type and site (Barna 2011; Hering
et al. 2012; Lotfizadeh et al. 2012; Taghiyari et al. 2008,
2010, 2011a, b, c; Wodzicki 2001). Furthermore, the
majority of humans world-wide depend upon wood prod-
ucts harvested from forests (Dykstra 2012); therefore,
efficient use of wood is highly important. In this connec-
tion, composite-boards offer the advantages of a homoge-
neous structure and the use of raw materials without
restrictions as to the shape and size (Grace 2005) and there
are many studies on finding methods for limitation of
formaldehyde emission and improving the quality (Stockel
et al. 2012; Valenzuela 2012). Composite-boards and
profiles are therefore expanding worldwide. In fact, wood-
based composite products are commonly substituted for
H. R. Taghiyari (&)
Wood Science and Technology Department, The Faculty of Civil
Engineering, Shahid Rajaee Teacher Training University,
Shabanloo St., Lavizan, Tehran, Iran
e-mail: [email protected]; [email protected]
123
Eur. J. Wood Prod. (2013) 71:353–360
DOI 10.1007/s00107-013-0691-6
solid wood in today’s building structures (Eshaghi et al.
2013; Taghiyari 2006). Structural and non-structural
engineered wood composites based on oriented strand-
board (OSB), plywood, medium density fiberboard (MDF),
laminated veneer lumber (LVL), thermoplastic/wood fiber
blends, etc. are now used in both interior and exterior
applications (Laks 2002). The main factors that influence
the properties and quality of the panels are the density of
the panel, geometry, and moisture content of the particles,
the pressing cycle, and the quantity and type of adhesive.
The production of wood composites has increased dra-
matically over the past three decades due to a number of
factors. The changing wood supply, the development of
new composite technologies, and the widespread accep-
tance by architects and builders have each contributed to
the increased wood composite production (Gardner et al.
2003). Their use, however, is often limited due to high
sensitivity to moisture and decay (Baileys et al. 2003), as
well as fire (Awoyemi and Westermark 2005; Awoyemi
2007; Taghiyari 2012b). Therefore, the emergence of new
technologies to produce an increasing array of new wood
composite products has forced the industry to follow up
varied protection processes and/or treatments to protect
these new wood-based products (Kirkpatrick and Barnes
2006). Wood-based composite products offer complexities
and opportunities not found in solid woods. Because there
are many types of wood composite products and manu-
facturing processes, there are a number of ways to apply
treatments to these materials (Gardner et al. 2003). Bio-
cidal protection may be incorporated into solid wood by
pressure/vacuum treatment processes with liquid-based
systems, by surface coatings (dip, spray, or brush), or by
direct placement in the product (such as borate rods). These
strategies are all post-manufacture treatments (PMT), and
the main concern with each of these treatments is chemical
gradients within the product. The advantage of wood-based
composites is that they offer in-process treatment (IPT)
options (incorporation during manufacture), as well as
PMT (Manning 2002). Several common systems for pres-
ervation of composites include: (1) use of pretreated wood;
(2) in-process preservative treatments favored for com-
posites made from flakes, particles, and fibers where the
preservative treatment is incorporated during the manu-
facturing process; (3) post-process preservative treatments
(PMT); and (4) use of recycled treated wood elements in
manufacturing or the use of wood species with a high
natural resistance against biodegradation or fire (Gardner
et al. 2003). It was also indicated that the inherent nature of
wood-based composites allows them to be treated with IPT,
which offers several distinct advantages not found with
solid wood products (Manning 2002). Therefore, different
materials may be easily used to modify and improve some
of the undesirable properties in composite boards or the
production procedure. In this connection, the heat-con-
ductive nature of nanometal particles (Gogoi and Deb
2012; Mahaptra et al. 2012; Narashimha et al. 2011;
Rangavar et al. 2013; Taghiyari 2011a, b, 2012a, b, 2013;
Taghiyari et al. 2012a, b, c, d, e; Rassam et al. 2012;
Wegner and Jones 2006; Wegner et al. 2005; Wisitoraat
et al. 2010; Wu et al. 2012; Yu et al. 2012) was used to
better polymerize the resin in the core of the mat (Tag-
hiyari et al. 2011a), as well as decreasing gas and liquid
permeability (Taghiyari 2011b). Enhancement of the ther-
mal conductivity of common heat transfer fluids when
small amounts of metallic and other nanoparticles were
dispersed in these fluids has also been reported by many
researchers (Gogoi and Deb 2012; Heidarpour et al. 2011;
Prondana et al. 2011; Sadeghi and Rastgo 2012; Soltani-
nezhad and Aminifar 2011). The improving effects of sil-
ver nanoparticles on physical and mechanical properties of
particleboard on an industrial scale as well as its hot-press
time reduction were also reported (Taghiyari et al. 2011a).
However, the effect of zycosil water-repellent property
in medium-density fiberboard (MDF) has not yet been
studied. The present study was therefore conducted to
evaluate if zycosil nanoparticles could significantly con-
tribute to a lower permeability and decrease the penetration
of water in MDF.
2 Experimental
Wood fibers were procured from Sanaye Choobe Khazar
Company in Iran (MDF Caspian Khazar). The fibers com-
prised a mixture of five species of beech, alder, maple,
hornbeam, and poplar from the neighboring forests. Control
boards were 16 mm in thickness and 0.67 g/cm3 in density.
Separate 50 9 50 mm2 specimens were prepared from each
replication to monitor density. The density of the boards
was kept constant for all treatments. The total nominal
pressure of the plates was 160 bars. The temperature of the
plates was fixed at 130 �C. Hot-pressing continued for
8 min. Urea–Formaldehyde resin (UF) was procured from
Sari Resin Manufacturing Company in Sari, Iran. Resin-
content was 10 % based on dry fiber in each treatment; UF-
resin was used with 200–400 cP in viscosity, 47 s of gel
time, and 1.277 g/cm3 in density. Ten boards were made for
each treatment. From each board, 20 permeability speci-
mens were cut from the central part of the board, and 20
other specimens were cut from the marginal part (marginal
parts are considered the 2-cm margins all around each board
which are usually cut-off in most factories).
The nano-zycosil liquid (NZ-liquid) used was the
resultant product of organo silane reacted with organic
reactant, produced in cooperation with Zydex Industries.
Its color was pale yellow, with the flash point at more than
354 Eur. J. Wood Prod. (2013) 71:353–360
123
85 �C and auto-ignition temperature at more than 200 �C,
specific gravity of 1.05 g/mL (at 25 �C), viscosity of
500–1,000 cps (at 25 �C). The nano-zycosil liquid was
comprised of hydroxyalkyl-alkoxy-alkylsilyl compounds
(38–42 %); and the solvent was ethylene glycol
(58–62 %). The size range of nanoparticles was 20–80 nm.
The NZ-liquid was mixed with the resin at the proportion
of 0, 50, 100, and 150 g/kg dry weight basis of fibers. For
each treatment, the weight of NZ-solids was deducted from
the fiber used to keep the density of the boards constant.
The final mixture of NZ ? resin was smoothly sprayed on
the fibers. The pH and viscosity of the resin were kept
constant for all treatments in the present study. Four boards
were manufactured for each treatment. Boards were kept in
a conditioning chamber (25 ± 2 �C, 40 ± 3 % relative
humidity) for 1 month before the liquid and gas perme-
ability specimens were measured.
2.1 Gas permeability measurements
Many techniques have been brought up to measure per-
meability in solid woods and wood-composite materials
(Dashti et al. 2012a, b; Dermoe et al. 2012; Lotfizadeh
et al. 2012). In the present study, gas permeability mea-
surement was carried out by an apparatus designed and
built by the author (Taghiyari 2011b; Taghiyari and Efhami
2011; Taghiyari et al. 2011b, 2012b) equipped with
7-storey automatic-time-measurement device with milli-
second precision (USPTO No. 8,079,249 B2, approved by
The Iranian Research Organization for Scientific and
Technology under certificate No. 47022). Falling-water
volume-displacement method was used to calculate spe-
cific gas permeability values based on the microstructure
porosity of wood (Shi 2007; Siau 1971; Taghiyari et al.
2010; Taghiyari and Sarvari Samadi 2010). Twenty spec-
imens were randomly cut at scattered locations from the
boards of each treatment by a hole-saw. Diameter of
specimens was 17 mm. For each specimen, gas perme-
ability values were measured at seven different water-col-
umn heights, that is seven different vacuum pressures, in a
single run. Internal diameter of the glass tube was 13 mm.
Water level was 15 cm above the starting sensor of the first
time-measurement device (Gas 1). Connection between the
specimen and holder was made fully air-tight. A vacuum-
pressure gauge with milli-bar precision was connected to
the whole structure to monitor pressure gradient (DP) and
vacuum pressure at any particular time as well as height of
water column. Vacuum pressures at the starting and stop-
ping points for each of the seven different water column
heights are listed in Table 1.
Three measurements were taken for each specimen.
Superficial permeability coefficient was then calculated
using Siau’s Equations (Siau 1995) (Eqs. 1, 2). The
superficial permeability coefficients were then multiplied
by the viscosity of air (l = 1.81 9 10-5 Pa s) for the
calculation of the specific permeability (K = kg l).
kg ¼VdCLðPatm � 0:074�zÞ
tAð0:074�zÞðPatm � 0:037�zÞ �0:760mHg
1:013� 106Pað1Þ
C ¼ 1 þ Vrð0:074DzÞVdðPatm � 0:074�zÞ ð2Þ
Where: kg is the specific gas permeability (m3/m), V d = pr2 Dz [r = radius of measuring tube (m)] (m3), C the cor-
rection factor for gas expansion as a result of change in
static head and viscosity of water, L the length of wood
specimen (m), Patm the atmospheric pressure (m Hg), �z the
average height of water over surface of reservoir during
period of measurement (m), t the time (s), A the cross-
sectional area of wood specimen (m2), Dz the change in
height of water during time t (m), Vr is the total volume of
apparatus above point 1 (including volume of hoses) (m3).
2.2 Liquid permeability measurement
Liquid permeability was measured using RILEM test
method II.4 (Fig. 1) according to RILEM Commission 25,
PEM, Test Method 1154 by International Union of Labo-
ratories and Experts in Construction Materials, Systems,
and Structures; penetration tests were conducted under
laboratory conditions according to ASTM E-514. Two
times were measured: (1) The time the first drop of water
falls off the bottom surface of the specimen; (2) The time
the level of water in the RILEM tube lowers by 50 mm in
the tube (that is, 6.6 CC of water). Correlations between
each of the 7 gas permeability times were separately cal-
culated with the-first-drop time as well as 50-mm-lowering
time.
Table 1 Vacuum pressures at starting and stopping points for each
of the seven measuring heights
Tab. 1 Vakuumdrucke bei Beginn und Ende der Versuche mit jeder
der sieben Messhohen
Code of
the 7
water
columns
Height of the
7 water
columns at
starting point
(cm)
Height of the
7 water
columns at
stopping
point (cm)
Starting
point
vacuum
pressure
(minus
milli-bar)
Stopping
point
vacuum
pressure
(minus
milli-bar)
Gas 1 149.5 139.5 155 146.5
Gas 2 134.5 124.5 141.5 132
Gas 3 119.5 109.5 126.5 117
Gas 4 104.5 94.5 112 101.5
Gas 5 89.5 79.5 97.5 86.5
Gas 6 74.5 64.5 82 72
Gas 7 59.5 49.5 66.5 56
Eur. J. Wood Prod. (2013) 71:353–360 355
123
2.3 Statistical analysis
Statistical analysis was conducted using SAS software
program, version 9.1 (2003). Two-way analysis of variance
(ANOVA) was performed to discern significant difference
at the 95 % level of confidence. Grouping was then made
between treatments using the Duncan test. Correlation and
hierarchical cluster analysis, including dendrogram and
using Ward methods with squared Euclidean distance
intervals, was carried out by SPSS/16 (2007).
3 Results and discussion
The amount of NZ-suspension used for each treatment (50,
100, and g/cm3) was deducted from the dried fiber used to
keep the density of the boards constant at 0.67 g/cm3.
Therefore, the volume of wood fibers decreased as the NZ-
content increased from 0 to 150 g/cm3. This resulted in the
wood fibers being less compacted and integrated together
in the MDF-matrix. SEM micrographs showed scattered
micro-cavities in the body of the NZ-treated boards
(Fig. 2b).
The specific gas permeability values measured for the
control boards based on the seven different water columns
(7 different vacuum pressures) indicated no significant
difference between the seven specific permeability values
(Fig. 3). However, significantly high difference was
observed between the central and marginal specimens. This
shows that the margins of the boards were not as uniformly
compact as the central parts. Careful measures should
therefore be taken to sample not from the marginal parts of
composite boards for scientific purposes. Correlation
analysis for the seven different gas permeability times
(central parts of the boards) with the two liquid perme-
ability times showed high significant positive R-square for
all the seven vacuum pressures (Table 2). However, the
seventh vacuum pressure showed the highest R-square
(0.954 for the 1st-drop, and 0.987 for 50-mm lowering
time); so the gas permeability values of this vacuum
pressure was used for reporting purposes in the present
paper. Similar study on the correlation between gas and
liquid permeability of particleboard showed the highest
correlation in the third vacuum pressure (Taghiyari 2011b).
It can therefore be concluded that in MDF where some of
the single fibers may be loose enough to be moved under
high vacuum pressures, lower vacuum pressures (that is,
Gas-7) may give a better scope of the liquid permeability.
The specific gas permeability value of the four treat-
ments showed that control specimens had the lowest spe-
cific gas permeability (0.13 9 10-13 m3/m) and NZ-150
specimens had the highest (0.39 9 10-13 m3/m) (Fig. 4).
The reason for the higher gas permeability of NZ-150 can
be assigned to the lower fiber volume of this treatment. The
micro-cavities in the MDF-matrix facilitated the air flow
(Fig. 2b). However, not much difference was seen in the
gas permeability of NZ-50 and NZ-100, although both
treatments showed higher gas permeability than that of the
control treatment. This may indicate that more NZ-parti-
cles have contributed in binding the fibers together at 100 g
Fig. 1 Liquid permeability
measurement apparatus
(RILEM) (The length of the
circular specimen in the present
study was 16 mm, equal to the
thickness of the MDF boards)
Abb. 1 Apparat zur Messung
der Flussigkeitsdurchlassigkeit
(RILEM) (Die Lange des
runden Prufkorpers betrug
16 mm, entsprechend der Dicke
der MDF-Platten)
356 Eur. J. Wood Prod. (2013) 71:353–360
123
Fig. 2 MDF texture a control
specimen: fibers are integrated
more intensely; b NZ-150: some
void spaces are observed in the
texture leading air to pass
through much easier
Abb. 2 a Struktur der MDF-
Kontrollprobe: Die Spane sind
starker verdichtet; b NZ-150: es
sind einige Hohlraume in der
Struktur zu sehen, durch die die
Luftdurchlassigkeit leichter
erreicht wird
Gas permeability coefficient of control treatment at seven different vacuum pressures
0
0.05
0.1
0.15
0.2
0.25
CC CM CC CM CC CM CC CM CC CM CC CM CC CM
Gas 1 Gas 2 Gas 3 Gas 4 Gas 5 Gas 6 Gas 7
Gas
per
mea
bili
ty
Fig. 3 Specific gas permeability values of the seven different
vacuum pressures for control treatment (9 10-13 m3/m) (CC Control
central specimens, CM control marginal specimens)
Abb. 3 Kennwerte der Gaspermeabilitat der Kontrollplatte bei 7
verschiedenen Vakuumdrucken (9 10-13 m3/m)
Table 2 Correlation analysis of the 7 gas permeability time values of
different water column heights with liquid permeability time values in
the control treatment (1st drop and 50-mm lowering time)
Gas and water permeabilities Gas 1 Gas 2 Gas 3 Gas 4 Gas 5 Gas 6 Gas 7
1st Drop time 0.83 ** (?) 0.86 ** (?) 0.89 ** (?) 0.90 ** (?) 0.91 ** (?) 0.93 ** (?) 0.95 ** (?)
50-mm lowering time 0.89 ** (?) 0.92 ** (?) 0.94 ** (?) 0.95 ** (?) 0.96 ** (?) 0.97 ** (?) 0.99 ** (?)
Gas 1 1 1.00 ** (?) 0.99 ** (?) 0.99 ** (?) 0.98 ** (?) 0.97 ** (?) 0.94 ** (?)
Gas 2 1 1.00 ** (?) 1.00 ** (?) 0.99 ** (?) 0.98 ** (?) 0.96 ** (?)
Gas 3 1 1.00 ** (?) 1.00 ** (?) 0.99 ** (?) 0.98 ** (?)
Gas 4 1 1.00 ** (?) 0.99 ** (?) 0.98 ** (?)
Gas 5 1 1.00 ** (?) 0.99 ** (?)
Gas 6 1 1.00 ** (?)
Gas 7 1
Gas 1–7: The 7 water column heights for measuring gas permeability making 7 vacuum pressures
NS Non significant
(?) Positive correlation
** Correlation is significant at the l % level (2-tailed)
* Correlation is significant at the 5 % level (2-tailed)
Gas Permeability (Gas 7)
0
0.05
0.1
0.15
0.2
0.25
0.3
0.35
0.4
0.45
Control NZ50 NZ100 NZ150
Sp
ecif
ic g
as p
erm
eab
ility A
BB
C
Fig. 4 Specific gas permeability values for control, NZ-50, NZ-100,
and NZ-150 treatments (9 10-13 m3/m) (NZ = nanozycosil)
Abb. 4 Kennwerte der Gaspermeabilitat der Kontrollplatte sowie der
Platten mit 50 (NZ-50), 100 (NZ-100) und 150 (NZ-150) g/kg Nano-
Zycosil (9 10-13 m3/m)
Eur. J. Wood Prod. (2013) 71:353–360 357
123
consumption level of NZ, resulting in more wood fiber-
integration and consequent lowering the gas permeability.
More than this NZ-content, however, resulted in enlarge-
ment of the micro-cavities to the extent that the binding
property of NZ could not compensate for.
NZ-100 treatment showed an overall highest 1st-drop
liquid permeability time, showing the highest imperme-
ability of this treatment against water (Fig. 5). Further-
more, NZ-50 showed the highest impermeability in terms
of 50-mm lowering time (Fig. 6). The highest liquid per-
meability (the lowest times) was observed in NZ-150
treatment, although not much difference was observed in
comparison to control specimens for both liquid perme-
ability times. This shows the impermeability effects of
nanozycosil against water penetration. That is, NZ-150
treatment showed nearly similar liquid permeability atti-
tude towards water to the control treatment, although this
treatment had the most micro-cavities and showed the
highest specific gas permeability. Water-repellant effects of
zycosil nanoparticles were also noticeable in NZ-50 and
NZ-100 treatments, although showing different attitude
towards the two liquid permeability times.
Cluster analysis was carried out based on the specific
gas permeability and the two liquid permeability times
(Fig. 7). Results of this analysis showed an overall simi-
larity between control and NZ-100 treatments. This proves
that zycosil nanoparticles have the potentiality to keep the
permeability properties of MDF constant regardless of the
lower fiber content and more micro-cavities. However, NZ-
150 was clustered quite differently, showing that the NZ-
particles could no longer compensate the effects of micro-
cavities on the permeability values. NZ-50 treatment was
clustered quite differently with the other three treatments.
It can therefore be concluded that this NZ-consumption
level could be recommended to improve impermeability
against water in MDF. The density of all four treatments
was kept constant in the present study to highlight the
water-repellant effects of zycosil nanoparticles. However,
NZ-application without decreasing the wood fiber volume
may be studied to come to a final decision for industrial
purposes.
Liquid permeability (1st drop)
0
2000
4000
6000
8000
10000
12000
14000
Control NZ50 NZ100 NZ150
Sec
on
d
A
B BB
Fig. 5 Liquid permeability of the 1st-drop for the four treatments of
control, NZ-50, NZ-100, and NZ-150 treatments (s) (NZ nanozycosil)
Abb. 5 Flussigkeitspermeabilitat bezogen auf den Beginn des
Abtropfens bei der Kontrollplatte sowie der Platten mit 50, 100 und
150 g/kg Nano-Zycosil
Liquid permeability (50-mm-lowering time)
0
5000
10000
15000
20000
25000
Control NZ50 NZ100 NZ150
Sec
on
d
A
BBCBC
Fig. 6 Liquid permeability of the 50-mm lowering time for the four
treatments of control, NZ-50, NZ-100, and NZ-150 (s) (NZ nano-
zycosil)
Abb. 6 Flussigkeitspermeabilitat bezogen auf die 50 mm-Absen-
kdauer bei der Kontrollpatte sowie der Platten mit 50, 100 und 150 g/kg
Nano-Zycosil
Fig. 7 Cluster analysis based on gas permeability value as well as the two liquid permeability times for the four treatments of control, NZ-50,
NZ-100, and NZ-150 (NZ nanozycosil)
Abb. 7 Clusteranalyse basierend auf den Kennwerten der Gaspermeabilitat und der beiden Flussigkeitsdurchlassigkeitszeiten der Kontrollplatte
sowie der Platten mit 50, 100 und 150 g/kg Nano-Zycosil
358 Eur. J. Wood Prod. (2013) 71:353–360
123
4 Conclusion
1. MDF with lower densities would usually have higher
specific gas permeability values; however, nano-zy-
cosil can alter this trend to some extent.
2. Zycosil water-repellant property decreases water
permeability in MDF to the extent that it even compen-
sates the micro-cavities resulted from the lower fiber-
content.
3. Consumption level of 50 g of zycosil nanoparticles/kg dry
weight fibers may be recommended for industrial pur-
poses to increase impermeability property towards water.
Acknowledgments The author is thankful to Mr. Mohammad Aieni,
the managing director, and Engin. Mohammad Taghi Kazemi, the
production manager, of Sanaye Choobe Khazar Co. (MDF Caspian
Khazar, htp://www.choobekhazar.com), for procurement of the nec-
essary fiber and raw materials for the present research project. The
technical consultancy of Mr. Younes Sarvari Samadi is also appreci-
ated. I am also grateful to Zydex Industries for preparation of Nano-
Zycosil liquid. Last but not least, we pay our tribute to Mr. Majid
Ghazizadeh, the internal sales manager of Pars Chemical Industries
Company, for the procurement of the resin for the present study.
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