Evaluation of
adsorptive properties of mesoporous materials by sorption
fibers
Du Xinzhen1,2, Tao
Xiaojuan, Wang Yarong1, Ding Ning1, Chen
Hui1 (1 Department of Chemistry, Northwest Normal
University, Lanzhou 730070; 2 The Key Laboratory of Polymer
Materials of Gansu Province, Lanzhou 730070, China)
Received Mar.10,
2006;Supported by the National Natural
Science Foundation of China (No: 20575053), the Natural Science Foundation
of Gansu Province (3ZS051-A25-011-022) and the Key Laboratory of Polymer
Materials of Gansu Province.
Abstract Mesoporous
silica and composite were used as fiber coatings to evaluate their
adsorptive properties. A diffusion-controlled process was involved for the
adsorption of toluene, p-xylene, biphenyl and anthracene onto
mesoporous materials in water matrix. Vigorous stirring and heating of the
solution are favorable for the diffusion of the studied compounds. The
fiber coated with phenyl-MCM-41 shows high adsorption efficiency and good
molecular recognition but negative effect of salt on adsorption of target
compounds. Rapid desorption could be obtained in aqueous solution
containing methanol. The fiber is easy to prepare and handle. Moreover,
only a small quantity of adsorption material was needed to prepare the
sorption fibers compared with conventional batch sorption experiments. The
fibers are inexpensive, durable and easy to couple with HPLC. Quantitative
adsorption and desorption was obtained with good reproducibility. The
coated fibers offer an alternative way to evaluate the adsorption behavior
of potential adsorption or separation materials. Keywords
Adsorption; mesoporous silica; sorption fibers; aromatic
compounds
1. INTRODUCTION Since
the discovery of the novel M41S mesoporous materials [1],
extensive attention was paid to them to be served as adsorbents and
separation materials because they have larger specific surface area and
uniform mesostructure [2]. Organic compounds and metal ions can
selectively adsorb onto the surface of mesoporous materials
[3-7], especially mesoporous composites [8-12]. For
the purpose of better understanding of adsorption behavior of synthesized
materials, batch sorption experiments of target compounds onto the
adsorbents were usually performed by adding a certain amount of adsorbent
(20~200mg) to a solution which is stirred continuously or allowed to stand
for 10-24 h on a platform shaker to ensure that the adsorption equilibrium
is reached. The slurries were centrifuged or filtered. Subsequently the
concentration of target compounds in the supernatants or filtrates were
measured using conventional analytical techniques. The amount of
specifically adsorbed compounds was calculated by the difference between
initial and final concentration of corresponding compound in solution. The
procedures are tedious and expensive. For these reasons, an attempt was
made to use MCM-41 mesoporous silica as the coatings of sorption fibers
which integrate the adsorption, concentration and sample introduction in a
single step. The cylindrical surface geometry of the fibers is well
defined and allows easy access of target compounds to and from the
surface, leading to efficient adsorption and desorption. The miniature
dimensions of the fiber are also convenient to couple with HPLC [13,
14]. Several factors affecting the adsorption and desorption
properties were studied. The adsorption efficiency and selectivity were
also discussed.
2. EXPERIMENTAL 2.1.
Materials Tetraethyl orthosilicate (Shanghai Chemical Reagents
Co.), cetyltrimethylammonium bromide (Beijing Chemical Reagents Co.),
toluene (To) and p-xylene (Xy) (Tianjin Chemical Reagents Co.),
biphenyl (Bp) and anthracene (An) (China National Medicines Co.), sodium
chloride (Shanghai Hunter Fine Chemicals Ltd.) and trimethoxyphenylsilane
(Fluka) were of analytical grade. Pure mesoporous silica was synthesized
following the procedures of the literature [15]. The removal of
template was carried out in ethanol containing 1
mol·L-1 hydrochloric acid.
One-step synthesis of phenyl functionalized MCM-41 was improved by
consulting with the literature [16]. Doubly distilled water was
used. 2.2. Analysis and methods The structure of the
synthesized material was characterized by a D8 diffratometer (Bruker,
Germany). Identification of organic functional groups was performed on 670
infrared spectrometer (Nicolet, USA) and the percentage of C and H was
estimated by 2400 CHN elemental analyzer (Perkin-Elmer, USA). The specific
surface area was determined by the Brunauer-Emmett-Teller on an ASAP 2010
instrument (Micromeritics, USA). The measured physical parameters of the
synthesized materials were listed in Table 1. The thermal stability of
mesoporous composite was examined on D4 thermogravimetric system
(Shimazdu, Japan). The thickness of fiber coatings was measured using
micrometer caliper. The coated fiber was characterized by a JSM-5600LV
scanning electron microscope (JEOL, Japan). The efficiency of adsorption
was estimated on LC-6A liquid chromatograph (Shimazdu, Japan) with a
Waters C18 column and SPD-6AV UV-Vis absorbance
detector.
Table 1 Physical parameters
of synthesized mesoporous materials
Materials |
Surface area
(m2·g-1) |
Carbon load
(%) |
Pore size
(nm) |
Phenyl-MCM-41 MCM-41 |
927.89 1362.48 |
30.10 0.00 |
2.13 2.87 |
2.3. Preparation of sorption
fibers The fiber was modified from a commercial 1-ml HPLC syringe. The
plunger wire (160 mm o.d.) inside the needle was cleaned with ethanol
and dried at 60oC. The mesoporous particles were immobilized
onto the steel wire with epoxy glue. The coated plunger wire was heated
for cure at 80oC for 8
hours. The fiber coating is 10 mm long and 10 mm thick. Fig. 1 shows SEM
image of the sorption fiber coated with phenyl-MCM-41. The coated fibers
were conditioned in mobile phase of HPLC for 30 min to free from
contaminants prior to use.
 Fig. 1 Scanning
electron micrograph of phenyl-MCM-41 coated fiber.
2.4. Procedures
The protecting needle of the fiber was pierced into the glass bottle
sealed with a silicone septum and the coated fiber was exposed to the
stirred solution containing To, Xy, Bp and An of 1.00×10-6 mol×
L-1 for adsorption respectively. The adsorption was carried out
on a heated stirring platform with the magnetic stirring rate of 1000 rpm
at 20 oC. The needle holding the coated fiber was withdrawn
from the water matrix and introduced into desorption chamber connected
with six-port injection valve of HPLC for 5-min static desorption in
methanol/water (70/30 v/v) when the injection valve was in the load
position. Subsequently the valve was switched to the injection position
for the delivery of target compounds to the chromatographic column at the
flow-rate of 1 ml× min-1. Chromatographic peak area was
utilized to examine direct adsorption efficiency of mesoporous
materials.
3. RESULTS AND
DISCUSSION 3.1 Adsorption Fig. 2 shows time
dependence of the adsorption process for the fibers with MCM-41 and
phenyl-MCM-41. A period of time was practically needed to reach their
adsorption equilibrium for all of the compounds. Adsorption equilibrium of
MCM-41 coating was almost established within 60 min. When phenyl-MCM-41
was used as the fiber coating, the amount adsorbed was increased but
longer adsorption time was required to reach equilibrium. The equilibrium
time for adsorption process increases with decreasing pore size of
mesoporous materials and with increasing molecular size of target
compounds. Actually it is not necessary to reach the equilibrium for
adsorption process. The adsorption time of 30 min is a reasonable
compromise between chromatographic peak area and adsorption time for
MCM-41 and phenyl-MCM-41 coatings.
 Fig. 2 Dependence of the adsorption on
time.
3.2 Desorption
Solvent desorption of the adsorbed compounds in the injector is the
reverse process of adsorption. Fig. 3 gives typical desorption time
profiles of phenyl-MCM-41 coating in methanol/water. There is a little
mass transfer resistance during the desorption process which is much fast
compared to that of adsorption process. 1-min and 3-min are enough to
reach the equilibrium of desorption for To and Xy as well as Bp and An,
respectively. The ratio of methanol and water in mobile phase has a
significant effect on the desorption process. Large amount content of
methanol in mobile phase leads to more rapid desorption. This is
supportive of the fact that adsorption and desorption processes are
dynamically controlled by diffusion in the mesoporous materials.
 Fig. 3
Dependence of the desorption on time. Adsorption time, 30
min.
3.3 Mass transfer
Stirring is very important because adsorption is a dynamic
diffusion-controlled process. Fig. 4 compares the dependence of adsorption
on stirring rate. The adsorption of MCM-41 coating is faster in the
stirred solutions and 1000 rpm is enough to approach perfect stirring. For
the phenyl-MCM-41 coating, however, the adsorption process greatly depends
on the degree of agitation. As a result of small pore size of
phenyl-MCM-41, one can infer that the diffusion process is slower because
perfect stirring is difficult to be achieved in the smaller mesopores of
phenyl-MCM-41. There is larger resistance of mass transfer for the
diffusion of the adsorbed compounds from bulk solution into the smaller
pores of phenyl-MCM-41 than that of MCM-41, especially for the diffusion
of Bp and An.

Fig. 4 Dependence of the adsorption on
stirring rate. Adsorption time, 30 min.
Generally temperature also plays an important role in adsorption process
because of its potential influence on thermodynamics and kinetics of
adsorption process of target compounds between fiber coating and water
matrix. High temperature is unfavorable to adsorption of target compounds
because adsorption is generally an exothermic process. However, both
MCM-41 and phenyl-MCM-41 coated fibers presented a positive effect of
temperature on adsorption of target compounds. Furthermore the adsorption
efficiencies increased with the increasing temperature of water matrix to
a greater extent for phenyl-MCM-41 coating. It clearly indicates that mass
transfer is the predominant factor during adsorption process for
mesoporous materials. For the sake of avoiding the volatility of aromatic
compounds, 20 ℃ was
employed. 3.4 Ionic strength Fig. 5 shows the dependence of
adsorption on the ionic strength of water matrix for phenyl-MCM-41 coated
fiber. The amount adsorbed decreases with increasing concentration of the
salt. This result may arise from the increased ionization of silanols at
the surface of mesoporous coating by the addition of sodium ions
[17]. The concentration of adsorbed sodium ions at the
liquid-solid interface is higher than that in bulk solution, which changes
the physical properties in the mesopores. Consequently higher
concentration of sodium chloride results in lower concentration of target
compounds at the interfacial area compared to the bulk solution because
higher concentration of salt causes a decreased solubility of nonpolar
compounds in water matrix. On the other hand, addition of salt can
increase the viscosity of aqueous solution, especially the solution at
liquid-solid interface. This may limit the diffusion of target compounds
from bulk solution to the mesoporous surface of fiber coating and result
in lower adsorption efficiency of studied
compounds.
 Fig. 5 Dependence of the adsorption on ionic
strength. Adsorption time, 30 min.
3.5 Efficiency and selectivity
of adsorption
The adsorption efficiency of mesoporous materials depends on the
partitioning of the target compound between fiber coating and water
matrix. As shown in Fig. 2, high concentration of the studied compounds
was obtained on the phenyl-MCM-41 fiber than the MCM-41 one. Table 2
summarizes the distribution constants (KD) of four
compounds. Adsorption efficiency of MCM-41 coating suggests that larger
surface area plays a sole role in adsorption process. The polar surface of
MCM-41 shows decreasing affinity in the order: To>Xy>Bp>An, in
agreement with that of their solubility in water. After chemical
modification at the surface of MCM-41, adsorption efficiency of
phenyl-MCM-41 coating was about 2~4 times greater than that of MCM-41
coating although the surface area of phenyl-MCM-41 decreases to some
extent compared to that of MCM-41. Clearly, surface modification also
greatly contributes to higher adsorption efficiency.
However, it should be noted that the adsorption behavior of phenyl-MCM-41
coating was very different from that of MCM-41 coating. As shown in Table
2, the KD values for toluene and biphenyl are larger
than those for p-xylene and Anthracene on the phenyl-MCM-41 coating,
respectively. This indicates that selectivity of adsorption was achieved
by hydrophobic nature and smaller mesopores in adsorption process when the
mesoporous surface was chemically bonded with phenyl group. Surface
modification is thermodynamically favorable to the adsorption process of
Bp and An with low solubility but results in larger resistance of mass
transfer from bulk solution to smaller mesopores. Thereby it takes longer
time to reach adsorption equilibrium for Bp and An.
Table 2 Distribution
constants of aromatic compounds
Phase
type |
KD |
Toluene |
p-Xylene |
Biphenyl |
Anthracene |
Phenyl-MCM-41 MCM-41 |
1071 644 |
873 480 |
1692 400 |
902 288 |
3.6 Stability of sorption
fibers Ryco et al reported that the structure of MCM-41 mesoporous
silica was completely lost upon boiling in water for two days due to
silicate hydrolysis [18]. In batch sorption experiments, the
structural collapse may have a significant effect on the adsorption
behavior of materials. According to the procedures described, the
cylindrical surface geometry of the fibers allows easy access of target
compounds to and from the surface, leading to efficient adsorption and
desorption in a short time. Furthermore, phenyl-silylation of MCM-41
effectively enhances the hydrothermal stability. The custom made fiber
with phenyl-MCM-41 coating can at least withstand 200
adsorption-desorption cycles toward vigorous stirring and desorption under
the conditions employed. The lifetime of the phenyl-MCM-41 coating becomes
much longer than that of pure mesoporous silica coating. Relative standard
deviation of five replicate adsorption-desorption runs is 0.10%~1.60% for
To, Xy, Bp and An of 1.00×10-6 mol× L-1 in spiked
water.
4. CONCLUSIONS The
fibers coated with MCM-41 and phenyl-MCM-41 were prepared to examine the
adsorptive properties of the synthesized materials. The adsorption of
mesoporous coatings involves a diffusion-limited process. The
phenyl-MCM-41 coating shows greater adsorption efficiency and better
selectivity of target compounds than MCM-41 one. A regeneration of the
fiber coating can be performed by desorption in methanol/water and the
original adsorption efficiency was obtained again. The sorption fibers can
tolerate many adsorption-desorption cycles under the experimental
conditions. As compared with conventional batch sorption experiments, the
sorption fiber was prepared with the adsorption material of less than 10
mg. Rapid and quantitative adsorption and desorption of target compounds
can easily be achieved with good reproducibility by coupling HPLC.
Consequently the sorption fiber is a useful tool for obtaining information
about potential adsorption or separation materials.
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吸附探头法评价介孔材料的吸附性质 杜新贞, 陶小娟, 王亚荣, 丁宁,
陈慧 (西北师范大学化学系, 兰州 730070) 摘要
以介孔二氧化硅及其复合体作为探头涂层评价了介孔材料的吸附性质,在水基体中,介孔材料对甲苯、对二甲苯、联苯和蒽的吸附过程受扩散控制,充分搅拌和加热有利于所研究芳烃分子的扩散。phenyl-MCM-41探头涂层有高的吸附效率和良好的分子识别能力,但盐效应不利于吸附,探头吸附物在甲醇/水溶液中可快速解吸。该探头易于制作,而且与常规批量吸附试验相比所需吸附材料很少,成本低,可多次重复作用,可与HPLC联用,定量吸附和解吸重现性好,为潜在吸附分离材料的评价提供了一种选择途径。 关键词
吸附; 分离; 介孔二氧化硅; 吸附探头; 芳香烃
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