Materials Science Forum
Vol. 555
Vol. 555
Materials Science Forum
Vol. 554
Vol. 554
Materials Science Forum
Vol. 553
Vol. 553
Materials Science Forum
Vols. 551-552
Vols. 551-552
Materials Science Forum
Vol. 550
Vol. 550
Materials Science Forum
Vols. 546-549
Vols. 546-549
Materials Science Forum
Vols. 544-545
Vols. 544-545
Materials Science Forum
Vols. 539-543
Vols. 539-543
Materials Science Forum
Vols. 537-538
Vols. 537-538
Materials Science Forum
Vols. 534-536
Vols. 534-536
Materials Science Forum
Vols. 532-533
Vols. 532-533
Materials Science Forum
Vols. 530-531
Vols. 530-531
Materials Science Forum
Vols. 527-529
Vols. 527-529
Materials Science Forum Vols. 544-545
Paper Title Page
Abstract: 1) Upon comparing Ceramic products, which have been made into samples by the exactly
same construction method as prefabbed wall of apartment, with the existing products, it is revealed
that there would beno diminution effect on Pollutants like TVOC and HCHO. On the contrary, from
the Ceramic applied prefab-wall, some pollutants, which were not seen from normal wall-panel, had
been emitted additionally. 2) When we spreaded seven kinds of catalyst products on the surface of
samples of MDF furniture and tested, two of those applied samples showed stronger tendency
regarding the TVOC and HCHO emission than unapplied samples. Consequently, it is clarified that
there's no effect of eliminating the pollutants like TVOC and HCHO from the application of catalysts
as well as ceramic. In this regard, when we consider all the results collectively which were earned
from these analysises up to now, using indiscreet after-treatment materials in residential place should
be applied only after prudent examination.
1
Abstract: A photocatalytic system for wastewater treatment from textile industries was constructed
and tested for its efficiency. The system consisted of two units – a photoreactor for dye
decomposition and a catalyst recovery unit. The photoreactor was an annular plug flow photoreactor
under irradiation of 36 W Toshiba blacklight. The catalyst recovery unit was 42 L of sediment tank
for TiO2 catalyst recovery. In our study, a Cibra Cron red R-W 150% (an anionic azo dye) was used
to prepare a synthetic textile wastewater. The experimental parameters such as flow rate, pH, dye
initial concentration, catalyst loading and setteled time that affected the system performance were
investigated. The photodegradation kinetics were found to follow the Langmuire - Hinshelwood
model and also depended on the TiO2 concentration and the pH. The optimum condition for
photocatalytic decomposition was at pH 3 and at 1 g/L of TiO2 catalyst loading. The reaction rate
constant, k and the adsorption constant, K for the scale-up photoreactor were 3.345 mg/L-min and
0.0204 L/mg, respectively. For the catalyst recycle unit, the overflow and underflow concentration
of the TiO2 catalyst were 2.00 and 0.002 mg/L, respectively, at 100 ml/min of inlet flow rate, 50
ml/min of overflow and 50 ml/min of underflow.
5
Abstract: Adhesion between TiO2 coatings and the fabrics was improved by using a silane adhesive
agent. To investigate a suitable method of applying adhesive agent, two different coating methods
were conducted. The silane was either mixed with Ti precursor for fabric dipping, or coated onto
the fabrics before dipping them in a Ti precursor. The effect of Ti precursor, sol and colloid, on
coating morphology was also studied. It was found that continuous coating with no cracking was
obtained when the fabrics were pre-treated with the silane. The TiO2 coatings had good adhesion,
regardless of the method of applying the adhesive agent. Thick, cracked coatings were obtained
from Ti colloid precursor while continuous coating was obtained from the Ti sol precursor.
9
Abstract: Ag-doped TiO2 catalyst employed as the oxidation catalyst candidate was prepared by
two methods, co-precipitation and dip coating method. Co-precipitation method was conducted by
adding AgNO3 into the titanium precursor before gelation and then the obtained solution was coated
on the alumna beads. Dip coating method was conducted by coating the first layer on alumina beads
with titanium precursor followed by coating the second layer with AgNO3. The fired Ag-doped
TiO2 coated on alumina beads was used as catalyst for catalytic oxidation of methanol and carbon
monoxide by using oxygen as oxidizing agent in a gas-phase reactor. The methods of catalyst
preparation were found to affect the catalytic efficiency. Dip coating method showed better
oxidation reaction as Ag-doped TiO2 catalysts were well dispersed on the alumina beads.
13
Abstract: TiO2 photocatalysis has attracted a great deal of attention during the last three
decades. One major goal in this field is the design and preparation of TiO2 based photocatalysts
possessing high photocatalytic activity to satisfy the requirements for practical applications. For the
development of successful strategies to achieve this goal it is of utmost importance to improve the
mechanistic understanding of the basic principles of photocatalysis. Therefore, various nanosized
TiO2 photocatalysts including pure TiO2, Fe(III)-doped TiO2 and platinized TiO2 have been
synthesized in our laboratories and their photocatalytic activity has been studied in detail. In
particular, the correlation between the structural characteristics of these newly synthesized catalysts
and their photocatalytic activity has been addressed. To explain the unexpected behavior of these
materials novel mechanistic principles, i.e., the antenna mechanism and the so-called deaggregation
concept have been developed and will be explained in this review.
17
Abstract: The effect of various reaction factors such as amount of Ni loaded,
temperature, and variety of supports on the methane conversion were investigated to
obtain higher methane conversion. The high activities were observed over Ni(10
wt%)/SiO2 catalyst and at 650oC of reaction temperature. Catalysts using mesoporous
supports such as SiO2 and MCM-41 showed good catalytic activity and stability.
23
Abstract: TiO2 films were deposited by using mid-frequency twin magnetron reactive
sputtering technique at ambient temperature on quartz and Si wafer. The films were
annealed after deposition. The phase composition and surface morphology of the TiO2
films were characterized by X-ray diffraction, Raman spectroscopy, and scanning
electron microscopy, while the optical properties and contact angle were measured using
a UV-Vis spectrophotometer and a contact angle meter. It is indicated that anatase phase
dominates below 900°C and a mixture of rutile and anatase exists in the film annealed at
1000°C. Furthermore, the hydrophilic property depends on phase composition and
morphological change in TiO2 films.
27
Abstract: Even though activated carbon fibers (ACF) have been attractive due to high specific
surface area and uniform micropore structure, there are only a few reports about the photocatalyst
immobilization on ACF or their photodegradation behavior for removal of organic pollutants. In this
study, ACF were selected as adsorptive support for photocatalyst immobilization. As photocatalysts,
TiO2 nanoparticles were synthesized by using a N2-diluted and oxygen-enriched co-flow hydrogen
diffusion flame. The visible flame length of 150mm was obtained by direct photographs. Flame
temperature was measured by rapid insertion measurement technique with a R-type (Pt/Pt-13%Rd)
thermocouple which was in wire shape (127μm diameter). TiO2 particles were sampled by using a
high temperature particle sampler and then were coated on ACF filters. The sampling was carried out
at 70mm and 110mm above the burner. The structure of TiO2 particles was analyzed by XRD. TiO2
coated ACF filters were characterized by FESEM-EDX and BET analyses. TiO2 particles on ACF
filters were found to be agglomerated particles and the size of primary particles was approximately
50nm. The structure of TiO2 particle was anatase-phase crystalline structure. The specific surface
area of TiO2 coated ACF filter was enhanced to be 1700~1860m2/g, depending on the sampling
location, and the pores were micropores, regardless of the sampling location.
31