Authors: Pimpawee Keawpapasson, Chayanee Tippayasam, Silawat Ruangjan, Pajaree Thavorniti, Thammarat Panyathanmaporn, Alexandre Fontaine, Cristina Leonelli, Duangrudee Chaysuwan
Abstract: Porous concretes such as aerated and lightweight concretes are commonly used in construction fields. Lightweight construction materials are used to reduce either the weight or the budget of building structures. Porous concrete production is widely utilised aluminium (Al) powder to increase pores in concrete structures and giving information for porous geopolymer production. It was introduced by adding 0.05-1% Al-powder as the initiated materials of geopolymers, to react with water in those materials and promote hydrogen gas inside specimens. The research, therefore, focused on the synthesis of porous geopolymer by metakaolin as a pozzolan and mixed with alkali solution (8M NaOH and Na2SiO3) as well as Al-powder as a foaming agent. The highly porous geopolymers were produced with various Al-powders as 0%, 0.2%, 0.4%, 0.6% 0.8% and 1% by weight. After 7, 14 and 28 days age, the specimens were tested the mechanical properties, such as compressive and flexural strengths. The water absorption, apparent porosity and bulk density were analyzed at 28 days age. The synthesis of metakaolin-based porous geopolymers with Al-powder presented good results. It showed that Al-powder content affected to degree of porosity of geopolymers. Keywords: Metakaolin based geopolymer, Porous geopolymer, Aluminium powder, Foaming agent, Mechanical and physical properties
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Authors: Angkhana Jaroenworaluck, Thammarat Panyathanmaporn, B. Soontornworajit, Sitthisuntorn Supothina, Sittinun Tawkaew, Siriya Jiamsakul, Tawan Sooknoi
Abstract: TiO2 and V-doped TiO2 gel were synthesized and coated onto porous α-Al2O3 beads to
study the thermal catalytic activities of oxidation reactions. Titanium isopropoxide (Ti(OPr)4) and
1,2-butadiol(Bu(OH)2) were used as starting chemicals for preparation of TiO2 gel without Vdoping.
After aging at ambient temperature for one week, a TiO2 gel was obtained. The
concentration of Ti(OPr)4 was varied, 0.2, 0.3, 0.7 and 2.4 M was used. For V-doping of the TiO2
gel, 0.05, 0.20 and 0.75 mole% of V was prepared by ultrasonically dissolving vanadium
acetylacetone (V(acac)2) in 1,2-butadiol. The solutions were then added to Ti(OPr)4. Finally, the
mixed solutions were kept under ambient temperature for one week to form the V-doped TiO2 gel.
TiO2 and V-doped TiO2 were calcined at 300, 400, 500, 600, 700, and 800 °C. XRD analysis, SEM
and TEM in conjunction with EDS analysis were used to identify the phases present, grain size and
morphology. The TiO2 grains have a particle size in the nano-scale range. Doping TiO2 with V
could retard growth of the TiO2 particles and affect phase transformation at higher calcination
temperatures. Both the TiO2 and V-doped TiO2 gels were prepared and coated onto α-Al2O3 beads
to test oxidation reactions in a purpose-designed reactor. The results of the catalytic reactions
indicated that V-doped TiO2 had a higher oxidation activity than the undoped TiO2 gel. The content
of vanadium was related to the reaction efficiency.
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Authors: Thammarat Panyathanmaporn, Angkhana Jaroenworaluck, Sitthisuntorn Supothina, Rung-Arun Chumnanklang, Kannikar Juengsuwattananon, Supatra Jinawath, Tawan Sooknoi, Siriya Jiamsakul, Sittinun Tawkaew
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.
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Authors: O. Nimittrakoolchai, Thammarat Panyathanmaporn, Angkhana Jaroenworaluck, Sitthisuntorn Supothina
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.
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Authors: Sittinun Tawkaew, Tawan Sooknoi, Angkhana Jaroenworaluck, Thammarat Panyathanmaporn, Sitthisuntorn Supothina
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.
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