Photocatalytic degradation of terephthalic acid on sulfated titania particles and identification of fluorescent intermediates
Graphical abstract
Introduction
Terephthalic acid (TA) is widely used as a raw material to produce polyester fiber, polyethylene terephthalate (PET) bottles, PET films, engineering plastics and medicines, etc. In 2013, polyester fiber and PET bottle resin accounted for 93% global TA demand. Global TA production quantity was 46 million tons in 2013 and was forecasted to reach 66 million tons in 2020. TA is toxic and known as an endocrine disruptor [1], [2]. In addition, it may also interfere with the reproductive system and normal embryonic development of animals and humans. Traditional aerobic biological treatment method is slow and inefficient. Traditional coagulants for removal of TA included FeCl3, AlCl3, MgCl2, CaCl2, Al2(SO4)3, polyaluminium chloride, FeSO4 and polyelectrolyte [3], [4]. Recently, several advanced oxidation processes were investigated for the destruction of TA, including UV–TiO2, UV–H2O2, UV–H2O2–Fe, O3, O3/TiO2 and UV–O3–H2O2–Fe [5]. The UV–O3–H2O2–Fe method was extended to the degradation of wastewater from TA manufacturing [6]. Besides TiO2 photocatalysts, ZnO was also studied for TA degradation [7]. Although UV–TiO2 based method had been investigated, only pure Degussa P25 TiO2 was evaluated. In this work, we extend the study to sulfated titanium dioxide (SO42−/TiO2) photocatalysts with sulfate species on the surface which we reported to have good activities for the degradation of reverse osmosis concentrate (ROC) [8]. We then compare the efficiencies of SO42−/TiO2 and Degussa P25 photocatalysts for the destruction of TA.
TA is also widely used as a probing molecule for the important OH radicals generated from photocatalysts [9], [10], [11]. Mason monitored the OH radicals generated from acoustic cavitation with TA by measuring the fluorescent intermediate, namely 2-hydroxyterephthalic acid (2-HTA) [12]. Ishibashi developed a fluorescence method for determining the quantum yield of OH radical production during TiO2 photocatalysis [10], [11]. They used TANa (TA sodium salt) and coumarin to trap OH radicals to produce fluorescent intermediates, namely 2-HTA and 7-hydroxycoumarin. Since 2008, more researchers adopted the TA or TANa fluorescence probing method to determine OH radical formation and the photocatalytic activity of photocatalysts [9], [13], [14], [15], [16], [17], [18], [19], [20], [21], [22], [23], [24], [25], [26]. Nine intermediates had been reported, including 4 aromatic and 5 aliphatic intermediates. The 4 reported aromatic intermediates were 2-HTA, 4-hydroxybenzoic acid (4-HBA), benzoquinone and benzene [5], [9], [10], [11]. The 5 reported aliphatic intermediates were formic, acetic, oxalic, maleic and fumaric acids [5], [7]. However, there had been no comprehensive study of intermediates to date. In addition, for different photocatalysts the TA degradation pathways might be different and generate different intermediates. Therefore, we investigated the intermediates produced from the photocatalytic degradation of TA by SO42−/TiO2 photocatalysts compared with those by bare TiO2 and P25. 5 new intermediates were discovered and identified through silylation method using GC/MS and fluorescence spectroscopy. These newly discovered intermediates are complementary to the previously discovered ones and might provide new insights to the mechanism of photocatalytic degradation of TA. In addition, the relative ratios of fluorescent intermediates might also shed some light on the photocatalytic activity and different mechanisms of photocatalysis.
Section snippets
Preparation & characterization of photocatalysts
SO42−/TiO2 catalysts were prepared by the sol–gel method from the hydrolysis of titanyl sulfate according to the procedure reported previously [27], [28]. In a typical preparation, 4.0 g of titanyl sulfate was dissolved and hydrolysed in 100 ml of ethanol/water solution for 6 h. Then TiO2 slurry was filtered, washed and calcined at pre-determined temperatures for 1 h. In this work, the calcination temperatures were 300, 400 and 600 °C and the corresponding final catalysts were named as 3.85% SO42−
Photocatalyst characterization
3.85% SO42−/TiO2 (154.9 m2/g) exhibited Type I isotherm and was microporous. 3.79% SO42−/TiO2 (146.9 m2/g) exhibited type II isotherm and was non-porous. 1.38% SO42−/TiO2 (69.7 m2/g) and bare TiO2 (31.2 m2/g) exhibited type IV isotherms and were mesoporous (Fig. 1a, S3). All 4 samples were pure anatase (Fig. 1b) while P25 (49.8 m2/g) was a mixture of anatase and rutile (75:25). 3.85% SO42−/TiO2 and 3.79% SO42−/TiO2 had average primary crystallite size of 6 nm while 1.38% SO42−/TiO2 and those of bare
Conclusion
SO42−/TiO2 photocatalysts were efficient for the photocatalytic degradation of TA. Their activity increased with decreased S content. Photocatalytic activity of 1.38% SO42−/TiO2 was very close to bare TiO2 and P25. Six intermediates, i.e., A–F were identified, including 5 fluorescent (A–E) and 1 non-fluorescent (F) compounds: 1,2,4,5-tetrahydroxybenzene, 4-hydroxylbenzoic acid, hydroxyhydroquinol, 2,5-octadiene-4-oxo-dioic acid, 4-(hydroxylmethyl) benzene-1,3-diol and 2,5-heptadienedioic acid,
Acknowledgement
We acknowledge the financial support from the National University of Singapore, and Ministry of Education (R-143-000-519-112 and R-143-000-582-112). This work is supported by the Singapore National Research Foundation under its Environment and Water Technologies Strategic Research Programme and administered by the Environment and Water Industry Programme Office (EWI) of the PUB on project 1301-IRIS-21.
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