Removal of dibenzothiophenes in kerosene by adsorption on rice husk activated carbon
Introduction
An extremely low sulfur content of the hydrogen produced from the reforming of hydrocarbon fuels is a key factor for fuel cell use. To suppress poisoning of the reforming and generating catalysts, the sulfur content of the hydrocarbon fuel should be as low as possible prior to fuel injection [1]. It is generally agreed that a sulfur content of <100 mass ppb is required for fuel cell applications [2]. Conventional hydrodesulfurization (HDS) is widely applied to reduce the sulfur content, but this does not remove all types of sulfur compound. Refractory sulfur compounds need to be removed by other cost-effective means, to promote the use of fuel cells. Song and Ma have comprehensively reviewed the approaches for deep desulfurization of hydrocarbon fuel [3].
Dibenzothiophene and its derivatives (hereafter called DBTs) contained in fuel oils such as kerosene and diesel oil are refractory poly-aromatic sulfur compounds. In particular, alkyl-substituted DBTs, i.e., 4-methyldibenzothiophene (4-MDBT) and 4,6-dimethyldibenzothiophene (4,6-DMDBT), are highly refractory [3], [4]. Modified HDS methods using catalysts such as CoMo and NiMo [5], [6], [7], [8], [9], [10], [11], [12], [13], γ-Irradiation using additives and catalysis [14], biodesulfurization [15], oxidative desulfurization [16], [17], and adsorptive desulfurization using porous materials [2], [18], [19], [20] have been proposed for the efficient removal of refractory DBTs from fuel oils. Desulfurization using activated carbons [21], [22], [23] or catalyst-loaded activated carbons [24], which can be performed at ambient temperature and pressure, has been intensively studied. This seems to be more realistic than other methods in economic terms and for operational safety reasons. Toida demonstrated that activated carbon with a specific pore structure could be used for the efficient and selective removal of DBTs [25]. An activated carbon with a composite micro-mesoporous structure and a large pore volume is required.
A huge quantity of rice husk (ca. 2 million metric tons) is produced every year as agricultural waste in Japan. A micro-meso composite structure was shown to be obtainable from rice husk subjected to chemical (alkaline) activation [26]. However, this activation process requires extensive alkali treatment and rinsing, which hinders its industrial realization and mass production. However, rice husk that is now considered as agricultural waste in Japan [27] may be converted into a cost-effective adsorbent to remove DBTs without the use of chemical activation.
In the present study, rice husk was converted into an activated carbon intended for DBT removal from kerosene using a CO2 gas activation method. Kerosene is widely used in Japan as a home heating fuel for portable and installed kerosene heaters, and can be readily purchased at filling stations or delivered to homes. Kerosene is a promising hydrogen source for fuel cells for domestic use in Japan. The DBTs adsorption capacity of rice husk activated carbon (RHAC) for commercial kerosene was evaluated in terms of the textural and chemical characteristics. The usefulness of activated carbon fiber (ACF) for ultra deep desulfurization of diesel oil has been examined by Sano et al. [28]. So, commercial micro-porous ACF was also tested as a reference.
Section snippets
Material preparation
Japanese rice husk samples were obtained by rice threshing performed in 2002–2004. The rice husk samples used are AK-OH (rice brand: Akita Komachi, production site: Ohgata, Akita Prefecture), AK-NI (Akita Komachi, Nishiki, Akita Prefecture), AK-OG (Akita Komachi, Ogachi, Akita Prefecture), HI-HO (Hitomebore, Honjo, Akita Prefecture), and KO-TO (Koshihikari, Toyooka, Shizuoka Prefecture). Samples of 10 g of raw rice husks were carbonized and activated in a stainless steel cylinder (SUS 304) with
Compositional, textural, chemical and adsorption characteristics of AK-OH activated under different conditions
RHACs were produced under different activation conditions from one type of rice husk (AK-OH). Table 3 shows the mass yield for the carbonization and activation process, as well as the elemental composition of activated AK-OH. The ash content increased with the activation temperature and time, while the content of hydrogen, carbon, and oxygen decreased. It is noteworthy that ash accounted for more than half of the activated AK-OH mass.
The pore structure of activated AK-OH was evaluated in
Conclusions
Japanese rice husks were first carbonized in N2 and then activated in CO2 at 800–900 °C for 1 h and at 850 °C for 0.25–3 h. The textural and chemical characteristics of RHACs obtained, as well as of ACF with much greater SBET and Vt, values, were evaluated to investigate the DBTs adsorption capacity in kerosene. A feature of the RHACs was a very high ash content, accounting for approximately half of their mass. The greatest CDBT value was observed for rice husk activated at 850 °C for 1 h, with a
Acknowledgements
This research was supported in part by the Industrial Technology Research Grant Program in 2006 from the New Energy and Industrial Technology Development Organization (NEDO) of Japan.
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