2010
DOI: 10.1016/j.energy.2010.02.024
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Catalytic pyrolysis of biomass: Effects of pyrolysis temperature, sweeping gas flow rate and MgO catalyst

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Cited by 240 publications
(74 citation statements)
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“…Decline in the bio-oil yield was observed with nitrogen flow between 40 to 60 mL/min. This could be as a result of short vapor residence time in the condenser coil which has contributed to yield more non-condensable gas (Uzun et al 2007;Pütün 2010;Keles et al 2011;Soetardji et al 2014). Generally, an increase in the yield of non-condensable gas was observed with increasing nitrogen flow, while bio-char yield decreased due to the rapid removal of pyrolysis vapor from the reaction zone.…”
Section: Effects Of Nitrogen Flow Rate and Reaction Temperature On Pymentioning
confidence: 93%
“…Decline in the bio-oil yield was observed with nitrogen flow between 40 to 60 mL/min. This could be as a result of short vapor residence time in the condenser coil which has contributed to yield more non-condensable gas (Uzun et al 2007;Pütün 2010;Keles et al 2011;Soetardji et al 2014). Generally, an increase in the yield of non-condensable gas was observed with increasing nitrogen flow, while bio-char yield decreased due to the rapid removal of pyrolysis vapor from the reaction zone.…”
Section: Effects Of Nitrogen Flow Rate and Reaction Temperature On Pymentioning
confidence: 93%
“…Unlike gasification, pyrolysis process consists of a thermal degradation of the initial solid biomass into gases and liquids without an oxidizing agent [21,26]. The products of biomass pyrolysisprimarily consist of biochar, bio-oil and gases including CH 4 , H 2 , CO and CO 2 [27,28]. Pyrolysis offers a flexible and attractive way of converting solid biomass into an easily stored and transported liquid fuels [29].…”
Section: Introductionmentioning
confidence: 99%
“…However, some recent studies on crop stems (Stals et al, 2010), wood (French & Czernik, 2010) and coconut shells (Siengchum, Isenberg, & Chuang, 2013) have demonstrated the use of fixed-bed batch reactors for HHR pyrolysis. Moreover, a typical HHR pyrolysis is performed with a short vapor residence time of 1-5 s, while some studies reveal residence times of 30-88 s in the pyrolysis of rise husk (Tsai, Lee, & Chang, 2007) and cotton seed (Putun, 2010) in fixed-bed reactors. Based on these investigations, the current study employs a fixed-bed reactor for both SHR and HHR pyrolysis of lignocellulosic biomass from herbaceous (wheat straw, timothy grass) and forestry (pinewood) resources.…”
Section: Introductionmentioning
confidence: 99%