2011
DOI: 10.1016/j.ijhydene.2011.04.204
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Experimental investigation of chemical-looping hydrogen generation using Al 2 O 3 or TiO 2 -supported iron oxides in a batch fluidized bed

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Cited by 107 publications
(56 citation statements)
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“…The study discuses in detail the methodology used to evaluate the performances using critical design factors such as, gasifier feeding system, heat and power integration analysis and potential ways to increase the overall energy efficiency. A few experimental studies have also been performed in order to determine the appropriate OC and the steam conversion rate [19,20]. All these studies are based on combinations of power plant arrangements, fuels and OCs.…”
Section: Introductionmentioning
confidence: 99%
“…The study discuses in detail the methodology used to evaluate the performances using critical design factors such as, gasifier feeding system, heat and power integration analysis and potential ways to increase the overall energy efficiency. A few experimental studies have also been performed in order to determine the appropriate OC and the steam conversion rate [19,20]. All these studies are based on combinations of power plant arrangements, fuels and OCs.…”
Section: Introductionmentioning
confidence: 99%
“…Further, dynamic modeling study of moving bed reactors have been carried out to reveal the inert characteristics of the reactors [19e21]. Meanwhile, fluidized bed reactors commonly used in chemical looping combustion (CLC) showed some limitations for deep reduction of iron oxides when fuel conversion was high [10,22,23]. Xiang and Xue et al [24,25] suggested a compact fluidized bed reactor system as the reducer which was consisting of a bubble fluidized bed, a riser, a cyclone and a dipleg to solve this disadvantage.…”
Section: Introductionmentioning
confidence: 99%
“…Because hydrogen is the major compound of synthesis gas (syngas) from the biomass/coal gasification process, hydrogen was therefore utilized as a fuel in CLC testing [1,2]. Five cycles of reduction-oxidation TG data were obtained for the SrCuO 2 oxygen carrier at the 600-800°C temperature range, shown in Fig.…”
Section: Stability Of Cyclic Combustion and Regeneration Clc Reactionsmentioning
confidence: 99%
“…In the fuel reactor, fuel (for example, methane, synthesis gas, coal, biomass) reacts with a solidstate oxygen carrier. In consequence, the fuel is oxidized to CO 2 and H 2 O [2], while the metal oxide is reduced to the metal oxide at a lower oxidation state or to its metallic form. After the water condensation, a pure stream of CO 2 in fuel reactor is obtained.…”
Section: Introductionmentioning
confidence: 99%