1998
DOI: 10.1016/s0196-8904(98)00052-1
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Exergy analysis of chemical-looping combustion systems

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Cited by 194 publications
(161 citation statements)
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“…The gasified syngas from coal is combusted by oxygen carriers in the fuel reactor, the syngas combustion is described as reaction (11) However, IGCC system as a post-combustion technology requires separating CO 2 with additional recovery system that energy penalty is estimated 17.5% resulted in declining of electricity generation efficiency from 46 to 39.3% HHV (Amelio et al, 2007). Chemical looping is proposed to be combined with IGCC for syngas combustion to reduce energy penalty for CO 2 capture, and the exergetic power efficiency was estimated as high as 48.7% by employment of Fe 2 O 3 as oxygen carrier in chemical looping combustion (Anheden and Svedberg, 1998). The simulation for coal direct chemical looping combustion was estimated around 50% for electricity generation with over 90% CO 2 capture (Li and Fan, 2008).…”
Section: Methane Reforming Reaction: Ch 4 + H 2 O ↔ Co + 3h 2 (7)mentioning
confidence: 99%
“…The gasified syngas from coal is combusted by oxygen carriers in the fuel reactor, the syngas combustion is described as reaction (11) However, IGCC system as a post-combustion technology requires separating CO 2 with additional recovery system that energy penalty is estimated 17.5% resulted in declining of electricity generation efficiency from 46 to 39.3% HHV (Amelio et al, 2007). Chemical looping is proposed to be combined with IGCC for syngas combustion to reduce energy penalty for CO 2 capture, and the exergetic power efficiency was estimated as high as 48.7% by employment of Fe 2 O 3 as oxygen carrier in chemical looping combustion (Anheden and Svedberg, 1998). The simulation for coal direct chemical looping combustion was estimated around 50% for electricity generation with over 90% CO 2 capture (Li and Fan, 2008).…”
Section: Methane Reforming Reaction: Ch 4 + H 2 O ↔ Co + 3h 2 (7)mentioning
confidence: 99%
“…Natural gas [7][8][9], refinery and industrial gases [10,11], synthesis gas from coal gasification [12][13][14], and coal [15,16] have been considered to be used as fuels in a CLC system. The use of syngas from coal gasification in a CLC process could be advantageous still using solid fossil fuels [17].…”
Section: Introductionmentioning
confidence: 99%
“…Together with the iron oxides, some extra inner material has been added to the circulating streams of oxygen carrier, since it has been reported that this may be necessary to ensure the required physical stability of the fine solid particles that contain the oxides [10]. The quantity of 0.27 mol of ZrO2 per mol of circulating FeO has been introduced for this purpose, following the same procedure as in ref.…”
Section: Clhg Reactorsmentioning
confidence: 99%
“…The quantity of 0.27 mol of ZrO2 per mol of circulating FeO has been introduced for this purpose, following the same procedure as in ref. [11], which is an intermediate value between those recommended by [7] and [10]. This inert material acts does not take part in any chemical transformation, and it acts in fact just as a heat carrier between the three reactors.…”
Section: Clhg Reactorsmentioning
confidence: 99%
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