2020
DOI: 10.1016/j.cej.2019.123659
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Simultaneous NO/CO2 removal by Cu-modified biochar/CaO in carbonation step of calcium looping process

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Cited by 27 publications
(3 citation statements)
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“…Large amounts of by-product CO 2 produced by SRE courses are commonly regarded as the primary cause of hydrogen purity degradation, while intolerable greenhouse issues abound. [158,159] As a result, to produce high hydrogen output, it is preferable to remove CO 2 in situ [149] and modify the reaction path accordingly according to LeChatelier's Principle, [160] (Eq ( 16)). As illustrated in the global reaction Eq.…”
Section: Sorption Enhanced Steam Reforming Of Ethanolmentioning
confidence: 99%
“…Large amounts of by-product CO 2 produced by SRE courses are commonly regarded as the primary cause of hydrogen purity degradation, while intolerable greenhouse issues abound. [158,159] As a result, to produce high hydrogen output, it is preferable to remove CO 2 in situ [149] and modify the reaction path accordingly according to LeChatelier's Principle, [160] (Eq ( 16)). As illustrated in the global reaction Eq.…”
Section: Sorption Enhanced Steam Reforming Of Ethanolmentioning
confidence: 99%
“…To achieve such an ambitious target, key supply-side technologies include novel energy-storage systems, carbon capture and utilization (CCUS) and zero-carbon electricity production are proposed [3]. Among these, CCUS using various hightemperature solid sorbents (hydrotalcites [4], MgO-based sorbents [5,6], ceramic materials [7], and calcium oxides [8][9][10]), have been considered as promising approaches for mitigating CO2 emissions from the top-emitting industries, namely: power plants, cement, iron & steel, and chemicals & plastics owing to their potential for increased useful energy production and decreased operating costs [11]. Moreover, these high-temperature sorbents are suitable for sorption enhanced methane reforming processes by shifting the thermodynamic equilibrium towards the production of high H2 yields, such as in the Sorption Enhanced Steam Methane Reforming (SESMR), the Sorption Enhanced Chemical Looping Reforming of Methane (SE-CL-RM), and the Super-Dry Chemical Looping Reforming of Methane (SD-CL-RM) [12][13][14].…”
Section: Introductionmentioning
confidence: 99%
“…It is superior in terms of NO x reduction efficiency, but it is accompanied by expensive operation costs and ammonia leakage. Therefore, quite a few scholars focus on reducing the initial formation of NO x by low-NO x combustion techniques to avoid employing SCR technique or to minimize its operation cost.…”
Section: Introductionmentioning
confidence: 99%