2020
DOI: 10.1016/j.fuproc.2020.106515
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Synthetic natural gas production from the three stage (i) pyrolysis (ii) catalytic steam reforming (iii) catalytic hydrogenation of waste biomass

Abstract: This is a repository copy of Synthetic natural gas production from the three stage (i) pyrolysis (ii) catalytic steam reforming (iii) catalytic hydrogenation of waste biomass.

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Cited by 23 publications
(3 citation statements)
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References 60 publications
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“…Although recycling clearly has a critical role to play in reducing the amount of waste, there is further opportunity and environmental benefit in recovering energy from what might previously have been seen as materials destined for landfill [1][2][3]. In particular, advanced thermochemical technologies, like pyrolysis or gasification, have an important role to play in converting waste into clean energy or fuels, hence promoting the green energy transition [4][5][6][7][8]. When needed for thermochemical conversions, MSW is typically transformed to refuse derived fuel (RDF), which is the recovered non-recyclable fraction of MSW, after mechanical treatment, partial drying and removal of recyclable materials.…”
Section: Introductionmentioning
confidence: 99%
“…Although recycling clearly has a critical role to play in reducing the amount of waste, there is further opportunity and environmental benefit in recovering energy from what might previously have been seen as materials destined for landfill [1][2][3]. In particular, advanced thermochemical technologies, like pyrolysis or gasification, have an important role to play in converting waste into clean energy or fuels, hence promoting the green energy transition [4][5][6][7][8]. When needed for thermochemical conversions, MSW is typically transformed to refuse derived fuel (RDF), which is the recovered non-recyclable fraction of MSW, after mechanical treatment, partial drying and removal of recyclable materials.…”
Section: Introductionmentioning
confidence: 99%
“…Most of the catalysts are applied in the production of synthetic gas from glycerol and are composed mainly of carbon and hydrogen oxides, using reagents such as steam and CO 2 (dry). Among these techniques, catalytic steam reforming generally occurs when a significant amount of carbon monoxide reacts with the added steam and undergoes the water vapor displacement reaction that results in the formation of carbon dioxide and hydrogen [42], while glycerol dry reforming (GDR) offers a better way to produce H 2 as it uses greenhouse gas (CO 2 ) as a raw material. Furthermore, this reaction can be conducted at atmospheric pressure while producing a high yield of H 2 [43,44].…”
Section: Industrial Wastementioning
confidence: 99%
“…Produk gas dari reaktor reformasi uap terdiri dari karbon monoksida dan hidrogen. Studi optimasi dari steam reforming menunjukkan bahwa prosesnya berlangsung pada suhu tinggi 800 ℃ dengan adanya katalis untuk meningkatkan proses reformasi uap katalitik [15]. Produk syngas hasil steam reforming akan dilanjutkan menuju sebuah cooler untuk didinginkan suhunya sebelum memasuki reaktor water-gas shift.…”
Section: Ch4+h2o⇄3h2+counclassified