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231225s2020 xx |||||o 00| ||eng c |
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|a 10.1080/09593330.2019.1639828
|2 doi
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|a pubmed24n0995.xml
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|a (NLM)31264942
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|a DE-627
|b ger
|c DE-627
|e rakwb
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|a eng
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| 100 |
1 |
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|a Özcan, Merve Doğan
|e verfasserin
|4 aut
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| 245 |
1 |
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|a Thermodynamic modelling and optimization of oxy-reforming and oxy-steam reforming of biogas by RSM
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|c 2020
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|a Text
|b txt
|2 rdacontent
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|a ƒaComputermedien
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|2 rdamedia
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|a ƒa Online-Ressource
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|2 rdacarrier
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|a Date Completed 09.12.2019
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|a Date Revised 17.12.2019
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|a published: Print-Electronic
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|a Citation Status MEDLINE
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|a In this study, a comparative thermodynamic equilibrium calculation of biogas oxy-reforming and oxy-steam reforming processes to produce syngas has been conducted by Aspen Plus simulation software. The effects of temperature (600-800°C), pressure (1-20 atm), and inlet O2/CH4 (0-1.0), H2O/CH4 (0-3.0), and CO2/CH4 (0.3-1.0) mole ratios on the equilibrium compositions of products were determined. The operation of the process was optimized using Gibbs free energy minimization method and statistical approach: response surface methodology (RSM). Optimum operating conditions CH4/CO2/O2 = 1:0.51:0.12 at 788°C and 1 atm for oxy-reforming and CH4/CO2/H2O/O2 = 1:0.63:0.19:0.07 at 780°C and 1 atm for oxy-steam reforming were obtained to reach maximum H2 yield, CH4 and CO2 conversions by minimizing carbon selectivity to produce syngas for methanol production
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|a Journal Article
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|a Gibbs free energy minimization
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|a Hydrogen
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|a reforming processes
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|a response surface methodology
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|a syngas
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| 650 |
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|a Biofuels
|2 NLM
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|a Steam
|2 NLM
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| 650 |
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|a Hydrogen
|2 NLM
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| 650 |
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|a 7YNJ3PO35Z
|2 NLM
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| 700 |
1 |
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|a Özcan, Orhan
|e verfasserin
|4 aut
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| 700 |
1 |
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|a Akın, Ayşe Nilgün
|e verfasserin
|4 aut
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| 773 |
0 |
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|i Enthalten in
|t Environmental technology
|d 1993
|g 41(2020), 1 vom: 15. Jan., Seite 14-28
|w (DE-627)NLM098202545
|x 1479-487X
|7 nnns
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| 773 |
1 |
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|g volume:41
|g year:2020
|g number:1
|g day:15
|g month:01
|g pages:14-28
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|u http://dx.doi.org/10.1080/09593330.2019.1639828
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