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Parametric Study fo...
Parametric Study for Production of Dimethyl Ether (DME) As a Fuel from Palm Wastes
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- Inayat, A. (författare)
- Department of Sustainable and Renewable Energy Engineering, University of Sharjah, Sharjah, United Arab Emirates
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- Ghenai, C. (författare)
- Department of Sustainable and Renewable Energy Engineering, University of Sharjah, Sharjah, United Arab Emirates
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- Naqvi, Muhammad, 1983- (författare)
- Mälardalens högskola,Framtidens energi,Mälardalens University,Universiti Teknologi Petronas, Malaysia
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- Ammar, M. (författare)
- Chemical Engineering Department, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, Perak, Malaysia
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- Ayoub, M. (författare)
- Chemical Engineering Department, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, Perak, Malaysia
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- Hussin, M. N. B. (författare)
- Chemical Engineering Department, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, Perak, Malaysia
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(creator_code:org_t)
- Amsterdam, Netherlands : Elsevier Ltd, 2017
- 2017
- Engelska.
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Serie: Energy Procedia, 1876-6102
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Ingår i: Energy Procedia. - Amsterdam, Netherlands : Elsevier Ltd. - 1876-6102. ; , s. 1242-1249
- Relaterad länk:
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https://doi.org/10.1...
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https://doi.org/10.1...
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https://urn.kb.se/re...
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https://doi.org/10.1...
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https://urn.kb.se/re...
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Abstract
Ämnesord
Stäng
- Dimethyl Ether (DME) has been getting numerous attention as it's potential as the second generation bio-fuel. Traditionally DME is produced from the petroleum based stock which involves two steps of synthesis (methanol synthesis from the syngas and DME synthesis from methanol). DME synthesis via single step is one of the promising methods that has been developed. In Malaysia, due to the abundance of oil palm waste, it is a good candidate to be used as a feedstock for DME production. In this paper, single step process of DME synthesis was simulated and investigated using the Aspen HYSYS. Empty Fruit Bunch (EFB) from palm wastes has been taken as the main feed stock for DME synthesis. Four parameters (temperature, pressure, steam/biomass ratio and oxygen/biomass ratio) have been studied on the H2/CO ratio and DME yield. The results showed that optimum H2/CO ratio of 1.0 has been obtained when having an oxygen to biomass ratio (O/B) of 0.37 and steam to biomass ratio (S/B) of 0.23. The increment in the steam to biomass ratio increased the production of DME while the increment in oxygen to biomass ratio will cause reduction in DME production. © 2017 The Authors.
Ämnesord
- TEKNIK OCH TEKNOLOGIER -- Maskinteknik -- Energiteknik (hsv//swe)
- ENGINEERING AND TECHNOLOGY -- Mechanical Engineering -- Energy Engineering (hsv//eng)
- TEKNIK OCH TEKNOLOGIER -- Kemiteknik (hsv//swe)
- ENGINEERING AND TECHNOLOGY -- Chemical Engineering (hsv//eng)
Nyckelord
- Aspen Hysys
- Biomass Gasification
- DME synthesis
- Process simulation
- Biomass
- Ethers
- Methanol
- Oxygen
- Palm oil
- Synthesis gas manufacture
- Empty fruit bunches
- Methanol synthesis
- Process simulations
- Second generation
- Single-step process
- Fuels
- Chemical Engineering
Publikations- och innehållstyp
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