2016
DOI: 10.4236/wjet.2016.41011
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Review on Innovative Catalytic Reforming of Natural Gas to Syngas

Abstract: Decreasing supplies of high quality crude oil and increasing demand for high quality distillates have motivated the interest in converting natural gas to liquid fuels, especially with the present boom in natural gas proven reserves. Nevertheless, one major issue is the curtailment of costs incurred in producing synthesis gas from natural gas, which account for approximately 60% of the costs used in producing liquid fuels. While there are three main routes to convert natural gas to syngas: steam reforming (SMR)… Show more

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Cited by 99 publications
(54 citation statements)
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“…The simulation of methane steam reforming ( Fig 4) used a Gibbs reactor to carry out reaction calculations based on minimizing the Gibbs energy for the system without the need for detailed stoichiometry or yield. Other reforming processes (Table 3) were simulated similarly on Aspen Plus® following operating conditions from the literature [40]. Auto-thermal reforming (ATR) of methane steam, dry and tri-reforming are coupled with a partial oxidation reaction (exothermic); the heat supplied by partial oxidation was completely used by the subsequent endothermic reforming reactions [40], so no input power is required in the simulations.…”
Section: Fuel Oil Power Station (Ops)mentioning
confidence: 99%
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“…The simulation of methane steam reforming ( Fig 4) used a Gibbs reactor to carry out reaction calculations based on minimizing the Gibbs energy for the system without the need for detailed stoichiometry or yield. Other reforming processes (Table 3) were simulated similarly on Aspen Plus® following operating conditions from the literature [40]. Auto-thermal reforming (ATR) of methane steam, dry and tri-reforming are coupled with a partial oxidation reaction (exothermic); the heat supplied by partial oxidation was completely used by the subsequent endothermic reforming reactions [40], so no input power is required in the simulations.…”
Section: Fuel Oil Power Station (Ops)mentioning
confidence: 99%
“…Other reforming processes (Table 3) were simulated similarly on Aspen Plus® following operating conditions from the literature [40]. Auto-thermal reforming (ATR) of methane steam, dry and tri-reforming are coupled with a partial oxidation reaction (exothermic); the heat supplied by partial oxidation was completely used by the subsequent endothermic reforming reactions [40], so no input power is required in the simulations. The output or input materials in equation 5 varied depending on the specific requirements of the subsequent process in the production chain.…”
Section: Fuel Oil Power Station (Ops)mentioning
confidence: 99%
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“…This proof copy is the copyright property of the publisher and is confidential until formal publication. o0030 (5) Combined reforming of methane (CMR) o0035 (6) Reforming with membrane o0040 (7) Tri-reforming of methane (TMR) [31] p0095…”
Section: P0025mentioning
confidence: 99%
“…To date, a significant amount of work has been conducted to convert methane into useful chemicals, for instance, syngas, methanol, light olefins, aromatic compounds, etc. Syngas is made of H2 and CO, which plays an important role in chemical industry because it is the feedstock for the manufacture of a wide range of chemicals, such as ammonia, acetic acid, MTBE, methanol, olefins, gasoline, phosgene, oxo-alcohols and synthetic liquid fuels 3 . Although it can be generated using raw materials such as coal, biomass, petroleum coke and natural gas, its production using natural gas as the feedstock is the most cost-effective option 4 .…”
Section: Introductionmentioning
confidence: 99%