2008
DOI: 10.1016/j.energy.2008.01.002
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Steam cracking and methane to olefins: Energy use, CO2 emissions and production costs

Abstract: While most olefins (e.g., ethylene and propylene) are currently produced through steam cracking routes, they can also possibly be produced from natural gas (i.e., methane) via methanol and oxidative coupling routes. We reviewed recent data in the literature and then compared the energy use, CO 2 emissions and production costs of methane-based routes with those of steam cracking routes. We found that methane-based routes use more than twice as much process energy than state-of-the-art steam cracking routes do (… Show more

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Cited by 129 publications
(144 citation statements)
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“…Industrially, olefins are produced via steam cracking of hydrocarbons [216]. The technology used for this process can be energy intensive and expensive to operate [217]. As an alternative, alkanes can be oxidatively-dehydrogenated, typically over transition metal oxides, to yield olefins and oxygenates [218][219][220].…”
Section: The Oxidation Of Alkanesmentioning
confidence: 99%
“…Industrially, olefins are produced via steam cracking of hydrocarbons [216]. The technology used for this process can be energy intensive and expensive to operate [217]. As an alternative, alkanes can be oxidatively-dehydrogenated, typically over transition metal oxides, to yield olefins and oxygenates [218][219][220].…”
Section: The Oxidation Of Alkanesmentioning
confidence: 99%
“…2 Nowadays most of the ethylene is produced via steam cracking, an inefficient process from an energetic viewpoint. 3 Therefore the search for alternatives to produce ethylene in a more energetically favorable way is highly interesting. Thus, oxidative dehydrogenation (ODH) of ethane is considered as a viable and interesting alternative for the industrial manufacture of ethylene.…”
Section: Introductionmentioning
confidence: 99%
“…Currently, ethylene is mainly produced by "steam cracking" of hydrocarbons which is the most energy-consuming process in the chemical industry [3]. A possible industrial alternative is the oxidative dehydrogenation of ethane to ethylene (ODHE), an exothermic process which can operate at only 300-400 o C in which the catalyst deactivation by coke can be minimized because of the presence of molecular oxygen as an oxidant in the reactor feed [4,5].…”
Section: Introductionmentioning
confidence: 99%