2015
DOI: 10.1016/j.fuel.2015.07.087
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Experimental and kinetic modeling study of the oxy-fuel oxidation of natural gas, CH4 and C2H6

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Cited by 19 publications
(7 citation statements)
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“…The produced H 2 O 2 is then consumed by hydrogen-based and methane-based reactions, for example R19, for the formation of high reactive OH radicals and the initiation of the fuel ignition. Moreover, the produced CH 3 interacts with O 2 via R4 for the production of formaldehyde and OH [56,57]. Therefore, it can be said that R2 is an intermediate reaction that affects the production of OH via the production of H 2 O 2 and CH 3 .…”
Section: Methane-based Reactionsmentioning
confidence: 99%
“…The produced H 2 O 2 is then consumed by hydrogen-based and methane-based reactions, for example R19, for the formation of high reactive OH radicals and the initiation of the fuel ignition. Moreover, the produced CH 3 interacts with O 2 via R4 for the production of formaldehyde and OH [56,57]. Therefore, it can be said that R2 is an intermediate reaction that affects the production of OH via the production of H 2 O 2 and CH 3 .…”
Section: Methane-based Reactionsmentioning
confidence: 99%
“…However, CO 2rich flue gas is required to increase the efficiency and economy during carbon capture and storage. Several new advanced combustion technologies that use O 2 /CO 2 as an oxidizer, such as oxy-fuel combustion technology (Buhre et al, 2005;Wall, 2007;Hjärtstam et al, 2009;Rathnam et al, 2009;Scheffknecht et al, 2011;Taniguchi et al, 2011;Chen et al, 2012;Dhaneswar and Pisupati, 2012;Luo et al, 2015;Moroń and Rybak, 2015;Liu et al, 2016;Ge et al, 2017;Seddighi, 2017;Menage et al, 2018;Zhang et al, 2018), moderate or intense low-oxygen dilution (MILD) oxy-combustion (Li et al, 2013;Tu et al, 2015;Mardani and FazlollahiGhomshi, 2016;Mao et al, 2017;Gładysz et al, 2018), gaseous fuel-fired oxy-fuel combustion technology (Yin et al, 2011;Seepana and Jayanti, 2012a;Seepana and Jayanti, 2012b;Oh et al, 2013a;Oh et al, 2013b;Oh and Noh, 2014;Giménez-López et al, 2015;Oh and Noh, 2015;Oh and Hong, 2016;Bürkle et al, 2018), and high-temperature oxygen combustion technology (Li et al, 2014;Li et al, 2015;Li et al, 2016), have been developed to meet this requirement. However, many other challenges must be solved before these combustion technologies can be widely adopted in the industry, since the differences in the physical properties and chemical characteristics of CO 2 and N 2 can lead to important distinctions in flame structure.…”
Section: Introductionmentioning
confidence: 99%
“…Outras abordagens para a estabilização incluem: o uso de bluff-bodies que estabilizam a chama na região de recirculação, pré-aquecimento, coflow, chamas-piloto, ecoamento Swirl entre outros. No caso particular da oxi-combustão com oxidante rico em dióxido de carbono, diversos estudos experimentais e numéricos (LIU et al, 2001;BENTZEN, 2007;MENDIARA;GLARBORG, 2009;GIMÉNEZ-LÓPEZ et al, 2015) observaram uma redução nas taxas de reação e temperatura da zona de reação. A causa deste efeito ainda é controversa, há autores que o relacionam com a maior capacidade térmica do dióxido de carbono em relação ao nitrogênio, o que levaria a uma redução na temperatura e por conseguinte nas taxas de reação (LIU et al, 2001 Na literatura, a reação 3.2 é considerada a principal fonte de radicais OH * ativados e seu tempo de vida é da ordem de grandeza de 1 µs(GAYDON, 2012).…”
Section: Combustãounclassified
“…Independente do mecanismo, todos devem ser calibrados com base em dados experimentais. Nesse procedimento as reações químicas ocorrem no interior de um reator controlado e instrumentado permitindo a medição simultaneamente de diversas espécies químicas ao longo do tempo em uma dada temperatura, como feito em(GIMÉNEZ-LÓPEZ et al, 2015).Para o metano o mecanismo mais consagrado e estudado é o GRI3.0 que foi avaliado em experimentos de velocidade de chama laminar (MAAREN; THUNG; GOEY, 1994), de Ignição em Shock-Tubes (WOIKI et al, 1998) e em reatores isotérmicos (ALZUETA; GLARBORG; DAM-JOHANSEN, 1997).…”
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