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Non-Catalytic Partial Oxidation of C2+ Hydrocarbon/H2 Mixtures
https://orcid.org/https://orcid.org/0000-0001-9823-6844
https://orcid.org/https://orcid.org/0000-0002-6765-1401
https://orcid.org/https://orcid.org/0000-0002-8236-3854
https://orcid.org/https://orcid.org/0000-0001-9648-4895
https://orcid.org/https://orcid.org/0000-0003-0339-0297
The paper reports the results of a kinetic and thermodynamic analysis of non-catalytic partial oxidation of methane and C2–C4 hydrocarbon/hydrogen mixtures (C/H = 1 : 4) at 1400–1700 K. The hydrocarbon conversion sequence and the time periods of the major process stages were identified for isothermal conditions. The initial stage of the oxidative conversion of C2+ hydrocarbons consists of their pyrolysis, primarily into ethylene and propylene, followed by oxidation of the pyrolysis products. In this respect, the kinetics of C2+ hydrocarbon oxidative conversion are different from those of methane conversion, marked by the almost simultaneous and significantly slower occurrence of pyrolysis and oxidation. The subsequent stages involve steam and dry reforming of the oxidation products, namely acetylene and methane; these stages continue until the main products (H2, CO, CO2, and H2O) reach an equilibrium distribution for the given temperature. The study findings are important for the optimization of various techniques for high-temperature syngas production via partial oxidation of C2+ hydrocarbons, as well as Moderate or Intense Low-Oxygen Dilution (MILD) combustion processes.
Non-Catalytic Partial Oxidation of C2+ Hydrocarbon/H2 Mixtures
https://orcid.org/https://orcid.org/0000-0001-9823-6844
https://orcid.org/https://orcid.org/0000-0002-6765-1401
https://orcid.org/https://orcid.org/0000-0002-8236-3854
https://orcid.org/https://orcid.org/0000-0001-9648-4895
https://orcid.org/https://orcid.org/0000-0003-0339-0297
The paper reports the results of a kinetic and thermodynamic analysis of non-catalytic partial oxidation of methane and C2–C4 hydrocarbon/hydrogen mixtures (C/H = 1 : 4) at 1400–1700 K. The hydrocarbon conversion sequence and the time periods of the major process stages were identified for isothermal conditions. The initial stage of the oxidative conversion of C2+ hydrocarbons consists of their pyrolysis, primarily into ethylene and propylene, followed by oxidation of the pyrolysis products. In this respect, the kinetics of C2+ hydrocarbon oxidative conversion are different from those of methane conversion, marked by the almost simultaneous and significantly slower occurrence of pyrolysis and oxidation. The subsequent stages involve steam and dry reforming of the oxidation products, namely acetylene and methane; these stages continue until the main products (H2, CO, CO2, and H2O) reach an equilibrium distribution for the given temperature. The study findings are important for the optimization of various techniques for high-temperature syngas production via partial oxidation of C2+ hydrocarbons, as well as Moderate or Intense Low-Oxygen Dilution (MILD) combustion processes.
Non-Catalytic Partial Oxidation of C2+ Hydrocarbon/H2 Mixtures
https://orcid.org/https://orcid.org/0000-0001-9823-6844
https://orcid.org/https://orcid.org/0000-0002-6765-1401
https://orcid.org/https://orcid.org/0000-0002-8236-3854
https://orcid.org/https://orcid.org/0000-0001-9648-4895
https://orcid.org/https://orcid.org/0000-0003-0339-0297
The paper reports the results of a kinetic and thermodynamic analysis of non-catalytic partial oxidation of methane and C2–C4 hydrocarbon/hydrogen mixtures (C/H = 1 : 4) at 1400–1700 K. The hydrocarbon conversion sequence and the time periods of the major process stages were identified for isothermal conditions. The initial stage of the oxidative conversion of C2+ hydrocarbons consists of their pyrolysis, primarily into ethylene and propylene, followed by oxidation of the pyrolysis products. In this respect, the kinetics of C2+ hydrocarbon oxidative conversion are different from those of methane conversion, marked by the almost simultaneous and significantly slower occurrence of pyrolysis and oxidation. The subsequent stages involve steam and dry reforming of the oxidation products, namely acetylene and methane; these stages continue until the main products (H2, CO, CO2, and H2O) reach an equilibrium distribution for the given temperature. The study findings are important for the optimization of various techniques for high-temperature syngas production via partial oxidation of C2+ hydrocarbons, as well as Moderate or Intense Low-Oxygen Dilution (MILD) combustion processes.
Non-Catalytic Partial Oxidation of C2+ Hydrocarbon/H2 Mixtures
Pet. Chem.
Savchenko, V. I. (author) / Ozerskii, A. V. (author) / Nikitin, A. V. (author) / Sedov, I. V. (author) / Arutyunov, V. S. (author)
Petroleum Chemistry ; 63 ; 1353-1364
2023-12-01
12 pages
Article (Journal)
Electronic Resource
English
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