“…RESULTS AND DISCUSSION Despite significant differences in the experimental procedure, the results correspond well to those obtained under almost identical conditions (tempera ture, pressure, and residence time of reagents in the reactor) reported in [10][11][12][13]; this is the consequence of the gas phase character of the process, which is mainly determined by its macrokinetic parameters. In both series of studies, the propane conversion strongly increased with the oxygen concentration.…”
Section: Results Of Experimentssupporting
confidence: 80%
“…In both series of studies, the propane conversion strongly increased with the oxygen concentration. The compo sition of the products is also the same, not only quali tatively, but also quantitatively, despite the lower initial [C 3 H 8 ]/[O 2 ] ratio in [10][11][12][13]. The significant increase in temperature led to a decrease in the propylene con centration in both series, while the ethylene concen tration remained the same and even slightly increased (Fig.…”
Section: Results Of Experimentsmentioning
confidence: 73%
“…As shown in [10][11][12][13], in the presence of oxygen under certain conditions, the process occurs by the branched chain mechanism, which dramatically increases the concentration of chain carriers (active radicals) and, accordingly, the propane conversion. These results confirm the significant difference between the mechanisms of homogeneous and heter ogeneous oxidative conversion of propane [11] and prospects for gas phase oxidation of light alkanes as a method for the production of olefins and as a method for selective purification of hydrocarbon gases from heavy hydrocarbon impurities [12].…”
Section: Results Of Experimentsmentioning
confidence: 99%
“…Thus, at 43% propane conversion, the selectivity of its conversion into propylene reached 38 mol %, and the total selectivity of the formation of propylene and ethylene was 75 mol % [9]. In recent studies on the oxidative conversion of light alkanes С 2 -С 5 , including in the presence of a large excess of methane [10][11][12][13] under slightly different experimen tal conditions, the results were generally in good agreement with the results of [6,8,9].…”
The influence of the initial concentration of oxygen and temperature on the oxidative conversion of propane in a two sectional flow reactor at constant pressure and contact time was studied. It was shown that an increase in the initial concentration of oxygen not only increases the conversion of propane, but also affects the ratio of the reaction products. The yield of ethylene and propylene was found to depend on the initial propane to oxygen ratio and reaction temperature.
“…RESULTS AND DISCUSSION Despite significant differences in the experimental procedure, the results correspond well to those obtained under almost identical conditions (tempera ture, pressure, and residence time of reagents in the reactor) reported in [10][11][12][13]; this is the consequence of the gas phase character of the process, which is mainly determined by its macrokinetic parameters. In both series of studies, the propane conversion strongly increased with the oxygen concentration.…”
Section: Results Of Experimentssupporting
confidence: 80%
“…In both series of studies, the propane conversion strongly increased with the oxygen concentration. The compo sition of the products is also the same, not only quali tatively, but also quantitatively, despite the lower initial [C 3 H 8 ]/[O 2 ] ratio in [10][11][12][13]. The significant increase in temperature led to a decrease in the propylene con centration in both series, while the ethylene concen tration remained the same and even slightly increased (Fig.…”
Section: Results Of Experimentsmentioning
confidence: 73%
“…As shown in [10][11][12][13], in the presence of oxygen under certain conditions, the process occurs by the branched chain mechanism, which dramatically increases the concentration of chain carriers (active radicals) and, accordingly, the propane conversion. These results confirm the significant difference between the mechanisms of homogeneous and heter ogeneous oxidative conversion of propane [11] and prospects for gas phase oxidation of light alkanes as a method for the production of olefins and as a method for selective purification of hydrocarbon gases from heavy hydrocarbon impurities [12].…”
Section: Results Of Experimentsmentioning
confidence: 99%
“…Thus, at 43% propane conversion, the selectivity of its conversion into propylene reached 38 mol %, and the total selectivity of the formation of propylene and ethylene was 75 mol % [9]. In recent studies on the oxidative conversion of light alkanes С 2 -С 5 , including in the presence of a large excess of methane [10][11][12][13] under slightly different experimen tal conditions, the results were generally in good agreement with the results of [6,8,9].…”
The influence of the initial concentration of oxygen and temperature on the oxidative conversion of propane in a two sectional flow reactor at constant pressure and contact time was studied. It was shown that an increase in the initial concentration of oxygen not only increases the conversion of propane, but also affects the ratio of the reaction products. The yield of ethylene and propylene was found to depend on the initial propane to oxygen ratio and reaction temperature.
“…Moreover, the methane content even increases, since it is one of the main products of oxycracking of its heavier homologues [11,14,20]. The main products of the oxycracking of methane homologues are ethylene, methane, ethane, hydrogen, and carbon monoxide, with ethane and propylene being present in small amounts [17,[20][21][22]. The presence of a heterogeneous catalyst significantly accelerates the process at low temperatures, but impedes it at higher temperatures, at which an abrupt transition to the branched-chain-reaction mode occurs.…”
Section: Selective Oxycracking Of Heavier Components Of Natural Gasmentioning
Recent developments in unconventional natural gas production increase the need for principally new small-scale technologies for gas processing and transportation. The promising way for small-scale gas processing is its autothermal partial oxidation to syngas or direct partial oxidation to chemicals. The paper considers some prospective gas chemical processes based on the partial oxidation of light alkanes. Among them are the conversion of natural gas to syngas in volumetric (3D) matrix burners made of a gas permeable material and direct conversion of methane to methanol without its preliminary conversion to syngas (DMTM). As a more simple technology that lets to use fat associated oil gas often flaring in remote sites, it can be suggested the selective oxidative cracking of heavier components of natural gas. This process converts heavy methane homologues from propane to pentane and heavier into ethylene, methane, ethane, hydrogen, and carbon monoxide, thus increasing methane index (octane number) of gas and making it suitable for feeding modern gas piston and gas turbine power engines. One more interesting prospect is the creation of technologies making use of the subsequent processing of valuable oxycracking products, such as olefins, CO, and hydrogen, for example, by their catalytic co-polymerization without preliminary separation from gas phase. The co-polymerization of CO and ethylene, followed by the separation of resulting liquid products, can considerably improve the economic attractiveness of the oxycracing process. Thus, despite the absence of economically proved and industrial-scale tested smallcapacity direct and indirect gas chemical technologies, intensive efforts to develop such alternative technologies let to expect near bright future for them.
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