Formaldehyde Oxidation Over Platinum: On the Kinetics Relevant to Exhaust Conditions of Lean-Burn Natural Gas Engines

被引:7
作者
Torkashvand, Bentolhoda [1 ]
Maier, Lubow [2 ]
Lott, Patrick [1 ]
Schedlbauer, Thomas [1 ]
Grunwaldt, Jan-Dierk [1 ,2 ]
Deutschmann, Olaf [1 ,2 ]
机构
[1] KIT, Inst Chem Technol & Polymer Chem ITCP, D-76131 Karlsruhe, Germany
[2] KIT, Inst Catalysis Res & Technol IKFT, D-76344 Eggenstein Leopoldshafen, Germany
关键词
Formaldehyde; Platinum; Kinetic Model; Surface reaction mechanism; Lean-burn gas engines; CATALYTIC PARTIAL OXIDATION; CO OXIDATION; METAL-CATALYSTS; MOLECULAR-BEAM; TEMPERATURE; HYDROGEN; METHANE; COMBUSTION; MECHANISM; EMISSIONS;
D O I
10.1007/s11244-018-1087-y
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Kinetics of formaldehyde oxidation over Pt-based catalytic converters at oxygen-rich conditions related to the exhaust of lean-burn natural gas engines is investigated experimentally and numerically. The numerical model proposed in this work is based on a thermodynamically consistent detailed surface reaction mechanism consisting of 30 elementary-like-steps among six gas-phase and ten surface species. The surface mechanism is evaluated by comparison of the results of the numerical simulation with the experimental measurements. The experimental data are derived from isothermal end-of-pipe tests over a powdered Pt-TiO2-SiO2 catalyst as well as spatially resolved concentration measurements conducted with a catalytic monolith sample over a wide range of temperature. The measurements were performed in a gas mixture of 80ppm HCHO, 10vol% O-2, 12vol% H2O and 6vol% CO2 balanced with N-2, containing a formaldehyde concentration typical in the exhaust of lean-burn gas engines. The simulations are based on a one-dimensional approach for the description of a packed-bed reactor and a two-dimensional model for the calculation of flow field and chemical reactions inside a single channel of a monolith.
引用
收藏
页码:206 / 213
页数:8
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