کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
205672 461122 2015 12 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
A large-scale benchmark for the CFD modeling of non-catalytic reforming of natural gas based on the Freiberg test plant HP POX
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
A large-scale benchmark for the CFD modeling of non-catalytic reforming of natural gas based on the Freiberg test plant HP POX
چکیده انگلیسی


• Natural gas reforming at high pressures and temperatures was studied experimentally.
• A semi-industrial test plant with comprehensive instrumentation was used.
• A new optical system allows the flame zone to be studied directly.
• Measurements were carried out at different pressures and temperatures.
• The data set provides a challenging benchmark for numerical modeling.

The non-catalytic reforming of natural gas to syngas was studied with test runs at the semi-industrial scale test plant HP POX. The product gas composition, and gas and wall temperatures across the reactor were considered at 50, 60 and 70 bar(g), while the reactor temperature was varied between 1200 and 1400 °C. In addition, the flame structure was studied using optical measurements. The experiment was designed to provide a challenging benchmark for numerical modeling. For that reason, the reactor geometry, boundary conditions, and the experimental data are provided in such a way that the results can easily be reproduced using CFD.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel - Volume 152, 15 July 2015, Pages 110–121
نویسندگان
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