کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
154663 456848 2015 13 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Predicting optimal temperature profiles in single-stage fixed-bed reactors for CO2-methanation
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Predicting optimal temperature profiles in single-stage fixed-bed reactors for CO2-methanation
چکیده انگلیسی


• We present a method to compute optimal temperature profiles in fixed-bed reactors.
• We predict optimal temperature profiles for the methanation of CO2.
• These temperature profiles result in a twofold improvement of the methane-yield.
• The results demonstrate the potential of improved heat transport in catalyst supports.

The catalytic conversion of carbon dioxide into methane, known as Sabatier process, is a promising option for chemical storage of excess renewable energy and greenhouse gas emission control. Typically externally cooled fixed-bed reactors (FBR) using supported nickel or ruthenium catalyst are applied. The Sabatier process, however, is strongly exothermic and leads to substantial hot spots within the reactor at stoichiometric feed ratios. Although high temperatures increase the reaction rate in general, they thermodynamically limit the achievable methane-yield in the Sabatier process. Here, we present an easy-to-use method based on a Semenov number optimization (SNO) to compute optimal axial temperature profiles in single-stage fixed-bed reactors that account for kinetic and thermodynamic limitations simultaneously, and thus result in maximized yield for a fixed reactor length. In a case study on CO2-methanation, these temperature profiles result in a twofold improvement of the methane-yield compared to isothermal and adiabatic operation, and thus demonstrate the high potential of thermal optimization that lies in the Sabatier process. The SNO-method provides a valuable tool to compute optimal temperature profiles, and allows intuitive insight into the key parameters for thermal process intensification. Further, it can readily be transferred to other processes that suffer from the dilemma between kinetic and thermodynamic limitations. Our findings illustrate the attractiveness of the SNO-method to compute optimal temperature profiles in fixed-bed reactors, and the need for catalyst supports with enhanced and tailorable heat transport properties.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Science - Volume 132, 18 August 2015, Pages 59–71
نویسندگان
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