کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
9702792 | 1462921 | 2005 | 15 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Transient behaviour of a small methanol reformer for fuel cell during hydrogen production after cold start
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی انرژی
انرژی (عمومی)
پیش نمایش صفحه اول مقاله
![عکس صفحه اول مقاله: Transient behaviour of a small methanol reformer for fuel cell during hydrogen production after cold start Transient behaviour of a small methanol reformer for fuel cell during hydrogen production after cold start](/preview/png/9702792.png)
چکیده انگلیسی
The best response from cold start was obtained with 960 W heating power, 80 °C heating temperature, 14 mL/min methanol and 70 L/min air supply rates among the experimented parameters. Under this operation setting, hydrogen was produced after 220 s from cold start with the production rate stabilising after 4-5 min and eventually reaching the highest concentration at 350 °C. Generally, hydrogen commenced production at a catalyst outlet temperature of 100 °C and stabilised at 350 °C.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Energy Conversion and Management - Volume 46, Issues 7â8, May 2005, Pages 1193-1207
Journal: Energy Conversion and Management - Volume 46, Issues 7â8, May 2005, Pages 1193-1207
نویسندگان
Rong-Fang Horng,