کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
43539 | 45976 | 2007 | 7 صفحه PDF | دانلود رایگان |

The effects of coprecipitated silica were investigated in iron-based catalysts for Fischer–Tropsch Synthesis (FTS). Silica-containing catalysts exhibited micro pores (<10 nm) and large specific surface areas, while the silica-free catalyst had large pores (10–100 nm) and low specific surface area.Coprecipitated silica enhances the productivity of hydrocarbon for FTS, especially C5+ hydrocarbon selectivity.Silica-free and silica-containing iron catalyst showed high activity and stability over 100 h test, and exhibited little difference of the product selectivity (olefin/paraffin ratio) over the temperature range of 513–553 K.An iron catalyst has higher activity with the low H2/CO ratio (0.4–1.0). Thus, an iron catalyst has the advantage in applications to coal-derived gas, as compared to the cobalt-based catalyst.
The effects of coprecipitated silica were investigated in iron-based catalysts for Fischer–Tropsch Synthesis (FTS). Silica-containing catalysts exhibited micro pores (<10 nm) and large specific surface areas, while the silica-free catalyst had large pores (10–100 nm) and low specific surface area.Coprecipitated silica enhances the productivity of hydrocarbon for FTS, especially C5+ hydrocarbon selectivity. Silica-free and silica-containing iron catalyst showed high activity and stability over 100 h test. Figure optionsDownload as PowerPoint slide
Journal: Applied Catalysis A: General - Volume 328, Issue 2, 10 September 2007, Pages 117–123