Abstract
We have investigated the kinetics and catalytic activity of CO 2-lignite gasification with various metal precursors as catalysts. K 2CO 3, Mn(NO 3) 2, and Ce(NO 3) 3 were used and impregnated on a coal using an evaporator. The gasification experiments were carried out with the low rank coal loaded with 5 wt% catalyst at the temperature range from 700~900 °C and atmospheric pressure with the N 2-CO 2 reactant gas mixture. The catalytic effect on the gasification rate of the low rank coal with CO 2 was determined by the thermogravimetric analyzer. It was observed that the low rank coal reached the complete carbon conversion regardless of the kinds of catalysts at 900 °C from the results of TGA. The catalytic activity was ranked as 5 wt% K 2CO 3 > 5 wt% Mn(NO 3) 2 > 5 wt% Ce(NO 3) 3 > Non-catalyst at 900 °C. The gasification rate increased with increasing the temperature. The activation energy of the catalytic gasification with 5 wt% K 2CO 3 was 119.0 kJ/mol, which was the lowest among all catalysts.
| Original language | English |
|---|---|
| Pages (from-to) | 312-318 |
| Number of pages | 7 |
| Journal | Applied Chemistry for Engineering |
| Volume | 22 |
| Issue number | 3 |
| State | Published - 2011.06 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 13 Climate Action
Keywords
- Char
- CO
- Gasification
- K CO
- Lignite
- Low rank coal
Quacquarelli Symonds(QS) Subject Topics
- Engineering - Chemical
- Chemistry
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