Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi
Refuse Derived Fuel (RDF) was pyrolysed at temperature ranges from 300°C to 800°C with heating rate of 10°C/min. The char yield decreased with increasing pyrolysis temperature up to 500°C, from 68.19% to 36.76% Above 500°C the char yield was almost constant. However, the gas yield (includes the loss...
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my.uitm.ir.816332023-08-15T07:36:28Z https://ir.uitm.edu.my/id/eprint/81633/ Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi Raja Deris, Raja Razuan Ryu, Changkook V. N., Sharifi Temperature Refuse Derived Fuel (RDF) was pyrolysed at temperature ranges from 300°C to 800°C with heating rate of 10°C/min. The char yield decreased with increasing pyrolysis temperature up to 500°C, from 68.19% to 36.76% Above 500°C the char yield was almost constant. However, the gas yield (includes the loss of fine oil droplets) shows an opposite trend, with increasing pyrolysis temperature. The oil production was almost stable above temperature 500°C. Liquid yield was very low which was below temperature 400°C because of the temperature was not sufficient enough for the RDF to pyrolyse. However, at temperature above 400°C, most of the oil produced has broken to yield more gas product. The analysis of pyrolysis gas showed that CO and CO2 are dominant in the early stage of pyrolysis. Hydrocarbon, H2 starts to appear at temperature above 500°C. 2006 Conference or Workshop Item PeerReviewed text en https://ir.uitm.edu.my/id/eprint/81633/1/81633.PDF Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi. (2006) In: Volume No. 1: Science and Technology, 30 – 31 May 2006, Swiss Garden Resort & Spa Kuantan, Pahang. |
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Refuse Derived Fuel (RDF) was pyrolysed at temperature ranges from 300°C to 800°C with heating rate of 10°C/min. The char yield decreased with increasing pyrolysis temperature up to 500°C, from 68.19% to 36.76% Above 500°C the char yield was almost constant. However, the gas yield (includes the loss of fine oil droplets) shows an opposite trend, with increasing pyrolysis temperature. The oil production was almost stable above temperature 500°C. Liquid yield was very low which was below temperature 400°C because of the temperature was not sufficient enough for the RDF to pyrolyse. However, at temperature above 400°C, most of the oil produced has broken to yield more gas product. The analysis of pyrolysis gas showed that CO and CO2 are dominant in the early stage of pyrolysis. Hydrocarbon, H2 starts to appear at temperature above 500°C. |
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Conference or Workshop Item |
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Raja Deris, Raja Razuan Ryu, Changkook V. N., Sharifi |
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Raja Deris, Raja Razuan Ryu, Changkook V. N., Sharifi |
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Raja Deris, Raja Razuan |
title |
Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi |
title_short |
Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi |
title_full |
Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi |
title_fullStr |
Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi |
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Pyrolysis of Refuse Derived Fuel (RDF) / Raja Razuan Raja Deris, Changkook Ryu and V. N. Sharifi |
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pyrolysis of refuse derived fuel (rdf) / raja razuan raja deris, changkook ryu and v. n. sharifi |
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2006 |
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https://ir.uitm.edu.my/id/eprint/81633/1/81633.PDF https://ir.uitm.edu.my/id/eprint/81633/ |
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