کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
760377 | 1462852 | 2016 | 12 صفحه PDF | دانلود رایگان |
• MW heating of coal was carried out with uniformly distributed carbon surfaces.
• The effects of carbon loading, MW power and N2 flow rate were investigated.
• Heating profile, pyrolysis products are influenced by the process variables.
• Highest coal-tar obtained when final temperature sustained for longer duration.
• Coal-tar is mainly composed of aromatics and saturated aliphatics hydrocarbons.
In this study, coal solids were subjected to Microwave (MW) pyrolysis conditions. Coconut Activated Carbon (CAC) solids used as a MW absorber was distributed uniformly over coal solids to reduce hotspots. Three process parameters; CAC loading, MW power and N2 flow rate were studies on pyrolysis heating performance. The highest coal-tar yield of 18.59 wt% was obtained with 600 W, 75 wt% CAC loading and 4 Liter per Minute (LPM) of N2 flow rate. This improved coal-tar yield is mainly of the fact that higher MW power and CAC loading produced sustained pyrolysis conditions for longer duration for the complete conversion of pyrolysis solids. The coal-tar was composed mainly of aromatics (naphthalenes, benzenes and xylene) and saturated aliphatics (alkanes and alkenes) hydrocarbons. The gas produced from pyrolysis of coal is mainly of H2 40.23–65.22 vol%.
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Journal: Energy Conversion and Management - Volume 110, 15 February 2016, Pages 142–153