Catalytic co-pyrolysis of palm oil empty fruit bunch and waste tire using calcium oxide catalysts for upgrading bio-oil
The paper discusses the influences of percentages of calcium oxide catalysts and operation temperature of catalytic co-pyrolysis on the products and characteristis of upgraded bio-oil. Catalytic co-pyrolysis was carried out in a fixed-bed reactor with an inner diameter of 30 mm and and a length of 3...
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Published in | Materials today : proceedings Vol. 87; pp. 321 - 326 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Elsevier Ltd
2023
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Subjects | |
Online Access | Get full text |
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Summary: | The paper discusses the influences of percentages of calcium oxide catalysts and operation temperature of catalytic co-pyrolysis on the products and characteristis of upgraded bio-oil. Catalytic co-pyrolysis was carried out in a fixed-bed reactor with an inner diameter of 30 mm and and a length of 300 mm. The treated EFB was mixed with the waste tire with a weight ratio of 25:75 and was added calcium oxide with catalysts with percentages of (1,2,3,4,5%). The mixed raw material and calcium oxide were put into the catalytic co-pyrolysis reactor and heated at 400 – 550 °C. The highest bio-oil yield is generated on the use of a CaO/raw material ratio of 3% w/w and temperature of 500 °C was 38.3 wt%. Bio-oil produced from catalytic co-pyrolysis of 25% palm oil empty fruit bunch (POEFB) and 75% waste tire using 3% calcium oxide catalyst has physical properties close to diesel oil. The GC–MS analysis has revealed that bio-oil contains hydrocarbon of 94.01% and oxygenated compounds of 5.99%. |
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ISSN: | 2214-7853 2214-7853 |
DOI: | 10.1016/j.matpr.2023.03.290 |