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Steam gasification of bagasse followed by thermal cracking of tar was carried out at atmospheric pressure using a dual bed reactor. The first bed was used for the steam gasification and the second bed was used for thermal cracking of tar. Iron fillings were used as the packed bed material in the second bed. The effects of reaction temperature (600 to 900 o C), packed bed height (40-100 mm) and steam/bagasse ratio on the product (char, tar and gas) yield and gas (H 2 , CO, CO 2 , CH 4 , C n H m)fatcat:qnwufskumrbszktp6ry3rkroua