Gasification of char derived from sewage sludge was studied by using the TG-MS system. Experiments were carried out at different temperatures and steam concentrations. The temperatures of 700-900 degrees C were necessary to complete the conversion in reasonable time. Three reaction rate models for gas-solid reaction were applied to describe the effect of char conversion on the reaction rate. In comparison to the shrinking core model for reaction-controlled regime and random pore distribution models, simple pseudo-homogeneous first-order kinetics was found to be the best for predicting the rate of char steam gasification. Kinetic parameters estimated from the experimental data are in accordance with the literature for lignocellulosic char gasification and are the first ones published for sewage sludge char gasification. (C) 2014 Elsevier Ltd. All rights reserved.