Kinetic and mass transfer aspects of biosorption of oxidisable organic matter (OOM) from wastewater are important for better understanding of the mechanisms of granules initiation and development. The modified mass transfer factor models were used to predict the liquid-solid mass transfer rates of OOM biosorption from palm oil mill effluent (POME) attached to aerobic granular sludge (AGS) in a sequencing batch reactor (SBR). The variations of [k(L)a](g), [k(L)a](f) and [k(L)a](d) pursuant to time were verified to have a zigzag pattern due to the organic loading rate varies with a change in the quality of POME feeding the SBR. The influence of added Serratia marcescens SA30 on the rates of mass transfer would be very remarkable due to the effects of metabolites and biomass growth this can lead to a rapid utilisation of OOM accumulated into AGS. The maximum efficiencies of SBR reaching 48% for CODt removal at [k(L)a](g) value of 3.054h(-1) and 68% for CODs removal at [k(L)a](g) value of 21.012h(-1) were verified before the addition of S. marcescens SA30 and those reaching 68% for CODt removal at [k(L)a](g) value of 1.229 x 10(63)h(-1) and 94% for CODs removal at [k(L)a](g) value of 7.152 x 10(64)h(-1) were verified after the addition of S. marcescens SA30. The resistance of mass transfer could be dependent on external mass transfer, which controls the movement of organic molecules along the experimental period of POME fed the SBR without and with added S. marcescens SA30. The performance of SBR would increase with increase of [k(L)a](g) value, and this provides new insight into dynamic response of the aerobic digestion to AGS development. (C) 2017 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.