A　recycling　batch　reactor　is　designed　to　measure　the　kinetics　rate,　in　which　the　catalytic　capsules　are　installed　in　the　same　way　as　in　catalytic　distillation　column　and　the　liquid　flow　condition　is　similar　to　that　in　catalytic　distillation　column.　The　apparent　kinetics　of　the　hydrolysis　of　methyl　acetate　is　studied　and　the　effectiveness　factors　are　tested　for　different　capsule　size　under　different　conditions.　The　effective　diffusivity　within　the　catalyst　capsule　is　calculated　to　be　about　9　×　10-8　m2·s-1.　The　mass　transfer　model　reported　in　part　one　of　this　paper　is　used　to　calculate　the　effectiveness　factor　of　catalyst　capsule.　It　shows　good　agreement　between　the　predicted　values　and　experimental　data　of　effectiveness　factor.　Maximum　deviation　is　13.7%　and　average　deviation　is　3.2%.