In this contribution, a rigorous process model to simulate the start-up of a cold and empty reactive distillation (RD) column is developed and experimentally validated with a transesterification process. Strategies for time optimal start-up of an RD column are presented. The mostly used strategy for conventional distillation of total reflux for RD is only recommendable with limitations. New, alternative strategies, like the recycling of the off-spec bottom and top product or the initial charging with product, to minimize the necessary start-up time are presented. Suitable strategies can save up to 82% of the needed time for the column start-up. (C) 2004 Elsevier Ltd. All rights reserved.
机构:
Washington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USAWashington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USA
Lee, JH
Dudukovic, MP
论文数: 0引用数: 0
h-index: 0
机构:
Washington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USAWashington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USA
机构:
Washington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USAWashington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USA
Lee, JH
Dudukovic, MP
论文数: 0引用数: 0
h-index: 0
机构:
Washington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USAWashington Univ, Dept Chem Engn, Chem React Engn Lab, St Louis, MO 63130 USA