SCI和EI收录∣中国化工学会会刊

›› 2011, Vol. 19 ›› Issue (3): 371-379.

• SEPARATION SCIENCE AND ENGINEERING • Previous Articles     Next Articles

Conceptual Design of a Butyl-levulinate Reactive Distillation Process by Incremental Refinement

Andreas Harwardt, Korbinian Kraemer, Bettina Rüngeler, Wolfgang Marquardt   

  1. Aachener Verfahrenstechnik-Process Systems Engineering, RWTH Aachen University, Germany
  • Received:2010-08-09 Revised:2011-04-09 Online:2011-06-28 Published:2011-06-28
  • Supported by:
    Work originally presented on the 2nd Int. Symp. Sustainable Chemical Product and Process Engineering, held at Hangzhou, China from May 9 to 12, 2010

Conceptual Design of a Butyl-levulinate Reactive Distillation Process by Incremental Refinement

Andreas Harwardt, Korbinian Kraemer, Bettina Rüngeler, Wolfgang Marquardt   

  1. Aachener Verfahrenstechnik-Process Systems Engineering, RWTH Aachen University, Germany
  • 通讯作者: Andreas Harwardt, E-mail: Andreas.Harwardt@avt.rwth-aachen.de
  • 基金资助:
    Work originally presented on the 2nd Int. Symp. Sustainable Chemical Product and Process Engineering, held at Hangzhou, China from May 9 to 12, 2010

Abstract: Butyl-levulinate has been identified as a promising fuel candidate with high oxygen content. Its combustion in diesel engines yields very low soot and NOx emissions. It can be produced by the esterification of butanol and levulinic acid, which themselves are platform chemicals in a biorenewables-based chemical supply chain. Since the equilibrium of esterification limits the conversion in a conventional reactor, reactive distillation can be applied to overcome this limitation. The presence of the high-boiling catalyst sulfuric acid requires a further separation step downstream of the reactive distillation column to recover the catalyst for recycle. Optimal design specifications and an optimal operating point are determined using rigorous flowsheet optimization. The challenging optimization problem is solved by a favorable initialization strategy and continuous reformulation. The design identified has the potential to produce a renewable transportation fuel at reasonable cost.

Key words: biofuels, conceptual design, reactive distillation, butyl-levulinate, mixed-integer nonlinear problems, continuous reformulation, process optimization, process intensification

摘要: Butyl-levulinate has been identified as a promising fuel candidate with high oxygen content. Its combustion in diesel engines yields very low soot and NOx emissions. It can be produced by the esterification of butanol and levulinic acid, which themselves are platform chemicals in a biorenewables-based chemical supply chain. Since the equilibrium of esterification limits the conversion in a conventional reactor, reactive distillation can be applied to overcome this limitation. The presence of the high-boiling catalyst sulfuric acid requires a further separation step downstream of the reactive distillation column to recover the catalyst for recycle. Optimal design specifications and an optimal operating point are determined using rigorous flowsheet optimization. The challenging optimization problem is solved by a favorable initialization strategy and continuous reformulation. The design identified has the potential to produce a renewable transportation fuel at reasonable cost.

关键词: biofuels, conceptual design, reactive distillation, butyl-levulinate, mixed-integer nonlinear problems, continuous reformulation, process optimization, process intensification