초록
<P><B>Abstract</B></P><P><B>Background</B></P><P><B>Fermentative production of butanol is limited to low concentrations, typically less than 2 wt% solvent, due to product inhibition. The result is high separation energy demand by conventional distillation approaches, despite favorable vapor–liquid equilibrium and partial miscibility with water. In previous work, a process integrating steam stripping, vapor compression, and vapor permeation separation was proposed for separating ethanol from water. Such a membrane assisted vapor stripping (MAVS) process is considered in this work for 1‐butanol/water and acetone/butanol/ethanol/water (ABE/water) separation</B>.</P><P><B>Results</B></P><P><B>Using process simulations, the earlier MAVS design was estimated to require 6.2 MJ‐fuel kg<SUP>−1</SUP>‐butanol to produce 99.5 wt% 1‐butanol from a 1 wt% 1‐butanol feed, representing an energy savings of 63% relative to a benchmark distillation/decanter system. Adding a fractional condensation step to the original MAVS design is predicted to reduce energy demand to only 4.8 MJ‐fuel kg<SUP>−1</SUP>‐butanol and reduce membrane area by 65%</B>.</P><P><B>Conclusion</B></P><P><B>In the hybrid distillation/membrane MAVS systems, the stripping column provides high butanol recovery and low effluent concentration while the vapor compression and membrane steps enable the efficient recovery of latent and sensible heat from both the retentate and permeate streams from the membrane system. Addition of the dephlegmator condenser reduces both compressor size and membrane area. Published 2013. This article is a U.S. Government work and is in the public domain in the USA</B></P>