Pervaporation of ethanol from lignocellulosic fermentation broth.

Pervaporation can be applied in ethanol production from lignocellulosic biomass. Hydrophobic pervaporation, using a commercial PDMS membrane, was employed to concentrate the ethanol produced by fermentation of lignocellulosic hydrolysate. To our knowledge, this is the first report describing this.

Preparation and evaluation of lignocellulosic biomass hydrolysates for growth by ethanologenic yeasts.

Lignocellulosic biomass is a potential feedstock for bioethanol production. Biomass hydrolysates, prepared with a procedure including pretreatment and hydrolysis, are considered to be used as fermentation media for microorganisms, such as yeast. During the hydrolysate preparation procedure, toxic compounds are released or formed which may inhibit the growth of the microorganism and thus the product formation.

Microbial renewable feedstock utilization: a substrate-oriented approach.

Increasingly lignocellulosic biomass hydrolysates are used as the feedstock for industrial fermentations. These biomass hydrolysates consist of complex mixtures of different fermentable sugars, but also contain inhibitors and salts that affect the performance of the product-generating microbes. The performance of six industrially relevant microorganisms, i.

Microbial production host selection for converting second-generation feedstocks into bioproducts.

Background: Increasingly lignocellulosic biomass hydrolysates are used as the feedstock for industrial fermentations. These biomass hydrolysates are complex mixtures of different fermentable sugars, but also inhibitors and salts that affect the performance of the microbial production host. The performance of six industrially relevant microorganisms, i.

Performance and population analysis of a non-sterile trickle bed reactor inoculated with Caldicellulosiruptor saccharolyticus, a thermophilic hydrogen producer.

Non-axenic operation of a 400 L trickle bed reactor inoculated with the thermophile Caldicellulosiruptor saccharolyticus, yielded 2.8 mol H2/mol hexose converted. The reactor was fed with a complex medium with sucrose as the main substrate, continuously flushed with nitrogen gas, and operated at 73 degrees C.