2007
DOI: 10.1016/j.jbiotec.2007.05.011
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Strategies for the development of a side stream process for polyhydroxyalkanoate (PHA) production from sugar cane molasses

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Cited by 336 publications
(198 citation statements)
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“…The experimental setup consisted of three benchscale reactors and a hollow fiber membrane filtration module (Albuquerque et al, 2007). The molasses acidogenic fermentation (stage 1) was carried out in a continuous stirred tank reactor operated under anaerobic conditions.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The experimental setup consisted of three benchscale reactors and a hollow fiber membrane filtration module (Albuquerque et al, 2007). The molasses acidogenic fermentation (stage 1) was carried out in a continuous stirred tank reactor operated under anaerobic conditions.…”
Section: Methodsmentioning
confidence: 99%
“…The molasses acidogenic fermentation (stage 1) was carried out in a continuous stirred tank reactor operated under anaerobic conditions. The conditions used to operate the acidogenic continuous stirred tank reactor are described in detail in Albuquerque et al (2007). The fermented molasses was clarified by microfiltration and used as a feedstock for subsequent culture selection and PHA accumulation.…”
Section: Methodsmentioning
confidence: 99%
“…In comparison to fermented effluent, polymer with single synthetic acid has higher M w up to 3.0 9 10 6 Da, which may be due to higher rates of polymerization [66]. M w of the copolymers was observed to be 4.5-9 9 10 5 Da with acetate and propionate, 8.5 9 10 5 Da, for P(3HB:3HV) with molasses and 3.5-4.3 9 10 5 Da for copolymer with fermented molasses [7,67]. The disruption of polymer chain by 3HV units causes the average M w to decrease with increasing monomer units, e.g.…”
Section: Substrate and Feeding Regimementioning
confidence: 99%
“…P(3HB:3HV) synthesized by mixed bacterial culture had higher 3HV up to 48 mol% at pH 9.5 in comparison to pH 8.5 and P(3HB:3HV:4HB) synthesized by Delftia acidovorans had increased 3HV (29-46 mol%) and 4HB (39-50 mol%) at pH 8.5 in comparison to pH 5.0 [71,72]. The pH can also have an indirect effect on PHA composition as the VFA profile produced under acidogenic fermentation can be manipulated by varying it [67]. In addition to this, nutrient level in media as compared to C affects the quality of PHA.…”
Section: Culture Conditionsmentioning
confidence: 99%
“…Mixed culture PHA production relies on a selection pressure that favors organisms with PHA storage capacity. In this case no reactor sterilization is necessary and the culture can adapt to various complex waste feed stocks (Albuquerque et al 2007;Bengtsson et al 2008;Serafim et al 2008), leading to potential environmental and economical advantages compared to both pure culture PHA production. Fermentations employing two or more microorganisms offer benefits over single culture fermentations either by commensalism or by neutralism or by conversion of substrate to a metabolite by first microorganism which is utilized by the second microorganism to produce the product (Kondo et al 1996;Shimizu et al 1999).…”
Section: Introductionmentioning
confidence: 99%