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1.
J Biosci Bioeng ; 121(4): 457-63, 2016 Apr.
Article in English | MEDLINE | ID: mdl-26481161

ABSTRACT

The major bottlenecks in achieving competitive bioethanol fuel are the high cost of feedstock, energy and enzymes employed in pretreatment prior to fermentation. Lignocellulosic biomass has been proposed as an alternative feedstock, but because of its complexity, economic viability is yet to be realized. Therefore, research around non-conventional feedstocks and deployment of bioconversion approaches that downsize the cost of energy and enzymes is justified. In this study, a non-conventional feedstock, inedible wild cassava was used for bioethanol production. Bioconversion of raw starch from the wild cassava to bioethanol at low temperature was investigated using both a co-culture of Aspergillus sp. and Saccharomyces cerevisiae, and a monoculture of the later with enzyme preparation from the former. A newly isolated strain of Aspergillus sp. MZA-3 produced raw starch-degrading enzyme which displayed highest activity of 3.3 U/mL towards raw starch from wild cassava at 50°C, pH 5.5. A co-culture of MZA-3 and S. cerevisiae; and a monoculture of S. cerevisiae and MZA-3 enzyme (both supplemented with glucoamylase) resulted into bioethanol yield (percentage of the theoretical yield) of 91 and 95 at efficiency (percentage) of 84 and 96, respectively. Direct bioconversion of raw starch to bioethanol was achieved at 30°C through the co-culture approach. This could be attractive since it may significantly downsize energy expenses.


Subject(s)
Aspergillus/enzymology , Biofuels/supply & distribution , Ethanol/metabolism , Flour , Manihot/chemistry , Starch/metabolism , Aspergillus/classification , Aspergillus/growth & development , Aspergillus/metabolism , Biofuels/economics , Coculture Techniques , Ethanol/economics , Fermentation , Flour/economics , Glucan 1,4-alpha-Glucosidase/metabolism , Hydrogen-Ion Concentration , Manihot/economics , Saccharomyces cerevisiae/growth & development , Saccharomyces cerevisiae/metabolism , Starch/economics , Temperature
2.
FEMS Microbiol Lett ; 362(5)2015 Mar.
Article in English | MEDLINE | ID: mdl-25743072

ABSTRACT

The current study assessed the occurrence of the Vibrio cholerae serogroups O1 and O139 in environmental samples along salinity gradients in three selected estuaries of Tanzania both through culture independent methods and by cultured bacteria. Occurrence of V. cholerae was determined by PCR targeting the V. cholerae outer membrane protein gene ompW. Furthermore, the presence of toxigenic strains and serogroups O1 and O139 was determined using multiplex PCR with specific primers targeting the cholera toxin gene subunit A, ctxA, and serotype specific primers, O1-rfb and O139-rfb, respectively. Results showed that V. cholerae occurred in approximately 10% (n = 185) of both the environmental samples and isolated bacteria. Eight of the bacteria isolates (n = 43) were confirmed as serogroup O1 while one belonged to serogroup O139, the first reported identification of this epidemic strain in East African coastal waters. All samples identified as serogroup O1 or O139 and a number of non-O1/O139 strains were ctxA positive. This study provides in situ evidence of the presence of pathogenic V. cholerae O1 and O139 and a number of V. cholerae non-O1/O139 that carry the cholera toxin gene in estuaries along the coast of Tanzania.


Subject(s)
Bacterial Outer Membrane Proteins/genetics , Estuaries , Vibrio cholerae O139/genetics , Vibrio cholerae O139/isolation & purification , Vibrio cholerae O1/genetics , Vibrio cholerae O1/isolation & purification , Water Microbiology , Cholera Toxin/genetics , DNA Primers , Genes, Bacterial , Polymerase Chain Reaction/methods , Polymorphism, Restriction Fragment Length , Tanzania , Vibrio cholerae O1/pathogenicity , Vibrio cholerae O139/pathogenicity , Virulence/genetics
3.
Bioresour Technol ; 180: 128-36, 2015 Mar.
Article in English | MEDLINE | ID: mdl-25594508

ABSTRACT

The thermoanaerobe, Caloramator boliviensis was used to ferment starch hydrolysate from inedible wild cassava to ethanol at 60°C. A raw starch degrading α-amylase was used to hydrolyse the cassava starch. During fermentation, the organism released CO2 and H2 gases, and Gas Endeavour System was successfully used for monitoring and recording formation of these gaseous products. The bioethanol produced in stoichiometric amounts to CO2 was registered online in Gas Endeavour software and correlated strongly (R(2)=0.99) with values measured by HPLC. The organism was sensitive to cyanide that exists in cassava flour. However, after acclimatisation, it was able to grow and ferment cassava starch hydrolysate containing up to 0.2ppm cyanide. The reactor hydrogen partial pressure had influence on the bioethanol production. In fed-batch fermentation by maintaining the hydrogen partial pressure around 590Pa, the organism was able to ferment up to 76g/L glucose and produced 33g/L ethanol.


Subject(s)
Clostridiales/metabolism , Ethanol/metabolism , Manihot/metabolism , Starch/metabolism , Batch Cell Culture Techniques , Biofuels , Biotechnology/methods , Carbohydrate Metabolism , Chromatography, High Pressure Liquid , Clostridiales/physiology , Cyanides/metabolism , Fermentation , Flour , Glucose/metabolism , Hydrolysis , Temperature , alpha-Amylases/metabolism
4.
Bioresour Technol ; 172: 58-67, 2014 Nov.
Article in English | MEDLINE | ID: mdl-25237774

ABSTRACT

The objective of this study was to characterise and evaluate a wild inedible cassava species, Manihot glaziovii as feedstock for bioenergy production. Tubers obtained from 3 different areas in Tanzania were characterised and evaluated for bioethanol and biogas production. These bioenergy carriers were produced both separately and sequentially and their energy values evaluated based on these two approaches. Composition analysis demonstrated that M. glaziovii is a suitable feedstock for both bioethanol and biogas production. Starch content ranged from 77% to 81%, structural carbohydrates 3-16%, total crude protein ranged from 2% to 8%. Yeast fermentation achieved ethanol concentration of up to 85g/L at a fermentation efficiency of 89%. The fuel energy of the bioethanol and methane from flour-peels mix ranged from 5 to 13 and 11 to 14MJ/kgVS, respectively. Co-production of bioethanol and biogas in which the peels were added to the fermentation residue prior to anaerobic digestion produced maximum fuel energy yield of (15-23MJ/kgVS).


Subject(s)
Biofuels , Biotechnology/methods , Ethanol/metabolism , Gases/metabolism , Manihot/metabolism , Anaerobiosis , Batch Cell Culture Techniques , Cellulose/analysis , Fermentation , Flour/analysis , Lignin/analysis , Methane/analysis , Phenotype , Plant Tubers/metabolism , Polysaccharides/analysis , Tanzania
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