However, two major aspects need indispensable optimization, viz. a suitable renewable biomass/wastewater and ideal microbial consortia that can convert this biomass efficiently to hydrogen gas. It is a natural, though transient, by-product of several microbial driven biochemical reactions, mainly in anaerobic fermentation processes. Dark-fermentation is a ubiquitous phenomenon under anoxic or anaerobic conditions. The oxidation of the substrate by bacteria generates electrons which need to be disposed off in

order to maintain the electrical neutrality under the anaerobic or anoxic conditions other compounds, such as protons, act as the electron acceptor and are reduced to molecular Ipatasertib hydrogen.22 and 23 The bacteria which grows at 65–80 °C are called as extreme thermophiles. The G + C content of the P. stutzeri was 53 mol% which was higher than the reports of Isaac KO Cann

24 for the species Thermoanaerobacterium polysaccharolyticum and Thermoanaerobacterium zeae. This strain grew well on starch and sucrose at 70 °C. No hydrogen evolution was observed at pH 4.0–5.0 in both starch and sucrose. The hydrogen production was low at 5.5–6.5 in starch and sucrose. The low or no hydrogen production at low pH could be Bioactive Compound Library research buy partially attributing to strong decrease in hydrogenase activity 25 and this enzyme is also highly sensitive to oxygen. 23 The strain preferred high temperature for optimum hydrogen production. The hydrogen production in the medium was pH dependent and occurred within the wide range of pH 6.0–9.0. In dark-fermentation processes, this problem is compounded by the fact that the gas produced is a mixture of primarily

H2 and CO2, but may also contain other gases such as CH4, H2S, or ammonia (NH4). Moreover, the H2 content of the gas mixture almost may be low (>50%). Maximal H2 production rates were observed during exponential growth phase, which was in the order of 8–12 h, within a total growth cycle of approximately 2 days. 23 Thus no hydrogen evolution was found after 42 h of fermentation. The hydrogen production obtained is however variable and depends greatly on the bacterial consortium and culture medium. 26 Raw materials add to the cost of biohydrogen production processes. The main criteria for the selection of a substrate for H2 production are its availability, cost, carbohydrate content and biodegradability.27 Cost reduction is achieved by either using the low cost substrate or finding a means to effectively utilize the 67–85 % of the unused spent media.28 Commercially produced food products, such as corn and sugar are not economical for H2 production.29 However, solid organic wastes from agricultural crops, industrial processes and domestic waste water represent a valuable resource for the energy production. Starch based wastewater has great potentiality for the H2 production.30 Disposal of these wastes is an economic load on the society.