18.5 Strategies to Enhance Microbial Hydrogen Production
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18.5.1
Integrative Process
The earlier sections have highlighted various processes involved in biohydrogen
production, which varies with the type of microbes involved. Microbial H2 pro-
duction has several challenges over chemical processes, and yield or production
rate is one such major hurdle of the process. An integrative approach to generate
a single-stage hybrid system or two-stage system for H2 production has recently
gained much attention intending to overcome the limitations of single operated
processes shown in Figure 18.1b,c. The dark fermentation process is characterized
by a massive accumulation of organic acids, which leads to an inhibitory effect
on H2-producing enzymes and the growth of microbes. These acid-rich effluents
are high in carbon content and can act as a substrate for further energy recovery
through a two-stage process. The dark fermentation effluents generated in the
first stage is processed by the second stage and can be used for methanogenesis
for methane production or H2 production through photo-fermentation, microbial
electrolysis cells (MECs) for H2, MFCs for bioelectricity, bioplastic production,
and heterotrophic algae cultivation for lipids [40–44]. These integrated processes
are involved in the efficient valorization of waste effluents for additional energy
production or other value-added products. This makes the integrative approach
more economically feasible and practically applicable to industrial scales.
18.5.2
Medium and Process Optimization
Fermentative hydrogen production is influenced by several factors that have been
discussed in detail in Sections 18.4 of this chapter. The composition of the fermen-
tation medium is very crucial for the activity of enzymes catalyzing H2 production,
like pyruvate ferredoxin oxidoreductase, hydrogenase, formate hydrogen lyase, and
pyruvate formate lyase. The fermentation medium is a source of nutrients essential
for the growth and metabolism of the microorganisms, which includes sources
of carbon, nitrogen, metal ions, and other trace elements. However, an optimum
range of these nutrients is necessary for efficient strain cultivation and production
of metabolites because a higher or lower range may lower the fermentation kinetics,
thereby reducing the product yield. Similarly, an optimum range of operating
conditions is also necessary to be maintained throughout the fermentation process,
which includes temperature, pH of the medium, substrate concentration, and
inoculum. Optimization of both the process parameters and medium components
is, therefore, also essential for biological H2 production. Several studies have
investigated the effect of these factors on the yield of H2 production and estimated
the optimum range of factors required for maximum production [16]. The co-factors
and the enzymes of all microbes are mostly active in an optimum pH and tem-
perature range; therefore, parameter optimization is the key technique to obtain
maximum yields. Different experimental design methods like central composite
design (CCD), Box–Behnken (BB) design, full factorial design, Plackett–Burman
design, Taguchi design, and one-variable-at-a time (OVAT) design can be used
to evaluate the optimum range and the effects of various parameters. Response