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16 Bioreactors for the Production of Industrial Chemicals and Bioenergy Recovery from Waste
by the catalytic activity of the hydrogen making enzyme. Earlier report exhibited
that biohydrogen production increased 1.59 times when FeSO4 concentration was
increased from 2.7 to 10.9 mg/l. Another study considered the effect of trace ele-
ments and the results confirmed that Na, Zn, Mg, and Fe were essential increment
to control the hydrogen production.
16.4.2
Hydraulic Retention Time (HRT) and Solid Retention Time (SRT)
Traditionally, several studies have utilized CSTRs in which HRT controls the micro-
bial growth rate and operational behavior of the structure. Therefore, HRT must be
larger than the highest growth rate of the microorganisms or else biomass washout
would be a possible risk by the dilution produced via uninterrupted volumetric flow.
However, membranes in AnMBR, compared to CSTR, offer solid–liquid segrega-
tion and can maintain the biomass in the system and thus approve decoupling of
HRT as well as SRT. Earlier studies reported that hydrogen-manufacturing rate was
enhanced in AnMBR as methanogenesis was prevented or ended by decreasing HRT.
Nevertheless, the specific biohydrogen production rate stayed unchanged. Currently,
it was reviewed that efficient biohydrogen generation from liquid waste streams
(wastewater) would be performed by means of the best possible HRT ranges from
0.5 to 12 hours [24].
16.4.3
Design of Biohydrogen-Producing Reactor
Design of reactor and its development is a key parameter in biohydrogen man-
ufacturing because it can change the microenvironment of the arrangement,
hydrodynamic performance, ascertaining microbial population, and their contact
with the substrate. The majority of studies used CSTRs as they supply perfect
mass transfer and get in touch with the microorganisms and the substrate. Many
researchers reported that on the whole biohydrogen manufacturing in AnMBR
under steady-state procedure slightly surpass that of CSTR [25].
16.4.4
Substrate Concentration
Saleem et al. investigated the influence of concentration of substrate on biohydro-
gen manufacturing in side–stream anaerobic dynamic membrane bioreactor. The
results confirmed that high influent chemical oxygen demand (COD) (above 30 g/l)
related to high organic loading rate (OLR) favored the build up of VFAs connected
to the prevention of biohydrogen generation. The steady hydrogen generation was
accomplished by functioning the system at low influent concentration of COD oper-
ating in the range of 10–30 g/l and at HRT of approximately one day. An additional
study was reported that steady increase in OLR from 4 to 22 g COD/l⋅day supported
the hydrogen manufacturing after that it decreased (20%). The results disclosed that
there is no widespread favorable OLR and it may vary with the exacting inoculum,
substrate, and nature of the system [16].