NewBioWorld A Journal of Alumni Association of Biotechnology (2019) 1(2):28-32
RESEARCH ARTICLE
Optimization of pH and
temperature for efficient bio-hydrogen production from lignocellulosic waste
Mona Tandon, Shailesh Kumar
Jadhav* and Kishan Lal Tiwari
S.o.S. in Biotechnology, Pt.
Ravishankar Shukla University, Raipur (C.G.) 492 010, India.
*Email- jadhav9862@gmail.com
ARTICLE
INFORMATION
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ABSTRACT
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Article history:
Received
16 December 2018
Received in revised form
12 February 2019
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Biomass is
the chief source of bio-hydrogen production which includes agricultural crops
as well as their residues, various effluents generated in human habitat,
aquatic plants and algae, and by-products released during food processing.
Bio-hydrogen is selectively produced from biomass because of its
cost-effectiveness, easy availability, high carbohydrate content and their
ease of biodegradability. This research paper includes optimization of pH and
temperature on bio-hydrogen producing capacity and their effect on bacterial
growth.
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Keywords:
Bio-hydrogen
Lignocellulosic biomass Dark fermentation
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Introduction
Hydrogen
having high energy yield of 142 KJ/g is a crucial alternative
source of energy carrier replacing fossil fuels. As it is pollution free, thus
known as a clean energy source which is eco-friendly (Nath and Das, 2004;
Rittmann and Herwig, 2012). Hydrogen is liberated during different processes
like electrolysis of water, through natural gases, steam reforming of hydrocarbons
and during biological processes.Hydrogen producing enzymes are
present in a microbe which produces the bio-hydrogen. Bio-hydrogen productionfrom a variety of renewable
resources utilized as a substrate by different approaches including direct bio-photolysis,
indirect bio-photolysis, photo-fermentation and dark-fermentation (Chen et al.
2008; Homann 2003; Lo et al. 2010; Manish and Banerjee 2008; Redwood et al. 2012).
Among these, dark-fermentation is a carbon neutral process for the production of
bio-hydrogen in which carbohydrate rich substrates are a breakdown by
facultative and obligate anaerobic bacteria. Many efforts have been directed to
the development of efficient technologies to obtain renewable energy from
lignocellulosic biomass, by recycling a large range of agricultural wastes
which are non-food parts of crops: such as stems, leaves, flowers, etc. and the
industrial waste products such as woodchips, skin and pulp from fruit pressing,
wastes from oil refineries from seeds etc. These agricultural wastes are used
for energy production. Anaerobic fermentation from bacteria by methanogenesis,
that has already found wide application for the reduction and stabilization of
agricultural wastes. Many microorganisms utilizes agricultural wastes as an
organic source of carbohydrate and convert into hydrogen Bacteria which produce
hydrogen include species of Enterobacter,
Bacillus and Clostridium via pyruvate metabolism which is an
intermediate, formed during the degradation of substrates (Martinez-Porqueras et al. 2013). Hydrogen evolution rate is higher
in the dark-fermentation process in contrast to other processes.Theoretically, four moles of
hydrogen can be produced per mole of glucose, assuming that all pyruvate is
converted to acetate but in reality, it is not possible. The pH is an important
key factor in bio-hydrogen production as it affects hydrogenase activity,
metabolic pathways shifts the volatile acid production and microbial
communities in bio-hydrogen production (Shridevi and Preetha 2015). Microbial
growth during fermentation process was inhibited at lower pH leads to lower
hydrogen production (Liu et al. 2011). This is because; the lower pH can change
the fermentation process for bio-hydrogen production to butyric acid type, propionic
acid type and ethanol type of fermentation. Generally, acidogens are less
sensitive to pH change than the acetogens and methanogens. The pH drop from 6
to 4.5 was considered to be the ideal pH range for the anaerobic bacteria and
for inhibition of methanogenic activity (Mohan et al. 2007). Bacterial families belonging to
mesophilic bacteria includes Entero bacteriaceae
and Clostridiaceae as well as the
family Thermoanaerobacterales, which
have attracted much attention in recent years, as it exhibits low hydrogen to
glucose yields of 1-2 mol/mol because of the thermodynamic limitation
associated with NADH utilized as an electron carrier (Chou et al. 2008; Lee et al. 2011; Rittmann
and Herwig 2012). Thermophilic H2 production has been shown to be
clearly advantageous over mesophilic H2 production with respect to
the yields of hydrogen to the substrate. Hydrogen yield has been shown to be
high 1.46 mol/molformesophilic bio-hydrogen producing microorganisms as
compared with thermophilic bacteria, 2.20 mol/mol (Verhaart et al. 2010). Ease of
accessibility, cost-effectiveness, high carbohydrate content and
biodegradability are taken into consideration while choosing any substrate for
bio-hydrogen production (Das and Veziroglu 2008). India is at second position
in world whereas, Chhattisgarh ranks fifth in India for maximum rice
production. This indicates generation of large amount of agricultural wastes.
So, rice bran
which is the by-product of rice can be suitable substrate for production of
bio-hydrogen. Rice bran constitutes cellulose which is attached to sugars and
hemicellulose which is attached to lignin. Rice bran is the by-product
generated in rice bran oil industry. Various bacterial strains are capable of
degrading complex carbohydrates but bio-hydrogen generation mainly depends on
type and concentration of substrate, its pH, and hydraulic retention time, the substrate to inoculums ratio,
metal ion concentration, etc. So
considering all these parameters, the objectives fixed for the current piece of
research are isolation and identification of maximum bio-hydrogen producing
bacteria from rice industry waste and at the same time optimization of
temperature and pH on bacterial growth.
Materials and methods
RB (Rice bran) and DORB (De-oiled Rice bran)
samples were collected from Paras gold oil refinery industry, Urla,
Chhattisgarh, India. Collected samples were kept in airtight container at room
temperature.
Isolation of bacteria and characterization
Bacteria were isolated from the RB
and DORB samples. 1g of the RB
and DORB samples was added to 10 ml of distilled water. Serial dilution
(10-1 to 10-9) was performed on a nutrient
agar plate (peptone 5g/l; beef
extract 3g/l; NaCl 5g/l; agar 15g/l; pH 6.8) by spread
plate method and incubated for 24hrs at 37±2°C (Thakur et
al.2012). Isolated colonies were purified using streak plate method and
maintained in nutrient agar slants as stock. Fermentation medium (peptone
10g/l; glucose 5g/l; NaCl 15g/l; phenol red 0.018g/l and pH -7.3) was prepared
and then transferred into a test tube having Durham's tube for detection of gas
production. Inoculation of culture in fermentative media and incubated at 37±2°C
for 48hr. Phenol red was used as an indicator which turns the medium from
pinkish red to yellow. The screened isolates were maintained on nutrient agar
slants at 37±2°C and stored at 4°C. Colony characterization of the isolated
bacteria from different season by their number, shape, elevation, margin, and
appearance was performed (Prescott and Harley 2002). Staining tests for the
screening of bacteria by gram staining, acid-fast staining, endospore staining,
and motility test were performed. Amylase test, urease, IMViC test (indole
test, methyl red test, Voges-Proskauer test, citric acid utilization test) and
catalase tests were performed for their biochemical characterization (Prescott
and Harley 2002).
Effect of pH
and temperature on bacterial cell growth
Temperature is a very important parameter in bio hydrogen production and
also influences cell growth. The pH is an important key factor in bio-hydrogen
production as it affects hydrogenase activity, metabolic pathways shifts the
volatile acid production and microbial communities in bio-hydrogen production.
Thus, the effect of pH on bacterial growth and bio-hydrogen production capacity
ranges from 4.5, 5, 5.5, 6, 6.5, and 7. The effect of temperature on bacterial
growth was investigated at different temperatures ranging from 25°C, 30°C,
35°C, 40°C and 45°C and for bio-hydrogen producing capacity from 30°C, 35°C,
40°C, 45°C and 50°C.
Batch fermentation hydrogen production
Batch
fermentation studies were carried out in 250ml Erlenmeyer flasks by the process
of liquid displacement method of all isolated culture (Fig.1). In this method,
two 250 ml conical flask was capped by rubber cork connected with plastic pipe
and an outlet in one flask which was in the measuring cylinder to measure the
production of bio-hydrogen in a millilitre. The first flask contained substrate
along with bacterial culture and second flask contained 10 % KOH, for the
absorption of carbon dioxide(CO2), which was again connected to a
measuring cylinder for collection of KOH (Kotay and Das 2006). Bio-hydrogen and
CO2released from headspace of fermentor from first flask containing
1:10 (w/v) of substrate to inoculums ratio through 10 % KOH where CO2
absorbed and collected in the measuring cylinder to measure the production of
bio-hydrogen in millilitre (Zanchetta et al. 2007).
The initial pH
value for hydrogen production was maintained at 6 compared to neutral pH under
mesophilic condition (37±2°C) (Mohan et al. 2008).
Hot
plate magnetic stirrer
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Figure 1: Experimental setup (Batch fermentation process)
for bio-hydrogen production.
This setup was placed on hot magnetic stirrer maintained at 37±2°C. Data
obtained from secondary screening for bio-hydrogen production and specific
hydrogen production rate (SHPR) was compared and analysed using Excel Software.
Results and
Discussion
Isolation of
bacteria
Bacteria were isolated from the RB
and DORB samples. 1g of the RB
and DORB samples was added to 10 ml of distilled water. Serial dilutions
(10-1 to 10-9)was performed on nutrient agar
plate by spread plate method and incubated for 24hrs at 37±2°C(Thakur et
al.2012).After incubation for 24 hrs, mixed culture of the bacteria was found
on the plates of dilution at 10-3, 10-4 and 10-5.
Pure culture was performed by streak plate method and pure cultures were
obtained by plating repeatedly. From these only six bacterial isolates were
selected which showed best results for bio-hydrogen production and goes for a
further test. Out of these cultures, RB II showed maximum bio-hydrogen
producing capacity of 510±3.9 ml H2/L with SHPR
0.70±0.33ml H2/g substrate/h.
Microscopic
and biochemical analysis
Bacterial
species were isolated from the RB sample and from DORB sample and their
microscopic study was performed (table 1).
Table 1: Microscopic and
Biochemical test performed in bacteria isolated from RB and DORB
Tests
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RB I
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RB II
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RB III A
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RB III
B
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DORB I
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DORB
II
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Gas producing
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+
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+
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+
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+
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+
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+
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Acid producing
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+
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+
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+
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+
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+
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+
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Gram staining
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─
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─
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─
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─
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─
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─
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Acid-fast staining
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─
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─
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─
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─
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─
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─
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Endospore staining
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─
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─
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─
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─
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─
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─
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Motility test
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+
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+
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+
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+
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─
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+
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Indole
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─
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─
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─
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─
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─
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─
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MR
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+
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─
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─
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─
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-
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─
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VP
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─
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+
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+
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─
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─
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─
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Citrate test
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+
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+
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+
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+
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+
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+
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Catalase test
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+
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+
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+
|
+
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+
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+
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Urease test
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─
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+
|
+
|
+
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+
|
+
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Amylase test
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+
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─
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─
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─
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─
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+
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All bacterial cultures are gram-negative, acid-fast negative, endospores
negative. Zhang et al. (2007) identified the spore-forming rod-shaped during
their studies on enhanced bio-hydrogen production from corn stalk wastes with
pre-treatment by acidification by mixed anaerobic cultures. Basically, the
bacteria can degrade organic and inorganic compounds by converting them into
various intermediate compounds by the action of various enzymes. They derive
their nutritional requirements from the compounds present in the ent waste. All
isolates of RB sample were indole negative, citrate positive, catalase
positive. All but one isolate showed MR negative and two showed VP positive
results.
Effect of pH
and temperature on bacterial growth
Environmental
conditions are the major parameters to be controlled in bacterial growth for
bio-hydrogen production. In this study, the effect of pH ranges from 5 to 8 and
temperature ranges from 25°C to 40°C on bacterial
growth was observed. At pH 6.0, bacterial growths were observed maximum while
at pH 8, bacterial growths were observed minimum (fig. 2). Bacterial strains
had the capacity to degrade complex carbohydrates. Studies concluded that pH
play an important role in hydrogen production, and the optimum pH for enhanced
yield of hydrogen recorded was in the wide range of pH (5.0-9.0) for various
kinds of hydrogen producing microbes by Mu et al. (2014).This may be
due to the suppression of methanogenic activity under acidic conditions. At higher
or lower than this pH accumulation of acids causes a sharp drop of culture pH and
subsequent inhibition of bacterial hydrogen production (Haridoss 2016). Pachapur et al. (2016) noted that impact of H2
production with increasing pH up to optimum (7.0)
had a comparative impact of increase in pH through crude glycerol. Ren et al.
(2007) observed maximum hydrogen yield of 1.77mmol/mmol of glucose was achieved
at pH 6.0in batch fermentation processes showed a similar result. While on the
study of the effect of temperature on bacterial growth, 35°C temperature
was the best for all selected bacteria whereas at 40°C bacterial
growth was found minimum (fig. 3). Chittibabu et al. (2006) observed efficiency of bacterial growth decreased when
temperature was increased from 38°C to 45°C because of denaturation of the key
enzymes or inactivation in the metabolic pathway at high temperature. Maximum
bacterial growth was observed at pH 6.0 and suitable temperature 35°C.
Figure 2: Bacterial growth of BHP bacteria isolated from
RB and DORB at different pH (5-8 pH).
Figure 3: Bacterial growth of BHP bacteria isolated
from RB and DORB at different temperature (25-40°C).
Bio-hydrogen
producing capacity at different pH and temperature
Hydrogen production is a growth associated product where mostly gas was
produced during the exponential phase carried out in 250ml batch fermentation
process by liquid displacement method.Temperature is one of the most
important physical factors affecting microorganism and at optimum temperature
enhances bio-hydrogen production. The maximum bio-hydrogen production was found
at pH 6.0 1351.6±15.89 ml H2/L with maximum SHPR 0.187±0.002 ml H2/g
substrate/h (Fig. 4). Bio-hydrogen producing capacity was maximum at 35°Cand
30°C having 1291.6ml H2/L with maximum SHPR 0.179±0.0001ml H2/g
substrate/h and 1358.3±8.3ml
H2/L with maximum SHPR 0.188±0.05 ml H2/g substrate/h respectively
(Fig. 5). At 35°C, showed maximum production due to the accumulation of VFA’s
over time, it causes the death of the bacteria hence decline in hydrogen
production was observed with more time interval. Shukla et al. (2015)
also reported bio-hydrogen production fromrice bran and rice mill effluent by using Clostridium
acetobutylicum NCIM 2877 at 35°C and pH 6.0 and found production was
68.7±0.9 ml with 85±1.0% substrate utilization. Chaoudhary et al. (2015) also
observed maximum bio-hydrogen production of 112 ml at 48 hours of hydraulic
retention time, 92 ml production at 35°C and 180 ml at initial pH 8 from isolated.
Cell growth
and hydrogen production were decreased when the temperature was increased from
38°C to 45°C and there was no hydrogen production at 45°C.
Figure 4(a): Bio-hydrogen productions in ml H2/L±SE of batch
fermentation at temperature 37°C±2°C,
Figure 4(b): SHPR in ml/g substrate/h
Figure 5(a):Bio-hydrogen productions in mlH2/l±SE of batch
fermentation at pH 6.0
Figure 5 (b): SHPR in ml/g substrate/h.
Conclusion
A hydrogen producing strain was isolated from municipal sewage sludge
and RB II showed
maximum hydrogen production of 1358.3±8.3ml H2/L with maximum SHPR
0.188±0.05 ml H2/g substrate/h. Maximum bio-hydrogen
production at ambient pH 6.0 and temperature 35°C will be isolated and utilized
for enhanced bio-hydrogen production was optimized. Further biological and
chemical pretreatments will improve bio-hydrogen yields. The dark fermentation
process can renovate unvalued organic waste into bio-hydrogen rich gas. This
approach also reduces the efficient production costs which are ultimately
beneficial from economic point of view.
Conflict of
interest
Authors had no conflict of interest.
Acknowledgement
Authors are thankful to the Department of Science and Technology, New
Delhi for financial support through DIST-FIST scheme to support to School of
Studies in Biotechnology, Pt. Ravishankar Shukla University, Raipur
(C.G.).Authors are also grateful to the RGNF, UGC
(University Grants Commission), New Delhi, circular number
F1-17.1/2015-16/RGNF-2015-17-SC-CHH-2144/(SA-III/Website) for financial
support.
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