Saccharification of paper products by cellulase from Penicillium funiculosum and Trichoderma reesei

Used paper products contribute largely towards organic-based waste produced and dumped by the world population. Cellulose, a structural component of paper materials, can be hydrolysed into glucose by a multi-component enzyme system called cellulase. Cellulase from Penicillium funiculosum and Trichoderma reesei were applied in the saccharification of paper products such as foolscap paper, filter paper, newspaper and office paper as well as microcrystalline cellulose. Foolscap paper showed the strongest susceptibility towards enzymatic hydrolysis with both enzymes. With an enzyme concentration of 10.0 mg/mL for each cellulase system the strongest synergistic action was observed at a combination of 1:1 (m/m) during saccharification of all cellulose materials. The individual enzyme performance as well as their synergistic actions showed different rates of hydrolysis during degradation of the investigated cellulose substrates.     

dl-2 Aminobutyric acid and calliterpinone are the potential stimulators of Trichoderma cellulase activities

Trichoderma citrinoviride EB-104 has recently been developed as a hyper β-glucosidase producing mutant strain. In the present study, efforts were made to further enhance its enzyme titers using low molecular weight stimulators viz., calliterpinone (a natural plant diterpenoid), dl-2-aminobutyric acid (isomer of an amino acid, aminobutyric acid) and jasmonic acid (a natural plant growth regulator). Among test stimulators, calliterpinone and dl-2-aminobutyric acid significantly enhanced activities of all three enzymes of cellulase complex i.e., FPase, endoglucanase and β-glucosidase. A 5.0 and 2.7 fold increase in FPase and endoglucanase activities, respectively, could be achieved by incorporating 12.5 mmol dl-2-aminobutyric acid into fermentation media. On the other hand, more than fivefold enhanced β-glucosidase activity was evident with 10 μmol of calliterpinone, raising its activity from 8.28 to 43.38 IU cm⁻³. This β-glucosidase activity of T. citrinoviride EB-104 is far higher than that of reported earlier. These test stimulators, which improved enzyme activities of cellulase complex in T. citrinoviride EB-104, may also be explored for enhancing the activities of other fungal enzymes.     

Optimization of cellulases production by Trichoderma citrinoviride on marc of Artemisia annua and its application for bioconversion process

The production of cellulases by Trichoderma citrinoviride fermented on marc of Artemisia annua, and bioconversion of the same marc by produced cellulase system was studied. The effects of pretreatments, substrate concentration, particle size, initial pH, temperature and concentration of the medium components on production of FPase, endoglucanase and β-glucosidase were monitored and comparatively evaluated. Among the three pretreatment processes, alkali hydrolysis with autoclaving was found to be most suitable for production of all the three enzymes. Optimum production of FPase, endoglucanase and β-glucosidase was obtained at 96 h, 96 h and 72 h of fermentation period, respectively. Substrate concentration of 1% with particle size between 200 μm and 475 μm gave the higher yields. Higher production of all the three enzymes was obtained with initial pH value of 5.5, temperature of 28 °C and 75% of mineral salt solution. Partially purified enzyme system obtained by optimized fermentation procedure, was applied for saccharification. Forty six percent of saccharification was noticed after 48 h of incubation on alkali hydrolyzed and autoclaved substrate which was 3.26 fold more than that of unpretreated substrate.     

Enzymatic saccharification of pretreated rice straw by cellulase produced from Bacillus carboniphilus CAS 3 utilizing lignocellulosic wastes through statistical optimization

A marine bacterium, Bacillus carboniphilus CAS 3 was subjected to optimization for cellulase production utilizing cellulosic waste through response surface methodology. Plackett – Burman and Central composite design was employed and the optimal medium constituents for maximum cellulase production (4040.45 U/mL) were determined as rice bran, yeast extract, MgSO₄·7H₂O and KH₂PO₄ at 6.27, 2.52, 0.57 and 0.39 g/L, respectively. The cellulase produced was purified to the specific activity of 434.94 U/mg and 11.46% of recovery with the molecular weight of 56 kDa. The optimum temperature, pH and NaCl for enzyme activity was determined as 50 °C, 9 and 30% and more than 70% of its original activity was retained even at 80 °C, 12 and 35% respectively. Further, enzymatic saccharification of pretreated rice straw yielded about 15.56 g/L of reducing sugar at 96 h, suggesting that the purified cellulase could be useful for production of reducing sugars from cellulosic biomass into ethanol.     

Production and optimization of high grade cellulase from waste date seeds by Cellulomonas uda NCIM 2353 for biohydrogen production

Production of high grade cellulolytic enzymes from waste agricultural biomass would valorise these wastes to valuable products as well as avoid the pollution problems associated with landfilling of the biomass. In the present study, waste date palm (Phoenix dactylifera) seeds were valorised for cellulase production from Cellulomonas uda NCIM 2353 and for its subsequent usage in biohydrogen production. Optimization of key operational parameters such as date seed concentration, xylose, casein and initial media pH were performed using central composite design to obtain the maximum enzyme yield. The optimum values obtained were (g/L): date seed concentration 30.65, xylose concentration 0.55, casein 7.00 and pH 7.40 for a determination coefficient of 0.999. The results demonstrated a higher prediction accuracy of response surface methodology as the cellulase activity increased six fold (175.96 IU/mL) after optimization. The optimum pH and temperature of purified cellulase was 7 and 50 °C respectively where the enzyme retained nearly 80% of activity upto 180 min. Enzymatic hydrolysis studies showed that a high saccharification efficiency of 60.5% was obtained for acid pretreated sugarcane bagasse by the indigenous cellulase, equivalent to the performance of commercial cellulase. Further, the as-obtained reducing sugars were decomposed by Clostridium thermocellum to produce biohydrogen of maximum concentration 187.44 mmol/L at end of 24 h of fermentation. Results show that date seed substrate based cellulase protein can be employed for industrial processes of biohydrogen production.     

Optimization of concomitant production of cellulase and xylanase from Rhizopus oryzae SN5 through EVOP-factorial design technique and application in Sorghum Stover based bioethanol production

Current study deals with the production of cellulases and xylanases from the Rhizopus oryzae SN5 isolated from composed soil of Himalayan pine forest, in order to meet the challenges of lignocellulosic biomass based biorefineries. Culture parameters for concomitant production of cellulase and xylanase were optimized through EVOP-factorial design technique under solid state fermentation. And maximum yield of cellulase and xylanase were obtained 437.54 U/gds and 273.83 U/gds, respectively at 30 °C and pH 6.0 after 5 days of incubation. On applying these enzymes for the saccharification of the dilute acid pretreated Sorghum Stover (SS), 0.407 g/g sugar was yielded. This hydrolysate on fermentation, yielded 0.411 g/g ehanol with Saccharomyces cerevisiae (NCIM 3288), which could be considered a good conversion. Therefore, Rhizopus oryzae SN5 was found as potent strain for the production of the cocktail of lignocellulosic biomasss hydrolytic enzymes and would be promising tool in the area of lignocellulose based bio-refineries.     

A novel staggered hybrid SSF approach for efficient conversion of cellulose/hemicellulosic fractions of corncob into ethanol

The following study reports bioconversion of corncob into ethanol using hybrid approach for co-utilization of dilute acid hydrolysate (pentose rich stream) and hexose rich stream obtained by enzymatic saccharification employing commercial cellulase Cellic CTec2 as well as in-house cellulase preparations derived from Malbranchea cinnamomea, Scytalidium thermophilium and a recombinant Aspergillus strain. Acid hydrolysis (1% H₂SO₄) of corncob at 1:15 solid liquid ratio led to removal of 80.5% of hemicellulosic fraction. The solid glucan rich fraction (63.5% glucan, 8.3% pentosans and 27.9% lignin) was hydrolysed at 10% substrate loading rate with different enzymes for 72 h at 50 °C resulting in release of 732 and 535 (mg/g substrate) total sugars by Cellic CTec2 and M. cinnamomea derived enzymes, respectively. The fermentation of enzyme hydrolysate with co-culture of Saccharomyces cerevisiae and Pichia stipitis added in sequential manner resulted in 3.42 and 2.50% (v/v) ethanol in hydrolysate obtained from commercial Cellic CTec2 and M. cinnamomea, respectively. Employing a hybrid approach, where dilute acid hydrolysate stream was added to solid residue along with enzyme Cellic CTec2 during staggered simultaneous saccharification and fermentation at substrate loading rate of 15% resulted in 252 g ethanol/kg corncob.     

Improvement of wheat straw hydrolysis by cellulolytic blends of two Penicillium spp.

Co-culture of fungal strains Penicillium janthinellum EMS-UV-8 (E), Penicillium funiculosum strain P (P) and Aspergillus sp. strain G (G) and blending of their crude cellulase were evaluated for improvements in cellulase activities as well as for enhanced hydrolysis of dilute acid pretreated wheat straw (PWS). The blending of crude enzymes of P and E enhanced the hydrolysis of PWS more effectively due to synergism in cellulolytic enzyme activities. Here, three types of blends were made on the basis of equal FPUs, equal protein content or fixed volume containing different proportions of individual enzymes, the former blend hydrolyzed 42.6% of PWS due to the 98%,62%, 64% and 34% synergistic enhancement in endo-glucanase, cellulase (FPU), β-glucosidase and xylanase activities, respectively. Hydrolysis at 10% solid loading of PWS in roller bottle reactor with this blend further enhanced hydrolysis yield to 74% within 24 h, which was much better than the corresponding hydrolysis yields of individual (38.1% by E and 61.5% by P) or the commercial enzyme (62.3%). This study proved that synergistic blends of cellulases from two Penicillium spp. are cost-effective tools for efficient wheat straw hydrolysis for on-site biofuel production.     

Cellulase production using biomass feed stock and its application in lignocellulose saccharification for bio-ethanol production

A major constraint in the enzymatic saccharification of biomass for ethanol production is the cost of cellulase enzymes. Production cost of cellulases may be brought down by multifaceted approaches which include the use of cheap lignocellulosic substrates for fermentation production of the enzyme, and the use of cost efficient fermentation strategies like solid state fermentation (SSF). In the present study, cellulolytic enzymes for biomass hydrolysis were produced using solid state fermentation on wheat bran as substrate. Crude cellulase and a relatively glucose tolerant BGL were produced using fungi Trichoderma reesei RUT C30 and Aspergillus niger MTCC 7956, respectively. Saccharification of three different feed stock, i.e. sugar cane bagasse, rice straw and water hyacinth biomass was studied using the enzymes. Saccharification was performed with 50 FPU of cellulase and 10 U of β-glucosidase per gram of pretreated biomass. Highest yield of reducing sugars (26.3 g/L) was obtained from rice straw followed by sugar cane bagasse (17.79 g/L). The enzymatic hydrolysate of rice straw was used as substrate for ethanol production by Saccharomyces cerevisiae. The yield of ethanol was 0.093 g per gram of pretreated rice straw.     

Hydrolysis of pretreated rice straw by an enzyme cocktail comprising acidic xylanase from Aspergillus sp. for bioethanol production

The most crucial enzyme involved in xylan hydrolysis is endoxylanase which cleaves the internal glycosidic bonds of xylan. The aim of this work was to study the production of extracellular xylanase by a locally isolated strain of Aspergillus sp. under solid-state fermentation (SSF) and to evaluate the potential of the enzyme in enzymatic hydrolysis of pretreated rice straw. Xylanase production reached maximum with incubation period (96 h), moisture level (80%), inoculum size (3 × 10⁶ spores/mL), pH (4.8), temperature (25 °C), carbon source (wheat bran) and nitrogen source (yeast extract). Under optimized conditions, xylanase production reached to 5059 IU/gds. Crude xylanase was used for supplementing the enzyme cocktail comprising cellulases (Zytex, India), β-glucosidase (In-house) and xylanase (In-house) for the saccharification of alkali-pretreated rice straw to get the maximum reducing sugar production. The cocktail containing the three enzymes resulted a maximum of 574.8 mg/g of total reducing sugars in comparison to 430.2 mg/g sugars by the cocktail without xylanase. These results proved that the crude xylanase preparation from Aspergillus sp. could be a potent candidate for the enzyme cocktail preparation for biomass hydrolysis in lignocellulosic bioethanol program.     

Characterization of a Trichoderma atroviride strain isolated from switchgrass bales and its use to saccharify ammonia-pretreated switchgrass for biobutanol production

The feedstock-specific enzyme systems for saccharification of biofuel feedstocks like switchgrass may potentially provide better enzymatic systems for production of second-generation biofuels. One strategy to develop these enzyme systems could be to harness the microorganisms growing naturally on specific feedstocks. This study presents the isolation and screening of fungal cultures from switchgrass bales for saccharification of ammonia-pretreated switchgrass for subsequent biobutanol production. The best performing fungal isolate during screening was identified through Sanger sequencing of its ITS region to be a unique strain of Trichoderma atroviride and further characterized for production of an enzyme system for saccharification of ammonia pretreated switchgrass. The maximum FPase, CMCase and xylanase activity produced by T. atroviride CUA1 were 0.25 fpu/mL, 0.18 IU/mL and 5.8 IU/mL, respectively. T. atroviride CUA1 also produced considerable amount of β-glucosidase activity. This isolate was used to produce an enzyme system to convert switchgrass to soluble sugars that were then fermented to butanol, ethanol, acetate and butyrate. Glucose was the major product of hydrolysis of ammonia-pretreated switchgrass performed using the enzyme system produced by the isolate. This fungus may be useful for the hydrolysis for the bioenergy crop of switchgrass to overcome this rate-limiting step in the overall conversion of biomass to biofuels.     

Enzymatic hydrolysis and fermentation of crushed whole sugar beets

Pectinase and cellulase enzymes were used for hydrolysis of whole sugar beets and the hydrolyzates were fermented with Escherichia coli KO11 and Saccharomyces cerevisiae via simultaneous saccharification and fermentation (SSF). Ethanol production rate was significantly higher for S. cerevisiae than for E. coli KO11. The combined effect of pectinase and cellulase loadings on ethanol production as well as residual galacturonic acid and arabinose concentrations were modeled for fermentations with S. cerevisiae. Ethanol yields of more than 92% were reached with moderate to high cellulase and pectinase loadings at 0.51 FPU g⁻¹ and 51 U g⁻¹ of dry biomass, respectively. Ethanol yields of 85% were achieved without any enzyme addition. However, addition of cellulase and pectinase enzymes increased effluent arabinose and galacturonic acid concentrations and reduced total suspended solids. This study demonstrated the yield potential of fermentation of crushed, whole sugar beets with or without the addition of cellulase and pectinase enzymes.     

Fermentative hydrogen production from macro-algae Laminaria japonica using anaerobic mixed bacteria

In this study, one macro-alga (Laminaria japonica) was used for fermentative hydrogen production by anaerobic mixed bacteria. The saccharification efficiency and hydrogen production by L. japonica with four different pretreatment methods, including heat, acid, alkaline and ultrasonic treatment, were investigated. The results showed that the saccharification efficiency from L. japonica that was pretreated with acid was the highest among the four methods. The saccharification efficiency for the total reducing sugars in the acid-pretreated L. japonica was 350.54 ± 19.89 mg/g (mean ± S.E.). The cumulative hydrogen production was 66.68 ± 5.68 mL/g from the heat-pretreated L. japonica, whereas that of L. japonica that was subjected to acid, alkaline, and ultrasonic pretreatment and the control was 43.65 ± 6.87 mL/g, 15.00 ± 3.89 mL/g, 23.56 ± 4.56 mL/g and 10.00 ± 1.21 mL/g, respectively. In addition, the effects of substrate concentration and initial pH on hydrogen production from heat-pretreated L. japonica were also analyzed. The results showed that the maximum hydrogen production was 83.45 ± 6.96 mL/g with a hydrogen concentration of approximately 28.4% from heat-pretreated L. japonica when the initial pH and substrate concentration were determined to be 6.0 and 2%, respectively. Heat pretreatment was the most effective method for increasing fermentative hydrogen production when L. japonica was used as the only substrate.     

Simultaneous enzymatic saccharification and ABE fermentation using pretreated oil palm empty fruit bunch as substrate to produce butanol and hydrogen as biofuel

Simultaneous saccharification and acetone–ethanol–butanol (ABE) fermentation was conducted in order to reduce the number of steps involved in the conversion of lignocellulosic biomass into butanol. Enzymatic saccharification of pretreated oil palm empty fruit bunch (OPEFB) by cellulase produced 31.58 g/l of fermentable sugar. This saccharification was conducted at conditions similar to the conditions required for ABE fermentation. The simultaneous process by Clostridium acetobutylicum ATCC 824 produced 4.45 g/l of ABE with butanol concentration of 2.75 g/l. The butanol yield of 0.11 g/g and ABE yield of 0.18 g/g were obtained from this simultaneous process as compared to the two-step process (0.10 g/g of butanol yield and 0.14 g/g of ABE yield). In addition, the simultaneous process also produced higher cumulative hydrogen (282.42 ml) than to the two-step process (222.02 ml) after 96 h of fermentation time. This study suggested that the simultaneous process has the potential to be implemented for the integrated production of butanol and hydrogen from lignocellulosic biomass.     

Recombinant multi-functional cellulase activity in submerged fermentation of lignocellulosic wastes

The expression of the multi-functional cellulase gene mfc in Coprinopsis cinerea is modulated using glyceraldehyde-3-phosphate dehydrogenase (gpd) promoter fragments from Agaricus bisporus, Flammulina velutipes, and Lentinula edodes. In submerged fermentation, with banana peels as the growth substrate, highest activities of endo-β-1,4-glucanase (0.48 U/ml), total cellulase (0.26 U/ml) and endo-β-1,4-xylanase (38.10 U/ml) were noted in the culture liquid Cabm44, which uses a 275 bp gpd fragment from A. bisporus. The lignocellulolytic enzymatic activities were increased nearly twofold in comparison with the wild-type strain.     

Conversion of paper sludge to ethanol by separate hydrolysis and fermentation (SHF) using Saccharomyces cerevisiae

The conversion of ethanol from paper sludge using the separate hydrolysis and fermentation (SHF) process with cellulase and Saccharomyces cerevisiae GIM-2 were investigated in this paper. Optimization strategy based on statistical experimental designs was employed to enhance degree of saccharification by enzymatic hydrolysis of paper sludge. Based on the Plackett-Burman design, hydrolysis time, substrate concentration and cellulase dosage were selected as the most significant variable on the degree of saccharification. Subsequently, the optimum combination of the selected factors was investigated by a Box-Behnken approach. A mathematical model was developed to show the effects of each factor and their combinatorial interactions on the degree of saccharification. The optimal conditions were hydrolysis time 82.7 h, substrate concentration 40.8 g L⁻¹ and cellulase dosage 18.1 FPU g⁻¹ substrate, and a degree of saccharification of 82.1% can be achieved. When hydrolysate was further fermented with S. cerevisiae GIM-2, the conversion rate of sugar to ethanol was 34.2% and the ethanol yield was 190 g kg⁻¹ of dry paper sludge, corresponding to an overall conversion yield of 56.3% of the available carbohydrates on the initial substrate. The results derived from this study indicate that the response surface methodology is a useful tool for optimizing the hydrolysis conditions to converse paper sludge to ethanol.     

Potential for using enriched cultures and thermotolerant bacterial isolates for production of biohydrogen from oil palm sap and microbial community analysis

A limited number of bacteria can convert oil palm (Elaeis guineensis) sap to hydrogen with satisfactory yield and productivity. In this study, a total of 18 fermentative enriched cultures and 36 newly isolated thermotolerant bacterial strains were compared for hydrogen production from oil palm (OP) sap. The new isolates were obtained from hot springs, palm oil mill effluent and oil palm sap. The test was conducted in three steps: (i) a test for hydrogen production from mixed substrates (cellulose, starch, xylose, and glucose) and OP sap; (ii) a test for substrate concentration tolerance; and (iii) a test for thermotolerance. Five enriched candidates for each of the hydrogen producers were selected according to the criteria defined for the screening test. The hydrogen production of these selected bacterial strains from hot springs were cultivated in batch fermentation of oil palm sap at room temperature (30 ± 2 °C). Five enriched cultures, namely 81RN1, OPS, 85RN5, 89SR3-2 and 112YL1 were found to give high cumulative hydrogen formation of 1085, 1009, 994, 983 and 778 mL H₂/L-OP sap, respectively, with the hydrogen content of 29.8, 29.4, 28.7, 27.1 and 27.5%, respectively. PCR–DGGE profiling showed that all these five enriched cultures consisted of species closely related to the genus Clostridium sp. based on the 16S rRNA gene. For pure cultures, the top five hydrogen producers were the isolates encoded as PS-3, PS-4, PS-5, PS-7 and PS-8 exhibiting the hydrogen production of 1973, 1774, 1335, 1170 and 1070 mL H₂/L-OP sap, respectively, with the hydrogen content of 33.7, 29.6, 32.5, 31.5 and 26.4%, respectively. Identification of these high hydrogen producers using 16S rRNA sequence matching showed that the isolates PS-3 and PS-8 belonged to Clostridium beijerinckii, while the isolate PS-7 belonged to Clostridium acetobutylicum and the isolates PS-4 and PS-5 belonged to Klebsiella sp. and Klebsiella pneumoniae, respectively. Therefore, the pure culture C. beijerinckii PS-3 exhibited 1.8 folds higher hydrogen production (1973 mL H₂/L-OP sap) than the enriched cultures of 81RN1 (1085 mL H₂/L-OP sap).     

Enhanced bio-hydrogen production from cornstalk hydrolysate pretreated by alkaline-enzymolysis with orthogonal design method

Bio-hydrogen (H₂) production from renewable biomass has been accepted as a promising method to produce an alternative fuel for the future. In this study, fermentative hydrogen production from cornstalk (CS) hydrolysate pretreated by alkaline-enzymolysis method was investigated. Meanwhile, a five-factor and five-level orthogonal experimental array was designed to study the influences of Ca(OH)₂ concentration, alkaline hydrolysis time, alkaline hydrolysis temperature, cellulase and xylanase dosages on cornstalk pretreatment and hydrogen production. A maximum reducing sugar yield of 0.59 g/g-CS was obtained at Ca(OH)₂ 0.5%, hydrolysis temperature 115 °C, hydrolysis time 1.5 h, cellulase dosage 4000 U/g-CS and xylanase 4000 U/g-CS. Under this same condition, the maximum hydrogen yields of 168.9 mL/g-CS, 357.6 mL/g-CS, and 424.3 mL/g-CS were obtained at dark-fermentation, photo-fermentation, and two-stage fermentation respectively. It's also found that the significance of these five parameters on H₂ production followed from high to low order as: Ca(OH)₂ concentration, cellulase dosage, xylanase dosage, hydrolysis time, and hydrolysis temperature. By comparing the energy produced with the energy spent, the maximum Energy Sustainability Index (ESI) value of 1.11 was obtained at the two-stage fermentation. The results suggested that two-stage fermentation is a promising and efficient way for hydrogen production from lignocellulosic biomass.     

Developing a thermophilic hydrogen-producing microbial consortia from geothermal spring for efficient utilization of xylose and glucose mixed substrates and oil palm trunk hydrolysate

Xylose and glucose are the major sugar components of lignocellulosic hydrolysate. This study aims to develop thermophilic hydrogen-producing consortia from eight sediments-rich samples of geothermal springs in Southern Thailand by repeated batch cultivation at 60 °C with glucose, xylose and xylose-glucose mixed substrates. Significant hydrogen production potentials were obtained from thermophilic enriched cultures encoded as PGR and YLT with the maximum hydrogen yields of 241.4 and 231.6 mL H₂/g sugar_consumed, respectively. After repeated batch cultivation the hydrogen yield from xylose-glucose mixed substrate of PGR increased to 375 mL H₂/g sugar_consumed which was 30% higher than that of YLT (287 mL H₂/g sugar_consumed). Soluble metabolites from xylose-glucose mixed substrates were composed mostly of butyric acid (20.6-21.8 mM), acetic acid (7.2-13.5 mM), lactic acid (8.2-11.7 mM) and butanol (4.4-13.0 mM). Denaturing gradient gel electrophoresis (DGGE) profiles illustrated small difference in microbial patterns of PGR enriched with glucose, xylose-glucose mixed substrate and xylose. The dominant populations were affiliated with low G + C content Gram-positive bacteria, Thermoanaerobacterium sp., Thermoanaerobacter sp., Caloramater sp. and Anoxybacillus sp. based on the 16S rRNA gene. Cultivation of the enriched culture PGR in oil palm trunk hydrolysate, the maximum hydrogen yield of 301 mL H₂/g sugar_consumed was achieved at hydrolysate concentration of 40% (v/v). At higher concentration to 80% (v/v), the hydrogen fermentation process was inhibited. Therefore, the efficient thermophilic hydrogen-producing consortia PGR has successfully developed and has great potential for production of biohydrogen from mixed sugars hydrolysate.     

Yeast and enzymatic hydrolysis in converting Chlorella biomass into hydrogen gas by Rhodobacter sp. and Rhodopseudomonas palustris

Enhanced hydrogen evolution was pursued in this work. Rhodobacter sp. (Rb) and Rhodopseudomonas palustris (Rp), single or mixed were used to extract hydrogen molecules from Chlorella fusca biomass. To elevate their fermentable contents, Chlorella was grown at nitrogen and/or phosphorus deprivation. Besides, cellulase and/or macerozyme, Triton X100 or sonicated yeast were applied for further biohydrogen fermentation. Utilizing hydrolysates of mineral deprived Chlorella cultures, Rb exhibited relatively higher cumulative hydrogen (4200 ml L^?1) than Rp (2500 ml L^?1) while mixed cultures attained significantly higher levels (4700 ml L^?1). Triton or enzymes significantly enhanced hydrogen evolution, with more effectiveness of macerozyme than cellulase. A novel use of sonicated yeast, as enzymes pool, induced the highest significant collective H₂ (up to 47 times that of microalgal supernatant). Sonicated yeast induced a remarkable hydrolysis of algae, as inferred from increased reducing sugars. However, hydrogen evolution efficiency exhibited poor proportionality with reducing sugars, indicating fermentation of other metabolites.