Hydrogenases and photobiological hydrogen production utilizing nitrogenase system in cyanobacteria

We constructed three hydrogenase mutants from Anabaena sp. PCC 7120: ΔhupL (deficient in uptake hydrogenase), ΔhoxH (deficient in bidirectional hydrogenase), and ΔhupL/ΔhoxH (deficient in both genes), and showed that the Δhup and ΔhupL/ΔhoxH produced H₂ at a rate 4–7 times that of wild-type under optimal conditions (Appl. Microbiol. Biotechnol. 58 (2002) 618). We have studied H₂ producing activity of Δhup in more detail. H₂ producing activity of Δhup cells was moderately improved in older cultures when 1% CO₂ was added to the bubbling air. The efficiency of light energy conversion to H₂ by the ΔhupL mutant at its highest H₂ production stage was 1.0–1.6% at an actinic visible light intensity of lower than 50 W/m² under argon atmosphere, and the activity lasted for at least 35 min. At 250 W/m², H₂ producing activity gradually decreased with illumination time.     

Extended H2 photoproduction by N2-fixing cyanobacteria immobilized in thin alginate films

Screening of the University of Helsinki Culture Collection for naturally good H₂ producing cyanobacteria recently revealed several promising strains. One of the superior strains is Calothrix 336/3, an N₂-fixing heterocystous filamentous cyanobacterium. Making use of an important feature of the Calothrix 336/3 cells to adhere to the substrate, we applied an immobilization technique to improve H₂ production capacity of this strain. We examined the basic properties of immobilization in Ca²⁺-alginate films in response to the production of H₂ of the Calothrix 336/3 strain and as reference strains we used a model organism Anabaena PCC 7120 and its uptake hydrogenase mutant, ΔhupL, that allow us to compare the responses of different strains to alginate entrapment. Immobilization of the Calothrix 336/3 and ΔhupL mutant cells in Ca²⁺-alginate resulted in prolonged H₂ production over several cycles. Immobilization of the Calothrix 336/3 cells was most successful and production of H₂ could be measured even after 40 days after immobilization.     

Sustained photobiological hydrogen production in the presence of N2 by nitrogenase mutants of the heterocyst-forming cyanobacterium Anabaena

Heterocyst-forming cells of the cyanobacterium Anabaena sp. strain PCC 7120 ΔHup, lacking an uptake hydrogenase, photobiologically produce H₂ by nitrogenase. Under N₂-rich atmosphere, the nitrogenase activity declines in a rather short time due to the sufficiency of combined nitrogen. From the parental ΔHup strain, site-directed double-crossover variants, dc-Q193S and dc-R284H, were created with amino acid substitutions presumed to be located in the vicinity of the FeMo-cofactor of nitrogenase. Unlike the case for the ΔHup strain, H₂ production activities of the variants were not decreased by the presence of high concentrations of N₂ and they continuously produced H₂ over 21 days with occasional headspace gas replacement. This property of N₂ insensitivity is a potentially useful strategy for reducing the cost of the culture gas in future practical applications of sustainable biofuel production. This Anabaena strain has only the Mo-containing nitrogenase which reduces acetylene to ethylene, but the dc-Q193S variant also produced ethane at low but measurable rates along with greater rates of ethylene production.     

Biohydrogen production by Anabaena sp. PCC 7120 wild-type and mutants under different conditions: Light, nickel, propane, carbon dioxide and nitrogen

Increasing awareness of environmental problems caused by the current use of fossil fuel-based energy, has led to the search for alternatives. Hydrogen is a good alternative and the cyanobacterium Anabaena sp. PCC 7120 is naturally able to produce molecular hydrogen, photosynthetically from water and light. However, this H₂ is rapidly consumed by the uptake hydrogenase.This study evaluated the hydrogen production of Anabaena sp. PCC 7120 wild-type and mutants: hupL⁻ (deficient in the uptake hydrogenase), hoxH⁻ (deficient in the bidirectional hydrogenase) and hupL⁻/hoxH⁻ (deficient in both hydrogenases) on several experimental conditions, such as gas atmosphere (argon and propane with or without N₂ and/or CO₂ addition), light intensity (54 and 152 ??Em⁻²s⁻¹), light regime (continuous and light/dark cycles 16 h/8 h) and nickel concentrations in the culture medium.In every assay, the hupL⁻ and hupL⁻/hoxH⁻ mutants stood out over wild-type cells and the hoxH⁻ mutant. Nevertheless, the hupL⁻ mutant showed the best hydrogen production except in an argon atmosphere under 16 h light/8 h dark cycles at 54 ??Em⁻²s⁻¹ in the light period, with 1 ??M of NiCl₂ supplementation in the culture medium, and under a propane atmosphere.In all strains, higher light intensity leads to higher hydrogen production and if there is a daily 1% of CO₂ addition in the gas atmosphere, hydrogen production could increase 5.8 times, related to the great increase in heterocysts differentiation (5 times more, approximately), whereas nickel supplementation in the culture medium was not shown to increase hydrogen production. The daily incorporation of 1% of CO₂ plus 1% of N₂ did not affect positively hydrogen production rate.     

A hydrogen-producing, hydrogenase-free mutant strain of Nostoc punctiforme ATCC 29133

The hupL gene, encoding the uptake hydrogenase large subunit, in Nostoc sp. strain ATCC 29133, a strain lacking a bidirectional hydrogenase, was inactivated by insertional mutagenesis. Recombinant strains were isolated and analysed, and one hupL⁻ strain, NHM5, was selected for further study. Cultures of NHM5 were grown under nitrogen-fixing conditions and H₂ evolution under air was observed using an H₂ electrode.     

La1−xSrxMO3 (M = Mn, Fe) perovskites as materials for thermochemical hydrogen production in conventional and membrane reactors

La_1−xSr_xMO₃ (M = Mn, Fe) perovskites are investigated as potential redox materials for the thermochemical production of hydrogen. Thermogravimetric oxidation/reduction experiments indicated that the materials are able to lose and uptake oxygen reversibly from their lattice up to 5.5 wt.% for La_1−xSr_xMnO₃ with x = 1 and up to 1.7 wt.% for La_1−xSr_xFeO₃ with x = 0. Pulse reaction experiments indicated that the materials can be used as redox catalysts in a redox process where water is dissociated giving rise to the production of pure hydrogen during the oxidation step. The oxidation and reduction steps can be combined in a membrane reactor constructed from dense perovskite membranes towards a continuous and isothermal operation. The system is also able to operate on partial pressure-based desorption without the need of a carbon-containing reductant, so that a process towards hydrogen production, based only on renewable hydrogen source such as water, can be established. At steady state and 900 ^°C, 25 ± 7 cm³ (STP) H₂ m⁻² min⁻¹ is produced in purified state.     

Visible light-induced hydrogen over CuFeO2 via S2O3 oxidation

The properties of CuFeO₂ have been studied according to the catalytic hydrogen production upon visible light. CuFeO₂ with a low band gap E_g, a good chemical stability and a suitable flat band potential appears as a suitable candidate. The potential of photoelectrons allows favorably a thermodynamically H₂-evolution from alkaline thiosulfate S₂O₃²⁻ solution. There is a major difference between pure and loaded oxide with some metal catalysts. Our best results have been obtained with unloaded CuFeO₂ at 50 °C and pH 13.60. Thiosulfate S₂O₃²⁻ ions can be oxidized to sulfite SO₃²⁻ and subsequently to sulfate SO₄²⁻ and the electronic exchange occurs via mediation of surface states. The quite high H₂-formation at the beginning shows a tendency towards saturation, it competes with SO₃²⁻ produced by parallel oxidation of S₂O₃²⁻.     

Enhancement of hydrogen production by the filamentous non-heterocystous cyanobacterium Arthrospira sp. PCC 8005

The efficiency of hydrogen production by different cyanobacterial species depends on several external factors. We report here the factors enhancing hydrogen production by filamentous non-heterocystous cyanobacterium Arthrospira sp. PCC 8005. Cells adapted to dark-anaerobic conditions produced hydrogen consistent with increased hydrogenase activity when supplemented with Fe²⁺. Stimulation of hydrogen production could be achieved by addition of reductants, either dithiothreitol or β-mercaptoethanol with higher production observed with the latter. Additionally, Fe²⁺ and β-mercaptoethanol added to nitrogen- and sulphur-deprived cells significantly stimulated H₂ production with maximal value of 5.91 ± 0.14 μmol H₂ mg Chla⁻¹ h⁻¹. Glucose and a small increase of osmolality imposed by either NaCl or sorbitol enhanced hydrogen production. High rates of hydrogen production were obtained in cells adapted in nitrogen-deprived medium with neutral and alkaline external pH, significant decrease of hydrogen production occurred under acidic external pH.     

Synthesis and characterization of oxygen-rich delafossite CuYO2+x—Application to H2-photo production

Here we report the synthesis and photo electrochemical properties of super oxides CuYO_2.50 and CuYO_2.25 prepared from the delafossite CuYO₂, respectively, by thermal oxidation at 380 °C under O₂-flow and soft chemistry in NaBrO solution (5 N). Their applications as catalysts for H₂ evolution upon visible light were investigated. The oxygen insertion was accompanied by partial oxidation of Cu⁺. For CuYO_2.25, the chemical analyses revealed the presence of mixed valent states containing at least formally an equal number of Cu⁺ and Cu²⁺. The thermal analysis (TGA) under reducing atmosphere indicates that oxygen is inserted in different crystallographic sites, for CuYO_2.25 it exhibits a two-step reduction mechanism with restoration of the parent oxide. In air, CuYO_2+x is thermally stable up to 500 °C above which it undergoes irreversible conversion into Cu₂Y₂O₅. They display p-type behavior ascribed to oxygen insertion and the conduction occurs by hopping mechanism between mixed copper valences. Under illumination, the oxides are stabilized by hole consumption reactions involving SO₃²⁻ and S²⁻ as holes scavengers. The flat-band potentials, lying between 0.17 and 0.26 V_SCE, allow a spontaneous H₂-photo formation. The rate of H₂-evolution is altered by the oxygen insertion and the best photo activity (1.33 μmol h⁻¹ mg⁻¹) was obtained over CuYO_2.25 immersed in S²⁻ solution (0.025 M); CuYO₂ is also reported for a comparison goal. Over time, the photoactivity is slowed down because of the competitive reduction of H₂O with the final products namely S₂O₆²⁻ and S_n²⁻.     

Isolation and evaluation of a high H2-producing lab isolate from cow dung

Hydrogen producing bacterial strain was isolated from Indian cow dung and identified of the bacterial family Enterobacteriaceae. This lab isolate was differentiated from Citrobacter Y-19 at molecular level by using RAPD, PCR based technique, and OPO-03₄₆₀ and OPO-17₈₀₀ RAPD marker for this specific strain (lab isolate) was identified. Fermentative studies were investigated for important parameters, starting with pH of the culture, temperature, inoculum age and inoculum volume, initial substrate concentration and different substrates. Among different substrates, dextrose and sucrose were the preferred substrates for hydrogen production. The optimal starting pH of the culture was found to be 5.0. The H₂ production increased with increase in temperature up to 30 °C. The maximum value of H₂ production was recorded when inoculum volume was 12.5% of the culture broth and inoculum age was 14 h. Under batch fermentation conditions, the maximum hydrogen production rate and yield were 355.2 ml l⁻¹ h⁻¹ and 2.1 mol/mol glucose (conversion 35%), respectively. These results indicate that this lab isolate is an ideal hydrogen producer.     

Hydrogen production based on the heterologous expression of NAD+-reducing [NiFe]-hydrogenase from Cupriavidus necator in different genetic backgrounds of Escherichia coli strains

This study explored the genetic engineering of Escherichia coli for hydrogen (H₂) production. In E. coli W3110, the introduction of NAD⁺-reducing [NiFe]-hydrogenase from Cupriavidus necator, combined with the inactivation of three endogenous [NiFe]-hydrogenases, exhibited not only H₂ production but also H₂ uptake based on exogenous hydrogenase. Although the H₂ production ability was much lower than the H₂ uptake ability, inactivation of the ethanol, lactate, and succinate production pathways resulted in a marked increase in H₂ production, demonstrating the bidirectional hydrogenase function in vivo depending on NADH/NAD⁺. Unexpectedly, H₂ production was completely repressed under conditions for high expression of exogenous hydrogenase. Furthermore, the introduction of the heterologous enzyme markedly repressed the endogenous H₂ production ability of E. coli W3110 but not the HST02. These in vivo behaviors largely correlated with in vitro hydrogenase activity suggested complicated interactions between the native and nonnative functional expression of [NiFe]-hydrogenases.     

The photoinduced evolution of O2 and H2 from a WO3 aqueous suspension in the presence of Ce/Ce

This is a report on the production of O₂ and H₂ from photocatalytic and photochemical processes in the WO₃–H₂O–Ce⁴⁺_aq–hν system. The photoproduction of O₂ and H₂ was studied over the range of WO₃ concentrations from 2 to 8 g dm⁻³, and conduction band electron scavenger concentrations 1–20 mM Ce_aq⁴⁺. Medium and high concentrations of the electron scavenger gave mainly O₂ as the main product. Dilute solutions of [Ce_aq⁴⁺]< 2 mM initially produced dioxygen, and then hydrogen after an induction period of 3–4 h. Yields of 140–250 μmol O₂  h⁻¹ and 1–7 μmol H₂ h⁻¹ were obtained and were found to depend on the physical properties and content of WO₃, the concentration of the electron scavenger, illumination period and wavelength, and the radiation geometry. The photoactivity of the suspension was correlated to the level of crystallinity of WO₃ powders. The studied system utilizes WO₃ to accomplish the initial light absorption, charge separation, and production of O₂ and H⁺ from the interaction of water molecules with photogenerated WO₃ valence band holes, in the presence of Ce⁴⁺_aq species as a scavenger of conduction band electrons. This is followed by the evolution of H₂ from a homogeneous photochemical reduction of H⁺ and/or H₂O by photoexcited Ce³⁺_aq, formed from the earlier reduction of Ce⁴⁺_aq. The obtained results show that, with an appropriate design, tungsten trioxide is a promising material that can be used as a photoactive component in energy conversion systems or in environmental photocatalysis, using artificial or solar light.     

Hydrogen production from a carbon-monoxide oxidation pathway in Rubrivivax gelatinosus

Upon feeding CO to the gas phase of a photosynthetic bacterium Rubrivivax gelatinosus CBS, a CO oxidation: H₂ production pathway is quickly induced. Hydrogen is produced according to the equation CO+H₂O→CO₂+H₂. Two enzymes are known to be involved in this pathway: a CO dehydrogenase (CODH) with a pH optimum of 8.0 and above, and a hydrogenase with a pH optimum near 7.5. Carbon monoxide dehydrogenase also displays a temperature optimum near 50°C. When CO mass transfer is not limited during a CO uptake measurement, an extreme fast rate of CO uptake was determined, allowing for the removal of near 87% of the dissolved CO from a bacterial suspension within 10 s. This process has therefore two potential applications, one in the production of H₂ gas as a clean renewable fuel using the linked CO oxidation: H₂ production pathway, and another in using the CODH enzyme itself as a fuel–gas conditioning catalyst. These applications thereby will improve the overall H₂ economy when gasified waste biomass serves as the inexpensive feedstock.     

Hydrogen photoproduction from hydrogen sulfide on Bi2S3 catalyst

Films of polycrystalline Bi₂S₃ have been prepared onto bismuth and platinum substrates by electrodeposition from an aqueous sulfide bath. The films were thin, uniform and well adhered. Bi₂S₃ is a direct band gap semiconductor with a value of 1.28 eV optimally matched with the solar spectrum. The photoelectrochemical study was undertaken for the generation of hydrogen by using illuminated n-Bi₂S₃ particles; it was found that hydrogen evolution depends highly on the synthesis method of powder. Impregnation of platinum onto Bi₂S₃ shows a production enhancement of about 25%. The most active photocatalyst, prepared by a solvent thermal process and loaded with Pt in 0.1 M S²⁻ alkaline electrolyte, yields 2.13×10⁻² ml mg⁻¹ of H₂ after 4 h of irradiation with the visible output of a 500 W halogen lamp.     

Maximizing the hydrogen photoproduction yields in Chlamydomonas reinhardtii cultures: The effect of the H2 partial pressure

Photoproduction of H₂ gas has been examined in sulfur/phosphorus-deprived Chalmydomonas reinhardtii cultures, placed in photobioreactors (PhBRs) with different gas phase to liquid phase ratios (V_g.p./V_l.p.). The results demonstrate that an increase in the ratio stimulates H₂ photoproduction activity in both algal suspension cultures and in algae entrapped in thin alginate films. In suspension cultures, a 4× increase (from ∼0.5 to ∼2) in V_g.p./V_l.p results in a 2× increase (from 10.8 to 23.1 mmol l⁻¹ or 264–565 ml l⁻¹) in the total yield of H₂ gas. Remarkably, 565 ml of H₂ gas per liter of the suspension culture is the highest yield ever reported for a wild-type strain in a time period of less than 190 h. In immobilized algae, where diffusion of H₂ from the medium to the PhBR gas phase is not affected by mixing, the maximum rate and yield of H₂ photoproduction occur in PhBRs with V_g.p./V_l.p above 7 or in a PhBR with smaller headspace, if the H₂ is effectively removed from the medium by continuous flushing of the headspace with argon. These experiments in combination with studies of the direct inhibitory effect of high H₂ concentrations in the PhBR headspace on H₂ photoproduction activity in algal cultures clearly show that H₂ photoproduction in algae depends significantly on the partial pressure of H₂ (not O₂ as previously thought) in the PhBR gas phase.     

One-stage H2 and CH4 and two-stage H2 + CH4 production from grass silage and from solid and liquid fractions of NaOH pre-treated grass silage

In the present study, mesophilic CH₄ production from grass silage in a one-stage process was compared with the combined thermophilic H₂ and mesophilic CH₄ production in a two-stage process. In addition, solid and liquid fractions separated from NaOH pre-treated grass silage were also used as substrates. Results showed that higher CH₄ yield was obtained from grass silage in a two-stage process (467 ml g⁻¹ volatile solids (VS)_original) compared with a one-stage process (431 ml g⁻¹ VS_original). Similarly, CH₄ yield from solid fraction increased from 252 to 413 ml g⁻¹ VS_original whereas CH₄ yield from liquid fraction decreased from 82 to 60 ml g⁻¹ VS_original in a two-stage compared to a one-stage process. NaOH pre-treatment increased combined H₂ yield by 15% (from 5.54 to 6.46 ml g⁻¹ VS_original). In contrast, NaOH pre-treatment decreased the combined CH₄ yield by 23%. Compared to the energy value of CH₄ yield obtained, the energy value of H₂ yield remained low. According to this study, highest CH₄ yield (495 ml g⁻¹ VS_original) could be obtained, if grass silage was first pre-treated with NaOH, and the separated solid fraction was digested in a two-stage (thermophilic H₂ and mesophilic CH₄) process while the liquid fraction could be treated directly in a one-stage CH₄ process.     

Hydrogen–methane production from swine manure: Effect of pretreatment and VFAs accumulation on gas yield

A two-phase anaerobic process to produce hydrogen and methane from swine manure was investigated, using pretreated sludge with heat, acid and alkali treatment as inoculum. The relative order of pretreatment methods of H₂ productivity effectiveness and CH₄ productivity effectiveness produced by the residua of the first phase was heat treatment > alkali treatment > acid treatment. When the inoculum sludge was heat-treated at 80°C for 30 min, the H₂ and CH₄ production rate was the highest of 36.6, 201.7 ml (g TS)_added⁻¹. There were significant correlations between biogas production and accumulation of acetic acid and butyric acids. When propionic acid and total VFA concentrations reached about 2850 mg L⁻¹ and 10.0 g L⁻¹, respectively, the average H₂ production rate and H₂ content decreased from 7.6 ml d⁻¹(g VS)_added⁻¹ and 55.3% to 1.4 ml d⁻¹(g VS)_added⁻¹ and 43.2%, respectively. The activity of methanogenic bacteria was inhibited to a significant extent when the total VFA concentration was above 10.0 g L⁻¹, but this inhibitory effect weakened when the VFA concentration fell to 6200–8500 mg L⁻¹. Correspondingly, average CH₄ production rate increased from 4.0 ml d⁻¹(g TS)_added⁻¹ to 12.5 ml d⁻¹(g TS)_added⁻¹. Propionic acid was degraded rapidly only when acetic and butyric acid concentrations dropped to 2500 mg L⁻¹ and 1000 mg L⁻¹, respectively.     

Biohydrogen production from algal biomass (Anabaena sp. PCC 7120) cultivated in airlift photobioreactor

The present study deals with the optimization of pretreatment conditions followed by thermophilic dark fermentative hydrogen production using Anabaena PCC 7120 as substrate by mixed microflora. Different airlift photobioreactors with ratio of area of downcomer and riser (A_d/A_r) in range of 0.4–3.2 were considered. Maximum biomass concentration of 1.63 g L⁻¹ in 9 d under light intensity of 120 μE m⁻² s⁻¹ was observed at A_d/A_r of 1.6. The mixing time of the reactors was inversely proportional to A_d/A_r. Maximal H₂ production was found to be 1600 mL L⁻¹ upon pretreatment with amylase followed by thermophilic fermentation for 24 h compared to other methods like sonication (200 mL L⁻¹), autoclave (600 mL L⁻¹) and HCl treatment (1230 mL L⁻¹). The decrease of pH from 6.5 to 5.0 during fermentation was due to the accumulation of volatile fatty acids. Amylase pretreatment gave higher reducible sugar content of 7.6 g L⁻¹ as compare to other pretreatments. Thermophilic fermentation of pretreated Anabaena biomass by mixed bacterial culture was found suitable for H₂ production.