Chlorobium limicola forma thiosulfatophilum: Biocatalyst in the Production of Sulfur and Organic Carbon from a Gas Stream Containing H2S and CO2

Chlorobium limicola forma thiosulfatophilum (ATCC 17092) was grown in a 1-liter continuously stirred tank reactor (800-ml liquid volume) at pH 6.8, 30°C, saturated light intensity, and a gas flow rate of 23.6 ml/min from a gas cylinder blend consisting of 3.9 mol% H₂S, 9.2 mol% CO₂, 86.4 mol% N₂, and 0.5 mol% H₂. This is the first demonstration of photoautotrophic growth of a Chlorobium sp. on a continuous inorganic gas feed. A significant potential exists for applying this photoautotrophic process to desulfurization and CO₂ fixation of gases containing acidic components (H₂S and CO₂).     

Hydrogen production by sorption-enhanced steam reforming of glycerol

Catalytic steam reforming of glycerol for H₂ production has been evaluated experimentally in a continuous flow fixed-bed reactor. The experiments were carried out under atmospheric pressure within a temperature range of 400–700 °C. A commercial Ni-based catalyst and a dolomite sorbent were used for the steam reforming reactions and in situ CO₂ removal. The product gases were measured by on-line gas analysers. The results show that H₂ productivity is greatly increased with increasing temperature and the formation of methane by-product becomes negligible above 500 °C. The results suggest an optimal temperature of ∼500 °C for the glycerol steam reforming with in situ CO₂ removal using calcined dolomite as the sorbent, at which the CO₂ breakthrough time is longest and the H₂ purity is highest. The shrinking core model and the 1D-diffusion model describe well the CO₂ removal under the conditions of this work.     

Organic acid production from CO2/H2 and CO/H2 by mixed-culture anaerobes

The gases CO, CO₂, and H₂ were used as substrates in anaerobic fermentations producing organic acids. Various mixed bacterial sources were used, including sewage sludge digester effluent, rabbit feces, and soil. Nonsterile microorganism selection was carried out using CO₂/H₂ and CO/H₂ as the primary carbon and energy sources. Cultures were grown in specially designed, high-pressure (to 70 psig) flasks. Methanogenic bacteria were eliminated from the cultures. Liquid products of the fermentations were acetic through caproic acids, with the even-numbered acids predominating. Carbon balances showed conclusively that acetic acid was formed from carbon contained in the CO or CO₂ feed gas. Measurements made included rates of acid product formation, cell density, and degree of gas utilization. Limited characterization of the microorganisms was also performed. Production of organic acids by mixed culture inocula from CO₂/H₂ or CO/H₂ had not been reported previously. Application of this work is to the production of organic chemicals from synthesis gas (SNG), produced by the gasification of fossil fuels (peat, lignite, and various ranks of coals), biomass (agricultural and forest residues, and various biomass crops grown expressly for energy recovery), and municipal solid waste.     

Production of poly-β-hydroxybutyric acid from carbon dioxide by Alcaligenes eutrophus ATCC 17697T

The characteristics of PHB production from carbon dioxide by autotrophic culture of Alcaligenes eutrophus ATCC 17697^T using a recycled gas closed circuit culture system under the condition of oxygen limitation were investigated. Cell concentration increased to more than 60 g/l after 60 h of cultivation, while the PHB concentration reached 36 g/l. PHB accumulation in the oxygen-limited culture was superior than that in an ammonium-deficient culture. The PHB produced was identified as a homopolymer of d-3-hydroxybutyrate by ¹H and ¹³C NMR analysis. The stoichiometry for PHB production from CO₂ under the oxygen limitation condition was indicated to be as follows: 33H₂ + 12O₂ + 4CO₂ → C₄H₆O₂ + 30H₂O. This stoichiometry shows that the hydrogen consumption per one mole of CO₂ for PHB production is larger than that for cell formation.     

The influence of H2, CO2 and dilution rate on the continuous fermentation of acetone-butanol

Summary The effect of product gases, H₂ and CO₂, on solvent production was studied using a continuous culture of alginate-immobilized Clostridium acetobutylicum. Initially, in order to find the optimum dilution rate for aceton--butanol production in this system, fermentations were carried out at various dilution rates. With 10% H₂ and 10% CO₂ in the sparging gas, a dilution rate of 0.07 h^–1 was found to maximize volumetric productivity (0.58 g·l^–1·h^–1), while the maximum specific productivity of 0.27 g^–·h^–1 occured at 0.12 h^–1. Continuous cultures with vigorous sparging of N₂ produced only acids. It was concluded that in the case of continuous fermentation H₂ is essential for good solvent production, although good solvent production is possible in an H₂-absent environment in the case of batch fermentations. When the fermentation was carried out at atmospheric pressure under H₂-enriched conditions, the presence of CO₂ in the sparging gas did not slow down glucose metabolism; rather it changed the direction of the phosphoroclastic reaction and as a result increased the butanol/acetone ratio.     

A highly sensitive, flow through h(2) gas analyzer for use in nitrogen fixation studies

Studies of H₂ evolution by N₂ fixing systems are frequently limited by an inability to accurately measure H₂ gas concentrations of less than about 10 microliters per liter. In this study, a H₂ gas analyzer is described which is able to accurately and reproducibly detect up to 100 times lower H₂ concentrations than most thermal conductivity gas chromatographs or other conventional instruments used for the measurement of H₂ gas. This high level of sensitivity (maximum of about 0.02 microliter per liter H₂ per millivolt output) and the ability to continuously monitor H₂ concentration directly in a flowing gas stream, makes this instrument well suited for use in an open gas exchange system.

Since the sensor used in the instrument was also sensitive to other combustible gases, it was necessary to demonstrate that H₂ was the only combustible gas produced by the N₂ fixing system being studied. When an air stream was passed through a pot containing nodulated soybean (Glycine max L.) roots, gas chromatographic analysis of the effluent gas stream revealed that H₂ was the only combustible gas present. These results were supported by other studies in which no combustible gases were detected in the effluent gas stream from soybean roots nodulated with USDA 110, a Rhizobium strain which displays active uptake hydrogenase activity.

     

On-line monitoring and control of acetone-butanol fermentation by membrane-sensor mass spectrometry

A mass spectrometry (MS) membrane sensor was developed and applied to on-line product measurement in acetone-butanol fermentation. The sensor facilitated the monitoring of acetone, butanol, ethanol, H₂ and CO₂, and single-compound calibration curves for both acetone and butanol showed a linear relationship between the product concentration and the MS response. However, when an actual fermentation was monitored, the product concentration calculated from the MS response was smaller than the concentration determined by gas chromatography, and the relationship between the response and the product concentration was nonlinear. It was found that large amounts of gases (H₂, CO₂) entering the MS analyzation chamber were causing a ‘space charge effect’, which resulted in an MS response ceiling. The problem could be resolved by reducing the surface area of the sensor membrane. Under some fermentation conditions, a by-product, n-butyl butyrate, was produced, and this interfered with the measurement of butanol due to a peak overlapping effect. However, it was found that this could be compensated for by using an empirical equation. Application of the MS membrane sensor in a fed batch culture of acetone-butanol fermentation resulted in successful control of the butanol concentration.     

Assessment of Reductive Acetogenesis with Indigenous Ruminal Bacterium Populations and Acetitomaculum ruminis

The objective of this study was to evaluate the role of reductive acetogenesis as an alternative H₂ disposal mechanism in the rumen. H₂/CO₂-supported acetogenic ruminal bacteria were enumerated by using a selective inhibitor of methanogenesis, 2-bromoethanesulfonic acid (BES). Acetogenic bacteria ranged in density from 2.5 × 10⁵ cells/ml in beef cows fed a high-forage diet to 75 cells/ml in finishing steers fed a high-grain diet. Negligible endogenous acetogenic activity was demonstrated in incubations containing ruminal contents, NaH¹³CO₃, and 100% H₂ gas phase since [U-¹³C]acetate, as measured by mass spectroscopy, did not accumulate. Enhancement of acetogenesis was observed in these incubations when methanogenesis was inhibited by BES and/or by the addition of an axenic culture of the rumen acetogen Acetitomaculum ruminis 190A4 (10⁷ CFU/ml). To assess the relative importance of population density and/or H₂ concentration for reductive acetogenesis in ruminal contents, incubations as described above were performed under a 100% N₂ gas phase. Both selective inhibition of methanogenesis and A. ruminis 190A4 fortification (>10⁵ CFU/ml) were necessary for the detection of reductive acetogenesis under H₂-limiting conditions. Under these conditions, H₂ accumulated to 4,800 ppm. In contrast, H₂ accumulated to 400 ppm in incubations with active methanogenesis (without BES). These H₂ concentrations correlated well with the pure culture H₂ threshold concentrations determined for A. ruminis 190A4 (3,830 ppm) and the ruminal methanogen 10-16B (126 ppm). The data demonstrate that ruminal methanogenic bacteria limited reductive acetogenesis by lowering the H₂ partial pressure below the level necessary for H₂ utilization by A. ruminis 190A4.     

A method for equilibration chamber sampling and gas chromatographic analysis of the soil atmosphere

The method includes sampling of gases from an equilibration chamber permanently installed in the soil, transferring the sample to laboratory and subsequent measurement by gas chromatography. The equilibration chamber allows sampling of the gas phase both above and below the groundwater level, which is a major advantage. After significant concentration changes in non-saturated soils, gases in chambers regain equilibrium with the surrounding soils within 1–2 days. In the most unfavourable equilibration situations,i.e. in mineral subsoils with stagnant groundwater and very low biological activity, 90% equilibrium is attained in about 15 days. N₂, O₂+Ar, CO₂, CH₄, N₂O, H₂ and Ne, are measured on a series/bypass multi-column system, followed by a thermal conductivity detector.     

Influence of buffer system and pH on the amount of oxygen exchanged between solvent H2O and the CO2 produced in the aerobic oxidation of Cypridina luciferin catalyzed by Cypridina luciferase.

Incorporation of ¹⁸O into CO₂ was measured under various buffer conditions when the bioluminescent oxidation of Cypridina luciferin, catalyzed by luciferase, was carried out either in H₂¹⁶O medium with ¹⁸O₂ gas, or in H₂¹⁸O medium with ¹⁶O₂ gas. The results indicate that (1) the exchange of oxygen between CO₂ and solvent H₂O is significantly influenced by the kind of buffer as well as by pH, (2) the exchange of oxygen between solvent H₂O and CO₂ produced from luciferin in a neutral buffer can be reasonably well estimated from the exchange that takes place when the same amount of CO₂ gas is introduced into the same buffer by the presently employed method, and (3) in the Cypridina bioluminescent reaction, one of two oxygens of O₂ is quantitatively incorporated into the product CO₂ prior to the exchange of oxygen between CO₂ and solvent H₂O.     

Control of Oxidative Sulfur Metabolism of Chlorobium limicola forma thiosulfatophilum

A metered blend of anaerobic-grade N₂, CO₂, and H₂S gases was introduced into an illuminated, 800-ml liquid volume, continuously stirred tank reactor. The system, described as an anaerobic gas-to-liquid phase fed-batch reactor, was used to investigate the effects of H₂S flow rate and light energy on the accumulation of oxidized sulfur compounds formed by the photoautotroph Chlorobium limicola forma thiosulfatophilum during growth. Elemental sulfur was formed and accumulated in stoichiometric quantities when light energy and H₂S molar flow rate levels were optimally adjusted in the presence of nonlimiting CO₂. Deviation from the optimal H₂S and light energy levels resulted in either oxidation of sulfur or complete inhibition of sulfide oxidation. Based on these observations, a model of sulfide and sulfur oxidases electrochemically coupled to the photosynthetic reaction center of Chlorobium spp. is presented. The dynamic deregulation of oxidative pathways may be a mechanism for supplying the photosynthetic reaction center with a continuous source of electrons during periods of varying light and substrate availability, as in pond ecosystems where Chlorobium spp. are found. Possible applications for a sulfide gas removal process are discussed.     

H2-CO2 Recirculation and pH Control for Growth of Methanogens in Mass Culture

We modified a fermentor (10-liter liquid volume) for the growth of anaerobic, H₂-CO₂-catabolizing bacteria. Gas in the fermentor (ca. 10% CO₂, 50% H₂, 40% CH₄) was recirculated by a diaphragm pump. During growth, the gas composition was maintained by the addition of a mixture of 80% H₂ and 20% CO₂, and this addition was controlled by a pH auxostat. During gas addition, gas was discharged from the recirculating gas stream and was collected by the displacement of an acidified salt solution.     

Selection of sulfur source for methane production by Methanobacterium thermoautotrophicum

Sulfur sources capable of replacing sulfide were surveyed for biomethanation from H₂ and CO₂ by thermoautotrophic methanogen, Methanobacterium thermoautotrophicum. Among sulfur containing compounds tested, l-cysteine, thiosulfate and coenzyme M gave poor growth when added as sulfur sources, whereas simultaneous addition of two sulfur sources, l-cysteine+thiosulfate, l-cysteine+l-methionine or l-cysteine+coenzyme M stimulated the growth.In a pressure-controlled fermentor system developed to obtain stoichiometry between input and output gases, the ratio of H₂ and CO₂ consumption to CH₄ production was almost stoichiometric, and when l-cysteine and thiosulfate or l-methionine were used in place of sulfide (control) similar growth patterns were observed. In a culture with continuous supply of substrates gases (1.3 vvm) and sulfur sources of 1 mM l-cysteine+2 mM thiosulfate, specific growth rate and specific methane production rate were 0.35 h⁻ and 3.24 l g⁻¹h⁻¹, respectively, compared to 0.22 h⁻¹ and 5.76 l g⁻h⁻¹ with Na₂ S.     

A sensitive technique for the rapid measurement of carbon dioxide concentrations

A method has been developed to measure concentrations of CO₂ in gases rapidly. A gas sample is injected into a flowing carrier gas that passes through an infrared CO₂ analyzer. A strip chart recorded peak response is obtained which is proportional to the CO₂ concentration. A resolution of better than 2 microliters of CO₂ per liter of gas was obtained. Seven to 10 seconds were required for sample analysis once the sample was obtained. Sorghum bicolor plant respiration was determined at different temperatures by measuring CO₂ using this system and by using a conventional system. The correlation between techniques was 0.996, and about the same variation occurred within each method. This technique greatly increased the efficiency of the infrared CO₂ analyzer in our laboratory for use in plant respiration and photosynthetic studies.     

Resistance of citrus fruit to mass transport of water vapor and other gases

The resistance of oranges (Citrus sinensis L. Osbeck) and grapefruit (Citrus paradisi Macf.) to ethylene, O₂, CO₂, and H₂O mass transport was investigated anatomically with scanning electron microscope and physiologically by gas exchange measurements at steady state. The resistance of untreated fruit to water vapor is far less than to ethylene, CO₂ and O₂. Waxing partially or completely plugs stomatal pores and forms an intermittent cracked layer over the surface of fruit, restricting transport of ethylene, O₂, and CO₂, but not of water; whereas individual sealing of fruit with high density polyethylene films reduces water transport by 90% without substantially inhibiting gas exchange.

Stomata of harvested citrus fruits are essentially closed. However, ethylene, O₂ and CO₂ still diffuse mainly through the residual stomatal opening where the relative transport resistance (approximately 6,000 seconds per centimeter) depends on the relative diffusivity of each gas in air. Water moves preferentially by a different pathway, probably through a liquid aqueous phase in the cuticle where water conductance is 60-fold greater. Other gases are constrained from using this pathway because their diffusivity in liquid water is 10⁴-fold less than in air.

     

Metabolic selectivity and growth of<Emphasis Type="Italic"> Clostridium thermocellum</Emphasis> in continuous culture under elevated hydrostatic pressure

The continuous culture of Clostridium thermocellum, a thermophilic bacterium capable of producing ethanol from cellulosic material, is demonstrated at elevated hydrostatic pressure (7.0 MPa, 17.3 MPa) and compared with cultures at atmospheric pressure. A commercial limitation of ethanol production by C. thermocellum is low ethanol yield due to the formation of organic acids (acetate, lactate). At elevated hydrostatic pressure, ethanol:acetate (E/A) ratios increased >10² relative to atmospheric pressure. Cell growth was inhibited by approximately 40% and 60% for incubations at 7.0 MPa and 17.3 MPa, respectively, relative to continuous culture at atmospheric pressure. A decrease in the theoretical maximum growth yield and an increase in the maintenance coefficient indicated that more cellobiose and ATP are channeled towards maintaining cellular function in pressurized cultures. Shifts in product selectivity toward ethanol are consistent with previous observations of hydrostatic pressure effects in batch cultures. The results are partially attributed to the increasing concentration of dissolved product gases (H₂, CO₂) with increasing pressure; and they highlight the utility of continuous culture experiments for the quantification of the complex role of dissolved gas and pressure effects on metabolic activity.     

Computational screening of ZIFs for CO2 separations

Using molecular simulations, we studied a diverse collection of zeolite–imidazolate frameworks (ZIFs) to evaluate their performances in adsorption- and membrane-based gas separations. Molecular simulations were performed for both single-component gases (CH₄, CO₂, H₂ and N₂) and binary gas mixtures (CO₂/CH₄, CO₂/N₂, CO₂/H₂ and CH₄/H₂) to predict the intrinsic and mixture selectivities of ZIFs. These two selectivities were compared to discuss the importance of multi-component mixture effects on making predictions about the separation performance of a material. Gas separation performances of ZIFs were compared with other nanoporous materials and our results showed that several ZIFs can outperform well-known zeolites and metal–organic frameworks in CO₂ separations. Several other properties of ZIFs such as gas permeability, working capacity and sorbent selection parameter were computed to identify the most promising materials in adsorption- and membrane-based separation of CO₂/CH₄, CO₂/N₂, CO₂/H₂ and CH₄/H₂.     

Conversion of Cellulose to Methane and Carbon Dioxide by Triculture of Acetivibrio cellulolyticus, Desulfovibrio sp., and Methanosarcina barkeri

The fermentation of cellulose by monocultures of Acetivibrio cellulolyticus and cocultures of A. cellulolyticus-Methanosarcina barkeri, A. cellulolyticus-Desulfovibrio sp., and A. cellulolyticus-M. barkeri-Desulfovibrio sp. was studied. The monoculture produced ethanol, acetate, H₂, and CO₂. More acetate and less ethanol was formed by the cocultures than by the monoculture. Acetate was utilized by M. barkeri in coculture with A. cellulolyticus after a lag period, whereas ethanol was metabolized by the sulfate reducer only under conditions of low H₂ partial pressure, i.e., when cocultured with A. celluloyticus-M. barkeri or when grown together with the methanogen. Only the three-component culture carried out the rapid conversion of cellulose to CO₂ and methane. Furthermore, this culture hydrolyzed the most cellulose—85% of that initially present. This amount was increased to 90% by increasing the population of M. barkeri in the triculture. Methane production was also increased, and a quicker fermentation rate was achieved.     

Carbon and nitrogen mass balance during flue gas treatment with Dunaliella salina cultures

The biotreatment of flue gases with algae cultures is a promising option to sequestrate CO₂, yet the emission of other greenhouse gases (GHG) from the cultures can hamper their environmental benefit. Quantitative data on the sequestration potential for CO₂ and NO _x in relation to the direct production of CH₄ and N₂O are urgently required. The present study assessed the flows of carbon (C) and nitrogen (N) through cultures of the green alga Dunaliella salina, supplied with biodiesel flue gas, by means of mass balancing. D. salina was grown in artificially lighted, field- (42-L bubble column reactor) and laboratory-scale cultures (23 °C, pH 7.5). In the bubble column reactor, algae grew with an average specific growth rate of 0.237 day^?1 under flue gas supplementation (6.3 % (v/v) CO₂, 1.2 ppmv NO _x ), and CO₂ was retained to 39 % in the system. The specific sequestration rate for CO₂ was low, with 0.13 g CO₂ L^?1 day^?1. Cultures emitted up to 13.03 μg CH₄ L^?1 day^?1 and 4261 μg N₂O L^?1 day^?1. The moderate retention of NO _x -N was outweighed by emissions of N₂O-N, and total N in the system decreased by 15.48 % during the 9-day trial. Results suggest that GHG production was mainly the outcome of anaerobic microbial processes and their emission was lower in pre-sterilized cultures. Under the tested conditions, up to six times more CO₂ equivalents were emitted during flue gas treatment. Therefore, the direct GHG emissions of algae culture systems, intended for flue gas treatment (i.e. open ponds) need to be reviewed critically.