Photosynthetic efficiency and oxygen evolution of Chlamydomonas reinhardtii under continuous and flashing light

As a result of mixing and light attenuation in a photobioreactor (PBR), microalgae experience light/dark (L/D) cycles that can enhance PBR efficiency. One parameter which characterizes L/D cycles is the duty cycle; it determines the time fraction algae spend in the light. The objective of this study was to determine the influence of different duty cycles on oxygen yield on absorbed light energy and photosynthetic oxygen evolution. Net oxygen evolution of Chlamydomonas reinhardtii was measured for four duty cycles (0.05, 0.1, 0.2, and 0.5) in a biological oxygen monitor (BOM). Oversaturating light flashes were applied in a square-wave fashion with four flash frequencies (5, 10, 50, and 100 Hz). Algae were precultivated in a turbidostat and acclimated to a low photon flux density (PFD). A photosynthesis–irradiance (PI) curve was measured under continuous illumination and used to calculate the net oxygen yield, which was maximal between a PFD of 100 and 200 μmol m^?2?s^?1. Net oxygen yield under flashing light was duty cycle-dependent: the highest yield was observed at a duty cycle of 0.1 (i.e., time-averaged PFD of 115 μmol m^?2?s^?1). At lower duty cycles, maintenance respiration reduced net oxygen yield. At higher duty cycles, photon absorption rate exceeded the maximal photon utilization rate, and, as a result, surplus light energy was dissipated which led to a reduction in net oxygen yield. This behavior was identical with the observation under continuous light. Based on these data, the optimal balance between oxygen yield and production rate can be determined to maximize PBR productivity.     

Enhanced astaxanthin production from microalga,Haematococcus pluvialis by two-stage perfusion culture with stepwise light irradiation

For efficient astaxanthin production from the culture of green microalga, Haematococcus pluvialis, a two-stage mixotrophic culture system was established with stepwise increased light irradiance. By perfusion process, high density biomass (2.47 g/L) was achieved during the vegetative stage due to no detrimental effect of inhibitory metabolites, which was 3.09 and 1.67 times higher than batch and fed-batch processes, respectively. During the induction stage, biomass and astaxanthin were subsequently produced to the very high level 12.3 g/L and 602 mg/L, under stepwise increased light irradiance (150–450 μE/m²/s), respectively. These results indicate that the combinatorial approach of perfusion culture during the vegetative stage and stepwise light irradiation during the induction stage is a promising strategy for the simultaneous production of high concentration of biomass and astaxanthin in microalgae including H. pluvialis.     

Mixed culture of oleaginous yeast Rhodotorula glutinis and microalga Chlorella vulgaris for lipid production from industrial wastes and its use as biodiesel feedstock

A mixed culture of oleaginous yeast Rhodotorula glutinis and microalga Chlorella vulgaris was performed to enhance lipid production from industrial wastes. These included effluent from seafood processing plant and molasses from sugar cane plant. In the mixed culture, the yeast grew faster and the lipid production was higher than that in the pure cultures. This could be because microalga acted as an oxygen generator for yeast, while yeast provided CO(2) to microalga and both carried out the production of lipids. The optimal conditions for lipid production by the mixed culture were as follows: ratio of yeast to microalga at 1:1; initial pH at 5.0; molasses concentration at 1%; shaking speed at 200 rpm; and light intensity at 5.0 klux under 16:8 hours light and dark cycles. Under these conditions, the highest biomass of 4.63±0.15 g/L and lipid production of 2.88±0.16 g/L were obtained after five days of cultivation. In addition, the plant oil-like fatty acid composition of yeast and microalgal lipids suggested their high potential for use as biodiesel feedstock.     

Under low irradiation,the light regime modifies growth and metabolite production in various species of microalgae

The effects of continuous light exposure (24L:0D) and a 12 h:12 h light/dark regime (12L:12D) were compared on the growth and carotenoid, protein, sugar, lipid, and fatty acid contents in Chlorella vulgaris, Nannochloropsis sp., Isochrysis galbana, and Dunaliella salina cultured in a batchwise facility. These microalgae were grown axenically under a low photon flux density (PFD) of 27 μmol photons m^?2 s^?1. C. vulgaris, Nannochloropsis sp., and I. galbana exhibited the highest cell densities when cultured under 24L:0D, whereas D. salina grew better under the alternating light/dark regime. I. galbana accumulated high levels of proteins, sugars, and lipids and exhibited the highest carotenoid content under 24L:0D. Protein production was enhanced in C. vulgaris under 24L:0D. The highest total lipid content was recorded for D. salina, reaching 74.6 % of total proteins, sugars, and lipids in cells at the stationary phase when grown under 12L:12D. The light/dark regime at low PFD was sufficient to stimulate the accumulation of monounsaturated and polyunsaturated fatty acids in all four algae. Their levels, like those of saturated fatty acids, did not differ significantly under the two light regimes. D. salina was an important source of tetradecenoic acid 14:1(n-5). Nannochloropsis sp. produced a large amount of the essential eicosapentaenoic acid, which reached 20 % of total fatty acids under 12L:12D, while I. galbana exhibited the highest level of docosahexaenoic acid, which reached 21 % under both light regimes. This study demonstrated the feasibility of culturing microalgae under low PFD in order to produce large quantities of valuable metabolites, especially various lipids with neutraceutical value.     

Photosynthetic efficiency of Chlamydomonas reinhardtii in attenuated, flashing light

As a result of mixing and light attenuation, algae in a photobioreactor (PBR) alternate between light and dark zones and, therefore, experience variations in photon flux density (PFD). These variations in PFD are called light/dark (L/D) cycles. The objective of this study was to determine how these L/D cycles affect biomass yield on light energy in microalgae cultivation. For our work, we used controlled, short light path, laboratory, turbidostat‐operated PBRs equipped with a LED light source for square‐wave L/D cycles with frequencies from 1 to 100 Hz. Biomass density was adjusted that the PFD leaving the PBR was equal to the compensation point of photosynthesis. Algae were acclimated to a sub‐saturating incident PFD of 220 µmol m^?2 s^?1 for continuous light. Using a duty cycle of 0.5, we observed that L/D cycles of 1 and 10 Hz resulted on average in a 10% lower biomass yield, but L/D cycles of 100 Hz resulted on average in a 35% higher biomass yield than the yield obtained in continuous light. Our results show that interaction of L/D cycle frequency, culture density and incident PFD play a role in overall PBR productivity. Hence, appropriate L/D cycle setting by mixing strategy appears as a possible way to reduce the effect that dark zone exposure impinges on biomass yield in microalgae cultivation. The results may find application in optimization of outdoor PBR design to maximize biomass yields. Biotechnol. Bioeng. 2012; 109: 2567–2574. © 2012 Wiley Periodicals, Inc.     

Co-fermentation of cassava waste pulp hydrolysate with molasses to ethanol for economic optimization

Cassava waste pulp (CWP)–enzymatic hydrolysate was co-fermented with molasses (CWP-EH/molasses mixture) with the aim to optimize ethanol production by Saccharomyces cerevisiae TISTR 5606 (SC 90). The optimal fermentation conditions for ethanol production using this mixture were 245 g/L initial total sugar supplemented with KH₂PO₄ (8 g/L), at 30 °C for 48 h of fermentation under an oxygen-limited condition with agitation at 100 rpm, producing an ethanol concentration of 70.60 g/L (0.31 g ethanol/g total sugar). The addition of cassava tuber fiber (solid residue of CWP after enzymatic hydrolysis) at 30 g/L dry weight to the CWP-EH/molasses mixture increased ethanol production to 74.36 g/L (0.32 g ethanol/g total sugar). Co-fermentation of CWP-EH with molasses had the advantage of not requiring any supplementation of the fermentation mixture with reduced nitrogen.     

Evaluation of closed photobioreactor types and operation variables for enhancing lipid productivity of <Emphasis Type="Italic">Nannochloropsis sp.</Emphasis> KMMCC 290 for biodiesel production

Previously, we have successfully produced biodiesel using the marine microalga Nannochloropsis sp. KMMCC 290 cultivated in a raceway open pond. Here, we investigated the effects of closed photobioreactors and operating variables on cell concentration and lipid content of the microalga to increase its lipid productivity. The flatplate photobioreactor (FPP) showed higher performance than bubble column and air-lift photobioreactors. Among the variables evaluated, light intensity, aeration rate, and carbon dioxide feeding significantly influenced cell concentration, whereas a simultaneous increase in light intensity and aeration rate, as well as carbon dioxide feeding noticeably increased the lipid content. The lipid productivity in the FPP was 26.7 × 10^-3 g/L/day, which was 16.6 times higher than that produced by the microalga cultivated in the raceway pond, 4.8 times higher than that from the simple flask-grown control culture, and 2.1 times higher than that from the FPP under initial conditions.     

Chemical composition and ethanol production potential of Thai seaweed species

This study evaluated the potential use of several Thai seaweed species for ethanol production. The high biomass of the green algae Ulva intestinalis and Rhizoclonium riparium and the red algae Gracilaria salicornia and Gracilaria tenuistipitata in an earthen pond culture led us to select these species for our study. The seaweed species were analyzed for chemical composition, resulting in ash contents of 37.62?±?0.15 % and fiber of 11.93?±?0.16 %, with the highest values in R. riparium. Low lipid values were found in all species, with the highest value (p?<?0.05) in G. salicornia (1.69?±?0.07 %) and the lowest in R. riparium (0.28?±?0.01 %) and G. tenuistipitata (0.26?±?0.01 %). The highest carbohydrate contents were found in G. tenuistipitata (54.89 %), and the lowest were in R. riparium (29.53 %). G. tenuistipitata (8.58?±?0.36 %) and U. intestinalis (8.24?±?0.28 %) had higher sulfate contents compared with G. salicornia (4.69?±?0.04 %) and R. riparium (1.97?±?0.20 %). The monosugar algal tissue components were analyzed by HPLC; rhamnose, xylose, fucose, arabinose, mannose, glucose, and galactose were used as reference sugars. Total sugar was found to be highest in G. tenuistipitata (98.21 %). Arabinose, glucose, and galactose were the main sugar components in all species. Glucose obtained from G. tenuistipitata (6.55 %) and R. riparium (6.52 %) was higher than in G. salicornia (0.27 %) and U. intestinalis (2.78 %). G. tenuistipitata fermentation gave a higher yield of ethanol (4.17?×?10^?3 g ethanol g^?1 sugars; 139.12 μg ethanol g^?1 glucose) than R. riparium (0.086?×?10^?3 g ethanol g^?1 sugars; 33.84 μg ethanol g^?1 glucose), U. intestinalis (0.074?×?10^?3 g ethanol g^?1 sugars; 9.98 μg ethanol g^?1 glucose), and G. salicornia (0.031?×?10^?3 g ethanol g^?1 sugars; 1.43 μg ethanol g^?1 glucose).     

Ethanol Production from High-Solid SSCF of Alkaline-Pretreated Corncob Using Recombinant Zymomonas mobilis CP4

In this work, Zymomonas mobilis was genetically improved for pentose utilization to increase the final ethanol concentration. It showed good fermentation ability on both soluble sugar mixture and lignocellulose. Nearly all the glucose and xylose in sugar mixture can be consumed, corresponding to 86 % of theoretic ethanol yield. Simultaneous saccharification and co-fermentation (SSCF) of NaOH-pretreated corncob was then carried out in a high dry matter (DM) loading of 15–25?w/v%. At the DM loading of 15 %, the suitable operating conditions were determined, i.e., Z. mobilis loading of 0.30 g dry weight/L at 30 °C (pH?5.5), under which the ethanol concentration reached 49.2 g/L. Higher final ethanol concentrations were obtained when SSCF was operated at the fed-batch mode. Several amounts of substrate (1 % to 10 %) were added, and the highest final ethanol concentration (60.5 g/L) was obtained at 10 % DM addition.     

Bio-ethanol Production from Green Onion by Yeast in Repeated Batch

Considered to be the cleanest liquid fuel, bio-ethanol can be a reliable alternative to fossil fuels. It is produced by fermentation of sugar components of plant materials. The common onions are considered to be a favorable source of fermentation products as they have high sugar contents as well as contain various nutrients. This study focused on the effective production of ethanol from Green onion (Allium fistulosum L.) by the yeast “Saccharomyces cerevisiae” in repeated batch. The results showed that the total sugar concentration of onion juice was 68.4 g/l. The maximum rate of productivity, ethanol yield and final bio-ethanol percentage was 7 g/l/h (g ethanol per liter of onion juice per hour), 35 g/l (g ethanol per liter of onion juice) and 90 %, respectively.     

Bench-scale bioethanol production from eucalyptus by high solid saccharification and glucose/xylose fermentation method

In the bioethanol production process, high solid saccharification and glucose/xylose co-fermentation are important technologies for obtaining increased ethanol concentrations; however, bench-scale studies using combinations of these methods are limited. In this study, we hydrolyzed high solid concentration of milled eucalyptus using commercial enzymes and obtained 138.4 g/L total monomeric sugar concentration. These sugars were fermented to 53.5 g/L of ethanol by a xylose-utilizing recombinant Saccharomyces cerevisiae strain, MA-R4. These experiments were performed in bench scale (using 50 L scale solid mixer and 70 L scale fermenter). The results obtained in this study were comparable to our previous results in laboratory scale, indicating that we successfully achieved an efficient high solid saccharification and glucose/xylose co-fermentation system in bench scale.     

Pilot-scale production of fuel ethanol from concentrated food waste hydrolysates using Saccharomyces cerevisiae H058

The aim of this study was to develop a bioprocess to produce ethanol from food waste at laboratory, semipilot and pilot scales. Laboratory tests demonstrated that ethanol fermentation with reducing sugar concentration of 200 g/L, inoculum size of 2 % (Initial cell number was 2 × 10⁶ CFU/mL) and addition of YEP (3 g/L of yeast extract and 5 g/L of peptone) was the best choice. The maximum ethanol concentration in laboratory scale (93.86 ± 1.15 g/L) was in satisfactory with semipilot scale (93.79 ± 1.11 g/L), but lower than that (96.46 ± 1.12 g/L) of pilot-scale. Similar ethanol yield and volumetric ethanol productivity of 0.47 ± 0.02 g/g, 1.56 ± 0.03 g/L/h and 0.47 ± 0.03 g/g, 1.56 ± 0.03 g/L/h after 60 h of fermentation in laboratory and semipilot fermentors, respectively, however, both were lower than that (0.48 ± 0.02 g/g, 1.79 ± 0.03 g/L/h) of pilot reactor. In addition, simple models were developed to predict the fermentation kinetics during the scale-up process and they were successfully applied to simulate experimental results.     

Ethanol production from galactose by a newly isolated Saccharomyces cerevisiae KL17

A wild-type yeast strain with a good galactose-utilization efficiency was newly isolated from the soil, and identified and named Saccharomyces cerevisiae KL17 by 18s RNA sequencing. Its performance of producing ethanol from galactose was investigated in flask cultures with media containing various combination and concentrations of galactose and glucose. When the initial galactose concentration was 20 g/L, it showed 2.2 g/L/h of substrate consumption rate and 0.63 g/L/h of ethanol productivity. Although they were about 70 % of those with glucose, such performance of S. cerevisiae KL17 with galactose was considered to be quite high compared with other strains reported to date. Its additional merit was that its galactose metabolism was not repressed by the existence of glucose. Its capability of ethanol production under a high ethanol concentration was demonstrated by fed-batch fermentation in a bioreactor. A high ethanol productivity of 3.03 g/L/h was obtained with an ethanol concentration and yield of 95 and 0.39 g/L, respectively, when the cells were pre-cultured on glucose. When the cells were pre-cultured on galactose instead of glucose, fermentation time could be reduced significantly, resulting in an improved ethanol productivity of 3.46 g/L/h. The inhibitory effects of two major impurities in a crude galactose solution obtained from acid hydrolysis of galactan were assessed. Only 5-Hydroxymethylfurfural (5-HMF) significantly inhibited ethanol fermentation, while levulinic acid (LA) was benign in the range up to 10 g/L.     

深红红螺菌吸氢酶缺失突变株在管式光合反应器中的产氢

本研究设计了一种2 L分体式管式光合反应器, 并研究了深红红螺菌(Rhodospirillum rubrum)吸氢酶缺失突变株在该反应器中分别利用人工光源(持续光照与光暗交替)和自然光的产氢规律。结果表明在人工光照条件下R. rubrum的产氢可维持5 d, 持续光照和光暗交替条件下(12 h: 12 h)的氢产量可分别达到5752 mL/PBR ± 158 mL/PBR和5012 mL/PBR ± 202 mL/PBR; 自然光条件下, 最适产氢光照强度为30000 Lux~40000 Lux; 在此光照条件下, R. rubrum产氢可维持6 d~ 10 d, 最高氢产量可达到2800 mL/PBR。尽管利用自然光的氢产量比利用人工光源氢产量低, 但是利用自然光的产氢比较经济, 并且该光合产氢系统操作简单, 该工艺有望开发为低成本的光合细菌产氢技术。     

Expression of exoinulinase genes in Saccharomyces cerevisiae to improve ethanol production from inulin sources

To improve inulin utilization and ethanol fermentation, exoinulinase genes from the yeast Kluyveromyces marxianus and the recently identified yeast, Candida kutaonensis, were expressed in Saccharomyces cerevisiae. S. cerevisiae harboring the exoinulinase gene from C. kutaonensis gave higher ethanol yield and productivity from both inulin (0.38 vs. 0.34 g/g and 1.35 vs. 1.22 g l^?1 h^?1) and Jerusalem artichoke tuber flour (0.47 vs. 0.46 g/g and 1.62 vs. 1.54 g l^?1 h^?1) compared with the strain expressing the exoinulinase gene from K. marxianus. Thus, the exoinulinase gene from C. kutaonensis is advantageous for engineering S. cerevisiae to improve ethanol fermentation from inulin sources.     

Influence of silicate on enrichment of highly productive microalgae from a mixed culture

Microalgae have the potential to supply a biobased society with essential feedstocks like sugar and lipids. Besides being productive, strains used for this purpose should grow fast, be resistant to predators, and have good harvestability properties. Diatoms, a class of siliceous algae, have these and other preferred characteristics. In this paper, we describe the enrichment of microalgae in sequencing batch reactors with and without supply of silicate. Both reactors were operated with a light–dark cycle. To maximize storage compound production, carbon fixation and nitrogen uptake were uncoupled by limiting the availability of nitrate to the dark phase. After ten cycles, a stable culture was established in both reactors. The diatom Nitzschia sp. dominated the silicate-rich reactor, and the green algae Chlamydomonas sp. dominated the silicate-depleted reactor. Over the remaining 27 cycles of the experiment, the microalgal community structure did not change, indicating a highly stable system. Although the dominant microalga was highly dependent on the presence of silicate, the performance of both microalgal enrichments was similar. Polymers of glucose were stored during the nitrogen-limited light period. On organic matter dry weight basis, the sugar content of the biomass increased during the light period from 17?±?4 to 53?±?4 % for the silicate-limited culture, and from 14?±?4 to 43?±?4 % (w w ^?1) for the silicate excess culture. These results show that storage compound production can be achieved under various conditions, as long as a selective environment is maintained.     

Butanol production by Clostridium acetobutylicum in a continuous packed bed reactor

In this study, we report on a butanol production process by immobilized Clostridium acetobutylicum in a continuous packed bed reactor (PBR) using Tygon^® rings as a carrier. The medium was a solution of lactose (15–30 g/L) and yeast extract (3 g/L) to emulate the cheese whey, an abundant lactose-rich wastewater. The reactor was operated under controlled conditions with respect to the pH and to the dilution rate. The pH and the dilution rate ranged between 4 and 5, the dilution rate between 0.54 and 2.4 h^?1 (2.5 times the maximum specific growth rate assessed for suspended cells). The optimal performance of the reactor was recorded at a dilution rate of 0.97 h^?1: the butanol productivity was 4.4 g/Lh and the selectivity of solvent in butanol was 88%_w.     

High-productivity lipid production using mixed trophic state cultivation of <Emphasis Type="Italic">Auxenochlorella</Emphasis> (<Emphasis Type="Italic">Chlorella</Emphasis>) <Emphasis Type="Italic">protothecoides</Emphasis>

A mixed trophic state production process for algal lipids for use as feedstock for renewable biofuel production was developed and deployed at subpilot scale using a green microalga, Auxenochlorella (Chlorella) protothecoides. The process is composed of two separate stages: (1) the photoautotrophic stage, focused on biomass production in open ponds, and (2) the heterotrophic stage focused on lipid production and accumulation in aerobic bioreactors using fixed carbon substrates (e.g., sugar). The process achieved biomass and lipid productivities of 0.5 and 0.27 g/L/h that were, respectively, over 250 and 670 times higher than those obtained from the photoautotrophic cultivation stage. The biomass oil content (over 60 % w/DCW) following the two-stage process was predominantly monounsaturated fatty acids (~82 %) and largely free of contaminating pigments that is more suitable for biodiesel production than photosynthetically generated lipid. Similar process performances were obtained using cassava hydrolysate as an alternative feedstock to glucose.     

Effects of methanol on cell growth and lipid production from mixotrophic cultivation of Chlorella sp.

The marine microalga Chlorella sp. was cultivated under mixotrophic conditions using methanol as an organic carbon source, which may also act to maintain the sterility of the medium for long-term outdoor cultivation. The optimal methanol concentration was determined to be 1% (v/v) for both cell growth and lipid production when supplying 5% CO₂ with 450 μE/m²/sec of continuous illumination. Under these conditions, the maximal cell biomass and total lipid production were 4.2 g dry wt/L and 17.5% (w/w), respectively, compared to 2.2 g dry wt/L and 12.5% (w/w) from autotrophic growth. Cell growth was inhibited at methanol concentrations above 1% (v/v) due to increased toxicity, whereas 1% methanol alone sustained 1.0 g dry wt/L and 4.8% total lipid production. We found that methanol was preferentially consumed during the initial period of cultivation, and carbon dioxide was consumed when the methanol was depleted. A 12:12 h (light:dark) cyclic illumination period produced favorable cell growth (3.6 g dry wt/L). Higher lipid production was observed with cyclic illumination than with continuous illumination (18.6% (w/w) vs 17.5% (w/w)), and better lipid production was also obtained under mixotrophic rather than autotrophic conditions. Interestingly, under mixotrophic conditions with 12:12 (h) cyclic illumination, high proportions of C_16:0, C_18:0, and C_18:1 were observed, which are beneficial for biodiesel production. These results strongly indicate that the carbon source is important for controlling both lipid composition and cell growth under mixotrophic conditions, and they suggest that methanol could be utilized to scale up production to an open pond type system for outdoor cultivation where light illumination changes periodically.     

Evaluation of hardboard manufacturing process wastewater as a feedstream for ethanol production

Waste streams from the wood processing industry can serve as feedstream for ethanol production from biomass residues. Hardboard manufacturing process wastewater (HPW) was evaluated on the basis of monomeric sugar recovery and fermentability as a novel feedstream for ethanol production. Dilute acid hydrolysis, coupled with concentration of the wastewater resulted in a hydrolysate with 66 g/l total fermentable sugars. As xylose accounted for 53 % of the total sugars, native xylose-fermenting yeasts were evaluated for their ability to produce ethanol from the hydrolysate. The strains selected were, in decreasing order by ethanol yields from xylose (Y _p/s, based on consumed sugars), Scheffersomyces stipitis ATCC 58785 (CBS 6054), Pachysolen tannophilus ATCC 60393, and Kluyveromyces marxianus ATCC 46537. The yeasts were compared on the basis of substrate utilization and ethanol yield during fermentations of the hydrolysate, measured using an HPLC. S. stipitis, P. tannophilus, and K. marxianus produced 0.34, 0.31, and 0.36 g/g, respectively. The yeasts were able to utilize between 58 and 75 % of the available substrate. S. stipitis outperformed the other yeast during the fermentation of the hydrolysate; consuming the highest concentration of available substrate and producing the highest ethanol concentration in 72 h. Due to its high sugar content and low inhibitor levels after hydrolysis, it was concluded that HPW is a suitable feedstream for ethanol production by S. stipitis.