Multi-Product Microalgae Biorefineries: From Concept Towards Reality.

Although microalgae are a promising biobased feedstock, industrial scale production is still far off. To enhance the economic viability of large-scale microalgae processes, all biomass components need to be valorized, requiring a multi-product biorefinery. However, this concept is still too expensive. Typically, downstream processing of industrial biotechnological bulk products accounts for 20-40% of the total production costs, while for a microalgae multi-product biorefinery the costs are substantially higher (50-60%). These costs are high due to the lack of appropriate and mild technologies to access the different product fractions such as proteins, carbohydrates, and lipids. To reduce the costs, simplified processes need to be developed for the main unit operations including harvesting, cell disruption, extraction, and possibly fractionation.

The impact of centralization of services on treatment delay in ovarian cancer: A study on process quality.

OBJECTIVE: Emphasis on improving healthcare quality has led to centralization of services for patients suspected of ovarian cancer. As centralization of services may induce treatment delays, we aimed to assess compliance with health system interval guidelines in patients suspected of ovarian cancer. DESIGN: Evaluation of health system intervals, comparison between direct and indirect referrals and between 2013 and 2014. SETTING: A managed clinical network (MCN) comprising 11 hospitals in the Netherlands. PARTICIPANTS: Patients that were treated for ovarian cancer within the University Medical Center Groningen in 2013 and 2014. INTERVENTION: Introduction of an MCN to centralize services for patients suspected of ovarian cancer. MAIN OUTCOME MEASURE: Compliance with national guidelines regarding health system intervals. RESULTS: Between 2013 and 2014 a clinically relevant improvement in compliance with guidelines was demonstrated. Within this period, median treatment intervals decreased from 34 to 29 days, and the percentage of patients in which treatment interval guidelines were met increased from 63.5 to 72.2%. New regulations and increased awareness of health system intervals inspired changes in local practice leading to improved compliance with guidelines. Compliance was highest in patients that were directly referred to our academic hospital. CONCLUSION: Evaluation of health system intervals in patients suspected of ovarian cancer was feasible and may be applicable to other MCNs. Though compliance with guidelines improved within the study period, there is potential for improvement. To facilitate real-time evaluation of compliance with national guidelines establishing uniformity of electronic patient files in the MCN is deemed essential.

Understanding the salinity effect on cationic polymers in inducing flocculation of the microalga Neochloris oleoabundans.

A mechanistic study was performed to evaluate the effect of salinity on cationic polymeric flocculants, that are used for the harvesting of microalgae. The polyacrylamide Synthofloc 5080H and the polysaccharide Chitosan were employed for the flocculation of Neochloris oleoabundans. In seawater conditions, a maximum biomass recovery of 66% was obtained with a dosage of 90mg/L Chitosan. This recovery was approximately 25% lower compared to Synthofloc 5080H reaching recoveries greater than 90% with dosages of 30mg/L. Although different recoveries were obtained with both flocculants, the polymers exhibit a similar apparent polymer length, as was evaluated from viscosity measurements. While both flocculants exhibit similar polymer lengths in increasing salinity, the zeta potential differs. This indicates that polymeric charge dominates flocculation. With increased salinity, the effectivity of cationic polymeric flocculants decreases due to a reduction in cationic charge. This mechanism was confirmed through a SEM analysis and additional experiments using flocculants with various charge densities.

Dosage effect of cationic polymers on the flocculation efficiency of the marine microalga Neochloris oleoabundans.

A mechanistic mathematical model was developed to predict the performance of cationic polymers for flocculating salt water cultivated microalgae. The model was validated on experiments carried out with Neochloris oleoabundans and three different commercial flocculants (Zetag 7557®, Synthofloc 5080H® and SNF H536®). For a wide range of biomass concentrations (0.49-1.37 g L(-1)) and flocculant dosages (0-150 mg L(-1)) the model simulations predicted well the optimal flocculant-to-biomass ratio between 43 and 109 mgflocculant/gbiomass. At optimum conditions biomass recoveries varied between 88% and 99%. The cost of the usage of commercial available flocculants is estimated to range between 0.15$/kgbiomass and 0.49$/kgbiomass.

Cationic polymers for successful flocculation of marine microalgae.

Flocculation of microalgae is a promising technique to reduce the costs and energy required for harvesting microalgae. Harvesting marine microalgae requires suitable flocculants to induce the flocculation under marine conditions. This study demonstrates that cationic polymeric flocculants can be used to harvest marine microalgae. Different organic flocculants were tested to flocculate Phaeodactylum tricornutum and Neochloris oleoabundans grown under marine conditions. Addition of 10 ppm of the commercial available flocculants Zetag 7557 and Synthofloc 5080H to P. tricornutum showed a recovery of, respectively, 98% ± 2.0 and 94% ± 2.9 after flocculation followed by 2h sedimentation. Using the same flocculants and dosage for harvesting N. oleoabundans resulted in a recovery of 52% ± 1.5 and 36% ± 11.3. This study shows that cationic polymeric flocculants are a viable option to pre-concentrate marine cultivated microalgae via flocculation prior to further dewatering.

Mechanism behind autoflocculation of unicellular green microalgae Ettlia texensis.

The oleaginous Ettlia texensis is an autoflocculating green microalga that can be used for bio-flocculation of other microalgae species to facilitate harvesting. In this study the mechanism behind autoflocculation of E. texensis was revealed by scanning electron microscopy (SEM) analysis and by characterisation of the cell surface properties. SEM analysis and measurement of extracellular polymeric substances (EPS) showed that autoflocculation of E. texensis is due to the EPS containing mainly glycoproteins patched to the cell surface. Despite the presence of charged groups on the cell surface, they do not seem to attribute to autoflocculation of E. texensis. During bio-flocculation of E. texensis with Chlorella vulgaris EPS structures between both microalgal species were observed. EPS thus not only play a predominant role in autoflocculation of E. texensis but also in bio-flocculation when using this microalga to harvest others.

Modeling microalgal flocculation and sedimentation.

In this study, a combined flocculation and sedimentation model is developed. The model predicts the time needed to reach a desired concentration of microalgal suspension in a sedimentation tank. The concentration of the particles as function of the time and the position in the tank is described. The model was validated with experimental data for Ettlia texensis. The concentration changes measured in time at different heights in the sedimentation vessel corresponded well with model predictions. The model predicts that it takes 25 h to reach a final concentration of 5.2 gDW L(-1), when the initial concentration is 0.26 gDW L(-1) and the tank height is 1m. This example illustrates the use of this model for the design of the settling tank needed for pre-concentration of microalgal biomass before further dewatering.

Effect of growth phase on harvesting characteristics, autoflocculation and lipid content of Ettlia texensis for microalgal biodiesel production.

The effect of growth phase on the recovery of the autoflocculating microalgae Ettlia texensis was studied. In the stationary phase, 90% recovery was achieved after 3h settling. Scanning electron microscopic pictures revealed that extracellular polymeric substances (EPS) on the cell surface were involved in autoflocculation. During the stationary phase an increase of the protein fraction in the EPS was observed while the total fatty acids content increased. The autoflocculating properties of E. texensis combined with favourite fatty acid content and composition make this microalgae an excellent candidate for biodiesel production if harvested at the end of the stationary phase.

Ratio between autoflocculating and target microalgae affects the energy-efficient harvesting by bio-flocculation.

The effect of ratio between autoflocculating and target microalgae in bio-flocculation was studied with emphasis on the recovery, sedimentation rate and energy demand for harvesting the target microalgae. When the autoflocculating microalgae Ettlia texensis, Ankistrodesmus falcatus and Scenedesmus obliquus were added to Chlorella vulgaris at a ratio of 0.25, the recovery of C. vulgaris increased from 25% to, respectively, 40%, 36% and 31%. The sedimentation rate increased as well. Addition of Tetraselmis suecica to Neochloris oleoabundans at a ratio of 0.25 increased the recovery from 40% to 50%. Application of bio-flocculation at a ratio of 0.25, followed by centrifugation reduces the energy demand for harvesting of the target microalgae from 13.8 MJ kgDW(-1) if only centrifugation is used to 1.83, 1.81, 1.53 and 1.34 MJ kgDW(-1), respectively, using T. suecica, E. texensis, A. falcatus and S. obliquus and 3h sedimentation before centrifugation.

Growth inhibition of Monodus subterraneus by free fatty acids.

Monodus subterraneus is a microalga, which is known for its high eicosapentaenoic acid (EPA; 20:5omega3) content. To produce EPA commercially, high volumetric productivities of microalgae are required. These high productivities can be reached in flat panel photobioreactors with small optical paths that have to be operated at high cell densities (>10 g/L). However, at these cell densities a reduction of productivity is observed. This growth inhibition is probably caused by growth inhibitors released by the microalgae, which have been suggested to be fatty acids. Our aim was to investigate if free fatty acids produced by M. subterraneus inhibited growth of this species. Therefore a bioassay was developed and saturated, unsaturated and poly-unsaturated fatty acids occurring in Monodus were tested on their growth inhibiting properties. Growth of M. subterraneus was completely inhibited at a saturated concentration (96 microM) of palmitoleic acid (16:1omega7). But, the saturated fatty acid palmitic acid (16:0) and the mono-saturated oleic acid (18:1omega9) were much stronger inhibitors. Growth was inhibited for 50% already at concentrations of 0.4 microM 16:0 and 3 microM 18:1omega9, respectively. These fatty acids probably cause the growth inhibition in high cell density cultures of M. subterraneus.

Selective extraction of carotenoids from the microalga Dunaliella salina with retention of viability.

Simultaneous production and selective extraction of beta-carotene from living cells of Dunaliella salina in a two-phase system of aqueous and organic phases has been investigated. Solvents with values of log P(octanol), which denotes hydrophobicity of a compound, ranging from 3 to 9 were used as organic phase. Viability and activity of Dunaliella salina in the presence of organic solvents were checked by microscopic observation and photosynthetic oxygen-production-rate measurements, respectively. Extraction ability of different solvents for both beta-carotene and chlorophyll was determined spectrophotometrically. In addition, beta-carotene contents of the cells growing in the aqueous phase and extracted beta-carotene by the different organic phases were quantified by the same method. Results showed that solvents having log P(octanol) > 6 can be considered biocompatible for this alga. Moreover, pigment extraction ability of a solvent is inversely dependent on its log P(octanol) value. By increasing the degenerative hydrophobicity the extraction ability for both chlorophyll and beta-carotene, decreases. However, this decrease is more profound for chlorophyll. Therefore, selective extraction of beta-carotene becomes feasible. Comparison of the total beta-carotene produced in the presence and in the absence of solvents shows that the presence of a second phase of biocompatible solvents in the culture media may induce the beta-carotene production pathway. The beta-carotene productivity per cell in a two-phase system with dodecane was the highest observed. Extraction ability of the biocompatible solvents dodecane, tetradecan, and hexadecane was similar.

Toxicity of homologous series of organic solvents for the gram-positive bacteria Arthrobacter and Nocardia Sp. and the gram-negative bacteria Acinetobacter and Pseudomonas Sp.

The toxicity of homologous series of organic solvents has been investigated for the gram-positive bacteria, Arthrobacter sp. and Nocardia sp., and the gram-negative bacteria, Acinetobacter sp. and Pseudomonas sp. The hydrophobicity of the solvent, expressed by its logP(octanol), proves to be a good measure for the toxicity of solvents in a two-phase system. The transition from toxic to nontoxic solvents occurs between logP(octanol) 3 and 5 and depends on the homologous series. No correlation has been found between the hydrophobicity of the substituent on the alkyl backbone of the solvent and the location of the transition point in toxicity. The logP(octanol), above which all solvents are nontoxic, is used to express the solvent tolerance of the bacteria. In general, the solvent tolerance of gram-negative bacteria is found to be slightly higher than that of gram-positive bacteria, but this does not hold for all homologous series of organic solvents investigated.Because the toxicity effects of organic solvents in a two-phase system can be ascribed to molecular as well as phase toxicity effects, molecular toxicity effects were investigated separately in a one-phase system with subsaturating amounts of organic solvent. The solvent concentration in the aqueous phase, at which 50% of the metabolic activity of the bacteria is lost, is used to express solvent toxicity. This concentration is found to be similar for the gram-positive Arthrobacter and the gram-negative Acinetobacter. Assuming the critical membrane concentration theory (G. J. Osborne et al. Enzyme Microb. Technol. 1990, 12: 281-291) to be valid, it can be concluded that differences in solvent tolerance between these two bacteria, cannot be ascribed to differences in response to molecular toxicity. Prediction of the toxicity of any solvent, using the critical membrane theory, appears to be possible in the case of alkanols or alkyl acetates. However, prediction of the toxicity of ethers appears to be impossible.

Purification and some properties of a thermostable DNA polymerase from a Thermotoga species.

A stable DNA polymerase (EC 2.7.7.7) has been purified from the extremely thermophilic eubacterium Thermotoga sp. strain FjSS3-B.1 by a five-step purification procedure. First, the crude extract was treated with polyethylenimine to precipitate nucleic acids. The endonuclease activity coprecipitated. DEAE-Sepharose, CM-Sephrarose, and hydroxylapatite column chromatography were used to purify the preparation. As a final step on a small scale, preparative sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis was used. The purified DNA polymerase exhibited a molecular weight of 85,000, as determined by both SDS-polyacrylamide gel electrophoresis and size-exclusion chromatography. Its pH optimum was in the range pH 7.5-8. When assayed over the temperature range 30-80 degrees C, the maximum activity in a 30-min assay was at 80 degrees C. The enzyme was moderately thermostable and exhibited half-lives of 3 min at 95 degrees C and 60 min at 50 degrees C in the absence of substrate. Several additives such as Triton X-100 enhanced thermostability. During storage at 4 degrees C and -70 degrees C, the stability of the enzyme was improved by the addition of gelatin.

Description of enzyme kinetics in reversed micelles. 1. Theory.

In the literature measurements of kinetic data of enzymes in reversed micelles have been interpreted in two ways. In the first, all enzyme parameters are expressed with respect to the total volume of the reversed micellar solution. In the second, the enzymatic conversion is related only to the fraction of the volume consisting of aqueous solution (pseudophase model). In this paper equations are derived describing the rate of an enzymatic reaction for three different kinds of enzymes: enzymes obeying Michaelis-Menten kinetics, enzymes following a ping-pong bi-bi mechanism and enzymes which convert substrates according to an ordered mechanism. In deriving these equations, a distinction is made between intermicellar exchange reactions of substrate(s) and product(s) and the enzymatic reaction which takes place in the waterpool of a reversed micelle. In the description, all intrinsic rate constants of the enzyme are assumed to be independent of its environment. The rate equations show that the presence and efficiency of the intermicellar exchange reaction, which supplies the enzyme with substrate and removes product, can affect the rate of an enzymatic reaction under common experimental conditions. Whereas kinetic parameters derived from double-reciprocal plots often seem to be affected by enclosure in reversed micelles, these apparent deviations from kinetics in aqueous media can be explained by the model presented here as arising from exchange phenomena. Neither the experimentally determined maximum enzyme velocity, vmax, nor the Michaelis constants are affected by the incorporation of the enzyme in reversed micelles. The deviations of kinetic parameters from the aqueous values are shown to depend strongly on the concentration of reversed micelles, the intermicellar exchange rate and the volume fraction of water, a dependence in agreement with findings reported in the literature.