Monitoring microalgal growth of Chlorella minutissima with a new all solid-state contact nitrate selective sensor

As third generation feedstock, microalgae are microorganisms that can grow only in the optimum conditions. There are parameters including the concentration of macro and microelements in nutrient solution, pH, temperature and light intensity that have significant impact on microalgal growth. In recent years, various sensing devices have been developed for sensitive measurement of these parameters during microalgal growth. In this study, a new potentiometric nitrate selective sensor was developed to indicate the nitrate uptake of microalgae and the effect of nitrate nutrient on microalgal growth, specifically, and this sensor was successfully applied to determine nitrate concentration in medium during microalgal growth. Moreover, the effects of nitrate, carbonate and phosphate concentration in the growth medium on biomass production of Chlorella minutissima were investigated by using Box–Behnken design method, and optimum conditions were determined for the highest biomass production of microalgae. As a result of the experiments, it was seen that the highest C. minutissima production was achieved using the medium consist of 2.63 g/L NaNO₃, 0.35 g/L Na₂CO₃ and 0.4 g/L KH₂PO_4. Statistically, it was observed that there was a proportional relationship between the microalgae production and investigated parameters such as carbon, nitrogen and phosphate amounts of culture mediums. The electrode showed a wide linear range between 1.0 × 10⁻¹ and 5.0 × 10⁻⁵ M with a detection limit of the 5 × 10⁻⁶ M and the response time was found as 10 s. The results showed that developed nitrate selective sensor could be successfully applied for continuous measurement of nitrate in microalgal productions at reduced cost.     

Fed-batch culture of Escherichia coli for L-valine production based on in silico flux response analysis

We have previously reported the development of a 100% genetically defined engineered Escherichia coli strain capable of producing L ‐valine from glucose with a high yield of 0.38 g L ‐valine per gram glucose (0.58 mol L ‐valine per mol glucose) by batch culture. Here we report a systems biological strategy of employing flux response analysis in bioprocess development using L ‐valine production by fed‐batch culture as an example. Through the systems‐level analysis, the source of ATP was found to be important for efficient L ‐valine production. There existed a trade‐off between L ‐valine production and biomass formation, which was optimized for the most efficient L ‐valine production. Furthermore, acetic acid feeding strategy was optimized based on flux response analysis. The final fed‐batch cultivation strategy allowed production of 32.3 g/L L ‐valine, the highest concentration reported for E. coli. This approach of employing systems‐level analysis of metabolic fluxes in developing fed‐batch cultivation strategy would also be applicable in developing strategies for the efficient production of other bioproducts. Biotechnol. Bioeng. 2011; 108:934–946. © 2010 Wiley Periodicals, Inc.     

Co-production of lactic acid and chitin using a pelletized filamentous fungus Rhizopus oryzae cultured on cull potatoes and glucose

Aims: This paper developed a novel process for lactic acid and chitin co-production of the pelletized Rhzious oryzae NRRL 395 fermentation using underutilized cull potatoes and glucose as nutrient source. Methods and Results: Whole potato hydrolysate medium was first used to produce the highest pelletized biomass yield accompanying the highest chitin content in biomass. An enhanced lactic acid production then followed up using batch, repeated batch and fed batch culture with glucose as carbon source and mixture of ammonia and sodium hydroxide as neutralizer. The lactic acid productivity peaked at 2·8 and 3 g l⁻¹ h⁻¹ in repeated batch culture and batch culture, respectively. The fed batch culture had the highest lactate concentration of 140 g l⁻¹. Conclusions: Separation of the biomass cultivation and the lactic acid production is able to not only improve lactic acid production, but also enhance the chitin content. Cull potato hydrolysate used as a nutrient source for biomass cultivation can significantly increase both biomass yield and chitin content. Significance and Impact of the Study: The three-step process using pelletized R. oryzae fermentation innovatively integrates utilization of agricultural residues into the process of co-producing lactic acid and chitin, so as to improve the efficiency, revenues and cost of fungal lactic acid production.     

Biomass and lipid production of heterotrophic microalgae <Emphasis Type="Italic">Chlorella protothecoides</Emphasis> by using biodiesel-derived crude glycerol

Microalgal lipids may be a more sustainable biodiesel feedstock than crop oils. We have investigated the potential for using the crude glycerol as a carbon substrate. In batch mode, the biomass and lipid concentration of Chlorella protothecoides cultivated in a crude glycerol medium were, respectively, 23.5 and 14.6 g/l in a 6-day cultivation. In the fed-batch mode, the biomass and lipid concentration improved to 45.2 and 24.6 g/l after 8.2 days of cultivation, respectively. The maximum lipid productivity of 3 g/l day in the fed-batch mode was higher than that produced by batch cultivation. This work demonstrates the feasibility of crude biodiesel glycerol as an alternative carbon substrate to glucose for microalgal cultivation and a cost reduction of carbon substrate feed in microalgal lipid production may be expected.     

布朗葡萄藻的培养基选择及其产物代谢规律

通过对布朗葡萄藻分别在Chu13、Chu13×2和BG-11培养基中培养结果的比较,发现在气升式光照生物反应器中Chu13培养基最有利于布朗葡萄藻的生长和烃的合成,培养15d后,其生物量和粗烃质量分数分别为1.82g/L和58.7%;棕榈酸、油酸和亚麻酸是布朗葡萄藻的主要脂肪酸组成,Chu13培养获得的藻体不饱和脂肪酸比例最高。Chu13培养基中布朗葡萄藻代谢规律的研究表明:粗烃含量随着生物量的增加而逐渐增大,15d后粗烃产量达到最大值1.07g/L,不同生长周期烃的组成保持一致,布朗葡萄藻的烃主要由C33H56和C34H58组成;在布朗葡萄藻生长周期中,不饱和脂肪酸的比例显著上升,培养15d达到64%以上。     

Hydrocarbon production from secondarily treated piggery wastewater by the green alga Botryococcus braunii

A laboratory study was conducted on the removal of nitrogen and phosphorus from piggery wastewater during growth of Botryococcus braunii UTEX 572, together with measurements of hydrocarbon formation by the alga. The influence was tested of the initial nitrogen and phosphorus concentration on the optimum concentration range for a culture in secondarily treated piggery wastewater. A high cell density (> 7 g L^–1 d. wt) was obtained with 510 mg L^–1 NO₃-N. Growth increased with nitrogen concentration at the basal phosphorus concentration (14 mg P L^–1). The growth rate was nearly independent ( = 0.027 0.030 h^–1) of the initial phosphate concentration, except under conditions of phosphate deficiency ( = 0.019 h^–1). B. braunii grew well in piggery wastewater pretreated by a membrane bioreactor (MBR) with acidogenic fermentation. A dry cell weight of 8.5 mgL^–1 and hydrocarbon level of 0.95 gL^–1 were obtained, and nitrate was removed at a rate of 620 mg NL^–1. These results indicate that pretreated piggery wastewater provides a good culture medium for the growth and hydrocarbon production by B. braunii.     

Toxicity and bioremediation of As(III) and As(V) in the green microalgae Botryococcus braunii: A laboratory study

Worldwide threats of fuel shortages in the near future and climate change because of greenhouse gas emissions are posing severe challenges and therefore it is vital to search for sustainable ways of preventing the consequences. The dual use of microalgae for phycoremediation and biomass production for sustainable biofuel production is a viable choice. Phycoremediation of As(III) and As(V) ions using microalgae was investigated in a two-staged batch reactor. Accumulation and toxicity of inorganic arsenic forms (As(III) and As(V)) to green microalgae Botryococcus braunii depend on environmental factors. Dissolved oxygen and pH cycles did not significantly differ due to the absence or presence of arsenic (either As(III) or As(V)) ions in the culture. Monod model was utilized for representing the growth kinetics of microalgae in pure media containing various concentrations of nitrate ions. Maximum specific growth rate and saturation constant were found to be 0.14788 d^?1 and 0.00105 g/L, respectively. With the increase in concentration of phosphate in growth medium, the growth of microalgae increased. Media with NaCl (1.0 g/L) and NaHCO₃ (1 g/L) resulted in higher maximum biomass concentration. Effect of coexisting ions on phycoremediation of As(III) and As(V) ions using microalgae was studied.     

搅拌式光生物反应器培养海带配子体细胞：不同脉冲补料方式的研究

本文以批次培养为对照,研究了七种脉冲补料方式对搅拌式光生物反应器中培养大型褐藻海带配子体细胞生长和培养液内氮磷营养盐消耗的影响,并首次探讨了脉冲补料方式下不同补料时间点和补料量的影响作用。培养条件设定为50 mg DCW (细胞干重) L-1接种密度、培养液为改良的APSW人工海水、光强60 µE m-2 s-1、光周期16/8 h L/D、通气速率和搅拌速率分别为50 mL min-1和100 rpm。结果表明少量补料利于细胞对氮磷的协同吸收,进而利于生物量扩增。当培养液内氮磷富足或耗尽时补料对于生物量大量生产效果甚微,可能由于氮磷吸收变缓、其储存现象显著,或是其吸收协同性降低。文中当细胞生长至对数中期开始频繁补加少量氮磷营养盐,即维持培养液内氮磷浓度在各自起始浓度的1/3至1/2之间,对生物量生产最有效,生物量增长倍数高达12.270倍。     

Improvement of both lipid and biomass productivities of Qatar Chlorocystis isolate for biodiesel production and food security

Microalgae are considered a very promising alternative for biofuel production. Several strategies were developed to modulate and improve algae metabolites production to meet the requirements for biodiesel production. Most previous research evidenced that the increase of the lipid content is accompanied by a decrease of the biomass production, which increases the cost of the downstream processing. Hence, the challenge is to find special culture conditions that increase the lipid and the biomass productivities simultaneously. In the present work, we developed a strategy for the improvement of biomass and lipid productivities in a novel local microalga isolate, Chlorocystis sp. QUCCCM14, which was not previously known as a promising strain. Indeed, culturing QUCCCM14 using f/2 medium with 10× NaH₂PO₄ (0.15 g L^?1 NaNO₃ and 5.6 mg L^?1 NaH₂PO₄) resulted in an improvement of 3.178 folds the lipid productivity reaching 56.121 mg L^?1 day^?1 and enhanced the biomass productivity reaching 141.363 mg L^?1 day^?1, simultaneously. Comparative analyses of the FAME profiles demonstrated that fed‐batch culture with phosphate or nitrate separately leads to a high production of the omega 3 fatty acids (Linolenic acid), whereas fed‐batch culture with phosphate and nitrate simultaneously increased the production of fatty acids suitable for biodiesel production.     

Statistical optimization of culture media for growth and lipid production of <Emphasis Type="Italic">Botryococcus braunii</Emphasis> LB572

Botryococcus braunii has an outstanding ability to produce lipid; however, it is a slow-growing green microalgae. Statistical optimization of growth media was performed to faster growth and to increase lipid concentration. The effect of media composition on the growth of B. braunii LB572 was examined using fractional factorial design and central composite design. The media components examined include sodium carbonate, potassium phosphate, calcium chloride, magnesium sulfate, ferric citrate, and sodium nitrate. The results indicated that potassium phosphate and magnesium sulfate were major impact factors. The optimum concentrations of potassium phosphate and magnesium sulphate were found to be 0.058 and 0.09 g/L, respectively, for growth and 0.083 and 0.1 g/L, respectively, for lipid production. These values were validated using bubble column photobioreactors. Lipid productivity increased to 0.19 g/L/day in lipid-optimized media, with an average biomass productivity of 0.296 g/L/day and 64.96% w/w. In growth-optimized media, lipid productivity was 0.18 g/L/day, with an average biomass productivity of 0.304 g/L/day and 59.56% w/w.     

Biosensor online control of citric acid production from glucose by Yarrowia lipolytica using semicontinuous fermentation

Our study aimed at the development of an effective method for citric acid production from glucose by use of the yeast Yarrowia lipolytica. The new method included an automated bioprocess control using a glucose biosensor. Several fermentation methodologies including batch, fed‐batch, repeated batch and repeated fed‐batch cultivation were tested. The best results were achieved during repeated fed‐batch cultivation: Within 3 days of cycle duration, approximately 100 g/L citric acid were produced. The yields reached values between 0.51 and 0.65 g/g and the selectivity of the bioprocess for citric acid was as high as 94%. Due to the elongation of the production phase of the bioprocess with growth‐decoupled citric acid production, and by operating the fermentation in cycles, an increase in citric acid production of 32% was achieved compared with simple batch fermentation.     

Growth of the hydrocarbon-rich microalga Botryococcus braunii in secondarily treated sewage

Summary A hydrocarbon-rich green microalga, Botryococcus braunii, was able to grow well in secondarily treated sewage (STS) from domestic waste-water in a batch system. The growth in STS from domestic waste-water was as good as in the common artificial medium of modified Chu 13 and its hydrocarbon contents were high enough at 53% and 40% compared with 58% in the case of the modified Chu 13 medium. B. braunii utilized nitrate from 7.67 or 4.48 mg/l to a level below detection of < 0.01 mg/l in STS. After this consumption of nitrate, nitrite was consumed, and ammonium was not. Phosphate, even at an extremely low concentration, was also consumed by B. braunii. These results show the possibility of using STS as a medium to grow B. braunii and for removal of nitrogen and phosphorus by algal consumption in STS.Correspondence to: S. Yokoyama     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

β‐poly(l‐malic acid) production by fed‐batch culture of Aureobasidium pullulans ipe‐1 with mixed sugars

β‐poly(l ‐malic acid) (PMLA) is a biopolyester, which has attracted growing attention due to its potential applications in medicine and other industries. In this study, the biosynthetic pathway of PMLA and the fermentation strategies with mixed sugars were both investigated to enhance PMLA production by Aureobasidium pullulans ipe‐1. Metabolic intermediates and inhibitors were used to study the biosynthetic pathway of PMLA. It showed that exogenous addition of l ‐malic acid, succinic acid, TFA, and avidin had negligible effect on PMLA production, while pyruvic acid and biotin were the inhibitors, indicating that PMLA biosynthesis was probably related to phosphoenolpyruvate via oxaloacetate catalyzed by phosphoenolpyruvate carboxylase. Sucrose was suitable for achieving the highest PMLA concentration, while fructose generated a higher yield of PMLA (PMLA produced per biomass). Furthermore, the fed‐batch culture using fed solution with different sugar mixture for PMLA production was implemented. During the fed‐batch culture with mixed solution, fructose could increase PMLA production. Compared with the batch culture, the feeding with mixed sugar (sucrose and glucose) increased PMLA concentration by 23.9%, up to 63.2 g/L, and the final volume of the broth was increased by 25%. These results provide a good reference for process development and optimization of PMLA production.     

Simultaneous use of sodium nitrate and urea as nitrogen sources improves biomass composition of Arthrospira platensis cultivated in a tubular photobioreactor

Arthrospira platensis is widely cultivated in open ponds for industrial purposes. However, high‐protein A. platensis biomass produced in photobioreactors (PBRs) is recommended for pharmaceutical and cosmetic formulations. A. platensis was cultivated in a 3.5 L tubular airlift PBR using both sodium nitrate and urea as nitrogen sources. Sodium nitrate was added from the start of the cultivation using a batch process. Urea was supplied daily at exponentially increasing feeding rate using a fed‐batch process. The simultaneous optimization of the independent variables, namely, total quantity of sodium nitrate (m_T1) and total quantity of urea (m_T2), led to an optimal condition of m_T1 = 15.0 mmol/L and m_T2 = 7.5 mmol/L. Maximum biomass concentration (5183 ± 94 mg/L) corresponding to the highest biomass productivity (683 ± 13 mg/L/day) was obtained under such condition. The addition protocol of both nitrogen sources resulted in high productivities of protein (6.2 ± 0.4 mg/L/day) as well as chlorophyll‐a (372.2 ± 7.7 mg/L/day). Such innovative process could be applied in the large‐scale production of A. platensis using tubular PBR for novel applications.     

Heterotrophic production of Chlorella sp. TISTR 8990—biomass growth and composition under various production conditions

The green microalga Chlorella sp. TISTR 8990 was grown heterotrophically in the dark using various concentrations of a basal glucose medium with a carbon‐to‐nitrogen mass ratio of 29:1. The final biomass concentration and the rate of growth were highest in the fivefold concentrated basal glucose medium (25 g L^?1 glucose, 2.5 g L^?1 KNO₃) in batch operations. Improving oxygen transfer in the culture by increasing the agitation rate and decreasing the culture volume in 500‐mL shake flasks improved growth and glucose utilization. A maximum biomass concentration of nearly 12 g L^?1 was obtained within 4 days at 300 rpm, 30°C, with a glucose utilization of nearly 76% in batch culture. The total fatty acid (TFA) content of the biomass and the TFA productivity were 102 mg g^?1 and 305 mg L^?1 day^?1, respectively. A repeated fed‐batch culture with four cycles of feeding with the fivefold concentrated medium in a 3‐L bioreactor was evaluated for biomass production. The total culture period was 11 days. A maximum biomass concentration of nearly 26 g L^?1 was obtained with a TFA productivity of 223 mg L^?1 day^?1. The final biomass contained (w/w) 13.5% lipids, 20.8% protein and 17.2% starch. Of the fatty acids produced, 52% (w/w) were saturated, 41% were monounsaturated and 7% were polyunsaturated (PUFA). A low content of PUFA in TFA feedstock is required for producing high quality biodiesel. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1589–1600, 2017     

A simple and rapid harvesting method for microalgae by in situ magnetic separation

A simple and rapid harvesting method by in situ magnetic separation with naked Fe₃O₄ nanoparticles has been developed for the microalgal recovery of Botryococcus braunii and Chlorella ellipsoidea. After adding the magnetic particles to the microalgal culture broth, the microalgal cells were adsorbed and then separated by an external magnetic field. The maximal recovery efficiency reached more than 98% for both microalgae at a stirring speed of 120 r/min within 1 min, and the maximal adsorption capacity of these Fe₃O₄ nanoparticles reached 55.9 mg-dry biomass/mg-particles for B. braunii and 5.83 mg-dry biomass/mg-particles for C. ellipsoidea. Appropriate pH value and high nanoparticle dose were favorable to the microalgae recovery, and the adsorption mechanism between the naked Fe₃O₄ nanoparticles and the microalgal cells was mainly due to the electrostatic attraction. The developed in situ magnetic separation technology provides a great potential for saving time and energy associated with improving microalgal harvesting.     

Echinenone production of a dark red-coloured strain of Botryococcus braunii

Echinenone has been used as an edible orange pigment, antioxidant and provitamin A. An echinenone-accumulating strain, BOT-20, of Botryococcus braunii was isolated from freshwater environments in Japan. The B. braunii BOT-20 strain is different from other strains of B. braunii, as it appeared dark red during its growth in the laboratory culture as opposed to green. The biomass of the strain was 1.9?g?L^?1 at 1?month after cultivation. The n-hexane/acetone (3:1, v/v) extract of the strain was 45.5% of the dry biomass weight and consisted of carotenoids (92%, of which 73% was echinenone) and hydrocarbons (8%). The echinenone content was 30.5% of the dry biomass weight, and production was 630?mg?L^?1. Hydrocarbons comprised only 3.7% of the total dry biomass weight. The main component of hydrocarbon was an analogue of botryococene by ¹H and ¹³C NMR. With high values of echinenone content and production, the B. braunii strain BOT-20 is expected to be a new bioresource for the commercial production of echinenone.     

Biological pretreatment of corn stover with Phlebia brevispora NRRL‐13108 for enhanced enzymatic hydrolysis and efficient ethanol production

Biological pretreatment of lignocellulosic biomass by white‐rot fungus can represent a low‐cost and eco‐friendly alternative to harsh physical, chemical, or physico‐chemical pretreatment methods to facilitate enzymatic hydrolysis. In this work, solid‐state cultivation of corn stover with Phlebia brevispora NRRL‐13018 was optimized with respect to duration, moisture content and inoculum size. Changes in composition of pretreated corn stover and its susceptibility to enzymatic hydrolysis were analyzed. About 84% moisture and 42 days incubation at 28°C were found to be optimal for pretreatment with respect to enzymatic saccharification. Inoculum size had little effect compared to moisture level. Ergosterol data shows continued growth of the fungus studied up to 57 days. No furfural and hydroxymethyl furfural were produced. The total sugar yield was 442 ± 5 mg/g of pretreated corn stover. About 36 ± 0.6 g ethanol was produced from 150 g pretreated stover per L by fed‐batch simultaneous saccharification and fermentation (SSF) using mixed sugar utilizing ethanologenic recombinant Eschericia coli FBR5 strain. The ethanol yields were 32.0 ± 0.2 and 38.0 ± 0.2 g from 200 g pretreated corn stover per L by fed‐batch SSF using Saccharomyces cerevisiae D5A and xylose utilizing recombinant S. cerevisiae YRH400 strain, respectively. This research demonstrates that P. brevispora NRRL‐13018 has potential to be used for biological pretreatment of lignocellulosic biomass. This is the first report on the production of ethanol from P. brevispora pretreated corn stover. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:365–374, 2017     

Rosmarinic acid production by Lavandula vera MM cell-suspension culture

The time courses of growth and rosmarinic acid production by Lavandula vera MM cell suspension were investigated. The uptake of the main nutrients (sucrose, nitrogen, phosphorus, K, Ca, Mg) was followed during cultivation and the data on the physiology of the L. vera MM cell culture are presented. It was established that the cell culture synthesizes rosmarinic acid during the linear phase of growth for a relatively short period (between the 4th and 8th days of cultivation). The influence of sucrose concentration in the nutrient medium on cell growth and accumulation of rosmarinic acid by L. vera MM cell culture was investigated. The results showed that 7% sucrose in the nutrient medium ensured a steady growth of the cell suspension and increased the yield of rosmarinic acid (29.2 g/l dry biomass and 507.5 mg/l rosmarinic acid compared to 13.0 g/l dry biomass and 68.6 mg/l rosmarinic acid for the control cultivation with 3% sucrose). Received: 17 September 1996 / Received revision: 31 January 1997 / Accepted: 1 February 1997