High quality biodiesel production from a microalga Chlorella protothecoides by heterotrophic growth in fermenters

The aim of the study was to obtain high quality biodiesel production from a microalga Chlorella protothecoids through the technology of transesterification. The technique of metabolic controlling through heterotrophic growth of C. protothecoides was applied, and the heterotrophic C. protothecoides contained the crude lipid content of 55.2%. To increase the biomass and reduce the cost of alga, corn powder hydrolysate instead of glucose was used as organic carbon source in heterotrophic culture medium in fermenters. The result showed that cell density significantly increased under the heterotrophic condition, and the highest cell concentration reached 15.5 g L(-1). Large amount of microalgal oil was efficiently extracted from the heterotrophic cells by using n-hexane, and then transmuted into biodiesel by acidic transesterification. The biodiesel was characterized by a high heating value of 41 MJ kg(-1), a density of 0.864 kg L(-1), and a viscosity of 5.2 x 10(-4) Pa s (at 40 degrees C). The method has great potential in the industrial production of liquid fuel from microalga.     

Biodiesel production from heterotrophic microalgal oil

The present study introduced an integrated method for the production of biodiesel from microalgal oil. Heterotrophic growth of Chlorella protothecoides resulted in the accumulation of high lipid content (55%) in cells. Large amount of microalgal oil was efficiently extracted from these heterotrophic cells by using n-hexane. Biodiesel comparable to conventional diesel was obtained from heterotrophic microalgal oil by acidic transesterification. The best process combination was 100% catalyst quantity (based on oil weight) with 56:1 molar ratio of methanol to oil at temperature of 30 degrees C, which reduced product specific gravity from an initial value of 0.912 to a final value of 0.8637 in about 4h of reaction time. The results suggested that the new process, which combined bioengineering and transesterification, was a feasible and effective method for the production of high quality biodiesel from microalgal oil.     

A symbiotic gas exchange between bioreactors enhances microalgal biomass and lipid productivities: taking advantage of complementary nutritional modes

This paper describes the association of two bioreactors: one photoautotrophic and the other heterotrophic, connected by the gas phase and allowing an exchange of O₂ and CO₂ gases between them, benefiting from a symbiotic effect. The association of two bioreactors was proposed with the aim of improving the microalgae oil productivity for biodiesel production. The outlet gas flow from the autotrophic (O₂ enriched) bioreactor was used as the inlet gas flow for the heterotrophic bioreactor. In parallel, the outlet gas flow from another heterotrophic (CO₂ enriched) bioreactor was used as the inlet gas flow for the autotrophic bioreactor. Aside from using the air supplied from the auto- and hetero-trophic bioreactors as controls, one mixotrophic bioreactor was also studied and used as a model, for its claimed advantage of CO₂ and organic carbon being simultaneously assimilated. The microalga Chlorella protothecoides was chosen as a model due to its ability to grow under different nutritional modes (auto, hetero, and mixotrophic), and its ability to attain a high biomass productivity and lipid content, suitable for biodiesel production. The comparison between heterotrophic, autotrophic, and mixotrophic Chlorella protothecoides growth for lipid production revealed that heterotrophic growth achieved the highest biomass productivity and lipid content (>22%), and furthermore showed that these lipids had the most suitable fatty acid profile in order to produce high quality biodiesel. Both associations showed a higher biomass productivity (10–20%), when comparing the two separately operated bioreactors (controls) which occurred on the fourth day. A more remarkable result would have been seen if in actuality the two bioreactors had been inter-connected in a closed loop. The biomass productivity gain would have been 30% and the lipid productivity gain would have been 100%, as seen by comparing the productivities of the symbiotic assemblage with the sum of the two bioreactors operating separately (controls). These results show an advantage of the symbiotic bioreactors association towards a cost-effective microalgal biodiesel production.     

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.     

光合自养缺陷型小球藻的筛选及生物能源应用

小球藻Chlorella protothecoides(C.protothecoides)是潜在的、可用于工业生产生物柴油的高产油微藻.本研究通过体外诱变的手段,获得了一株完全不能进行光合自养生长的突变体Al64.利用尼罗红染色和叶绿素自发荧光分析和电子显微镜分析细胞的亚显微结构,结果显示该突变体中叶绿体严重退化,其中类囊体膜结构缺失,导致该突变体缺乏叶绿素,无法进行光合自养生长.在富糖富氮的培养条件下,该光合自养缺陷型突变体的细胞密度和油脂含量比野生型细胞分别高5.54%和6.76%,分析还发现,该突变体产油能力为0.158 g L?1 h?1,比野生型提高12.8%.本文通过缺失光合作用突变体的构建,在异养高氮条件下实现了生物量及细胞内油脂含量的同步提高,为进一步提高微藻生产生物柴油的产量提供了新的研究平台.     

Heterotrophic production of biomass and lutein by Chlorella protothecoides on various nitrogen sources

The effects of nitrate, ammonium, and urea as nitrogen sources on the heterotrophic growth of Chlorella protothecoides were investigated using flask cultures. No appreciable inhibitory effect on the algal growth was observed over a nitrogen concentration range of 0.85-1.7 g l(-)(1). In contrast, differences in specific growth rate and biomass production were found among the cultures with the various nitrogen compounds. The influence of different nitrogen sources at a concentration equivalent to 1.7 g l(-)(1) nitrogen on the heterotrophic production of biomass and lutein by C. protothecoides was investigated using the culture medium containing 40 g l(-)(1) glucose as the sole carbon and energy source in fermentors. The maximum biomass concentrations in the three cultures with nitrate, ammonium, and urea were 18.4, 18.9, and 19.6 g l(-)(1) dry cells, respectively. The maximum lutein yields in these cultures were between 68.42 and 83.81 mg l(-)(1). The highest yields of both biomass and lutein were achieved in the culture with urea. It was therefore concluded that urea was the best nitrogen source for the production of biomass and lutein. Based on the experimental results, a group of kinetic models describing cell growth, lutein production, and glucose and nitrogen consumption were proposed and a satisfactory fit was found between the experimental results and predicted values. Dynamic analysis of models demonstrated that enhancing initial nitrogen concentration in fermentor cultures, which correspondingly enhances cell growth and lutein formation, may shorten the fermentation cycle by 25-46%.     

Heterotrophic production of lutein by selected Chlorella strains

Seven Chlorella strains representing three species obtained from culture collections and research laboratories were screened for their potential of heterotrophic production of lutein on two different media (Basal and Kuhl) containing glucose. While both media supported good growth and lutein formation of the seven strains in darkness, higher biomass concentrations and lutein content were achieved on Basal medium. Chlorella protothecoides CS-41 was chosen from the seven strains for further investigation due to its higher productivities of both biomass and lutein. The maximal biomass concentration and lutein content of C. protothecoides cultivated heterotrophically with 9 g L^-1 glucose in a 3.7-L fermentor were respectively 4.6 g dry cells L^-1 and 4.60 mg lutein g^-1 dry cells on Basal medium, and 4.0 g dry cells L^-1 and 4.36 mg lutein g^-1 dry cells on Kuhl medium. The heterotrophic cultivation process was scaled up successfully to 30 L using a fermentor, in which the Basal medium containing 36 g L^-1 glucose was used; the maximal biomass concentration of 16.4 g dry cells L^-1, specific growth rate of 0.92 d^-1,lutein content of 4.85 mg lutein g^-1 dry cells,growth yield of 0.47 g dry cells g^-1 glucose and lutein yield of 1.93 mg lutein g^-1 glucose were respectively achieved. This revised version was published online in August 2006 with corrections to the Cover Date.     

Waste molasses alone displaces glucose-based medium for microalgal fermentation towards cost-saving biodiesel production

The by-product of sugar refinery—waste molasses was explored as alternative to glucose-based medium of Chlorella protothecoides in this study. Enzymatic hydrolysis is required for waste molasses suitable for algal growth. Waste molasses hydrolysate was confirmed as a sole source of full nutrients to totally replace glucose-based medium in support of rapid growth and high oil yield from algae. Under optimized conditions, the maximum algal cell density, oil content, and oil yield were respectively 70.9 g/L, 57.6%, and 40.8 g/L. The scalability of the waste molasses-fed algal system was confirmed from 0.5 L flasks to 5 L fermenters. The quality of biodiesel from waste molasses-fed algae was probably comparable to that from glucose-fed ones. Economic analysis indicated the cost of oil production from waste molasses-fed algae reduced by 50%. Significant cost reduction of algal biodiesel production through fermentation engineering based on the approach is expected.     

不同营养条件下原始小球藻对蒽的富集和降解研究

研究了自养与异养条件下原始小球藻对蒽的降解和富集能力 .结果表明 ,自养条件下 ,浓度为1 0mg·L-1的蒽有 48.18%被降解 ,其中 2 8.81%属于自然光降解 ,仅有 19.37%被原始小球藻降解 .而异养条件下的原始小球藻对浓度为 2 .5mg·L-1的蒽降解率达到 33.5 3%,说明异养原始小球藻不仅能耐受高浓度蒽 ,而且表现出比自养原始小球藻更强的蒽降解能力 .两种条件下 ,80 %以上残留的蒽都被富集到藻细胞中 .虽然自养条件下原始小球藻对蒽的生物富集系数达 90 6 4,远大于异养条件下的生物富集系数(1899) ,但异养条件下藻对蒽的绝对富集量 (2 0 2 .2 9μg)远远高于自养条件下的 6 9.6 87μg .     

假丝酵母99-125脂肪酶的发酵工艺研究

对假丝酵母99-125脂肪酶的发酵工艺条件进行了一系列研究。选择了合适的培养基成分并进行优化 ,获得了最优的摇瓶培养基配方 (% ,W/V) :豆油 4.0 ,全脂豆粉 4.0 ,K₂HPO₄0.1,KH₂PO₄ 0.1。产酶水平能达到 5000IU/mL。在 30L发酵罐上进行初步放大实验 ,其产酶水平能达到 8100IU/mL。在1m³发酵罐上进行中试放大 ,产酶水平可达到 8000IU/mL。     

Enzymatic coproduction of biodiesel and glycerol carbonate from soybean oil and dimethyl carbonate

The enzymatic coproduction of biodiesel and glycerol carbonate by the transesterification of soybean oil was studied using lipase as catalyst in organic solvent. To produce biodiesel and glycerol carbonate simultaneously, experiments were designed sequentially. Enzyme screening, the molar ratio of dimethyl carbonate (DMC) to soybean oil, reaction temperature and solvent effects were investigated. The results of enzyme screening, at 100 g/L Novozym 435 (immobilized Candida antarctica lipase B), biodiesel and glycerol carbonate showed conversions of 58.7% and 50.7%, respectively. The optimal conditions were 60 °C, 100 g/L Novozym 435, 6.0:1 molar ratio with tert-butanol as solvent: 84.9% biodiesel and 92.0% glycerol carbonate production was achieved.     

Preparation of lipophilic alkyl (hydroxy)benzoates by solvent-free lipase-catalyzed esterification and transesterification

Agal-fermentation-based microbio-diesel production was realized through high-cell-density fermentation of Chlorella protothecoides and efficient transesterification process. Cell density achieved was 16.8 g l⁻¹ in 184 h and 51.2 g l⁻¹ in 167 h in a 5-l bioreactor by performing preliminary and improved fed-batch culture strategy, respectively. The lipid content was 57.8, 55.2, and 50.3% of cell dry weight from batch, primary, and improved fed-batch culture in 5-l bioreactor. Transesterification was catalyzed by immobilized lipase, and the conversion rate reached up to 98%. The properties of biodiesel from Chlorella were comparable to conventional diesel fuel and comply with US standard for Biodiesel. In a word, the approach including high-density fermentation of Chlorella and enzymatic transesterification process were set up and proved to be a promising alternative for biodiesel production.     

Effects of cassava starch hydrolysate on cell growth and lipid accumulation of the heterotrophic microalgae <Emphasis Type="Italic">Chlorella protothecoides</Emphasis>

Heterotrophic fermentation of microalgae has been shown to accumulate high amounts of microalgal lipids, which are regarded as one of the most promising feedstocks for sustainable biodiesel production. To increase the biomass and reduce the cost of microalgal culture, the purpose of this study was to evaluate the possibility of using cassava starch hydrolysate (CSH) instead of glucose as carbon source for heterotrophic culture of Chlorella protothecoides in flasks. First, the two-step enzymatic process of hydrolysis of cassava starch by α-amylase and glucoamylase was optimized; the conversion efficiency for cassava starch was up to 97.7%, and over 80% of CSH was glucose. Subsequently, we compared heterotrophic cultures of C. protothecoiedes using glucose or CSH as carbon source. The results demonstrated that when using CSH as the organic carbon source, the highest biomass and the maximum total lipid yield obtained were 15.8 and 4.19 g/L, representing increases of 42.3 and 27.7%, respectively, compared to using glucose as the organic carbon source. This suggests that CSH is a better carbon source than glucose for heterotrophic Chlorella protothecoides.     

酶法合成生物柴油工业化研究进展

介绍了北京化工大学近年来酶法合成生物柴油工业化研究的结果。主要内容包括以下几个方面:高产脂肪酶菌株的选育、脂肪酶发酵工艺优化及放大、脂肪酶固定化方法、酶反应器放大、生物柴油分离精制及副产物甘油综合利用。该脂肪酶假丝酵母Candida sp.99-125在5 m3罐发酵活力不低于8 000 IU/mL,然后将该脂肪酶吸附固定在织物膜上并进行表面改性,用于搅拌罐式反应器生产每吨甲酯的需酶量仅为4.2 kg,产品经分离精制调质后,其各项指标完全符合德国生物柴油生产标准。副产物甘油可用于1,3-丙二醇发酵,30 L发酵罐中1,3-丙二醇的产量可达到76.1 g/L。     

厌氧条件下小球藻细胞的异养转化和乳酸发酵(简报)

某些藻类植物,如小球藻——一种单细胞绿藻,不但能利用无机碳源通过光合作用进行自养生长,还能利用有机碳源转化为异养生长,这种转化又是可逆的。迄今为止,对于人工控制下藻细胞向异养转化的代谢和调控机理尚不清楚。本文通过分析小球藻细胞异养转化过程对氧气的依赖性,进一步研究它们在厌氧条件下的生长和乳酸发酵特征,探讨可异养转化的单细胞藻类(作为特殊的实验生物系统)在发酵工程和细胞工程领域里应用的可能性。     

小球藻藻菌共生体系在产油方面的特性

【目的】研究人工构建藻菌共生体系在产油方面的特性。【方法】从BG11培养基中分离、筛选出无菌小球藻,通过人工共培养方法构建了藻菌共生体系,探讨了共生体系中小球藻的生长及产油特性。【结果】相比无菌小球藻,藻菌共生体系对于藻的生长、油脂积累以及产生生物柴油的脂肪酸组分方面都有明显的促进作用,其中细菌(Stenotrophomonas maltophilia)和小球藻构建的共生体系效果最好,小球藻生物量提高了9%,油脂含量提高了36.3%,C18-1的含量提高了259.2%。【结论】进一步说明人工共培养方法构建藻菌共生体系能够提高微藻生物柴油的质量,具有很好的利用价值。     

以异养细胞作为种子的椭圆小球藻产油脂光自养培养优化

异养细胞种子/光自养培养方法是一种可异养培养的能源微藻培养的有效方法,但已有文献尚未从工艺优化角度考察其发展潜力。为了获得较高细胞密度的用于光自养培养的种子和提高光自养培养的细胞密度与油脂产率,对异养细胞种子/光自养培养的培养基和培养条件进行了优化。结果表明,采用优化后的培养基,椭圆小球藻在摇瓶中异养培养的最高藻细胞密度可达11.04 g/L,比在初始培养基条件下提高了28.0%,在5 L发酵罐中异养培养的藻细胞密度达到73.89 g/L;在2 L柱式光生物反应器中光自养培养的藻细胞密度、油脂含量和油脂产率分别达1.62 g/L、36.34%和6.1 mg/(L·h),油脂成分主要为含C16-C18碳链的脂肪酸,是制备生物柴油的理想原料。经过优化,异养细胞种子/光自养培养这一方法能够显著地提高椭圆小球藻产油脂的能力,这进一步表明异养细胞种子/光自养培养方法有望成为可异养的能源微藻的高效培养方式。     

小球藻高密度培养及油脂提取条件的优化

【目的】高密度培养小球藻及优化油脂提取条件。【方法】通过进行单因素实验研究不同培养基组成及环境因子对其细胞生长影响,并采用超声波提取法进行正交实验对藻粉油脂提取条件进行研究。【结果】对椭圆小球藻Y4进行异养培养,最适培养条件为:葡萄糖50 g/L,硝酸钾2 g/L,适宜的培养温度、摇床转速和接种量分别为29°C、180 r/min和20%。在此基础上,进行了1 L发酵罐培养实验,获得了干重18.25 g/L的生物量。通过对油脂提取条件进行优化,Y4的油脂提取率由优化前的25.0%提高到60.2%,提高了35.2%。【结论】优化了小球藻的培养条件及油脂提取条件,促进了小球藻的开发和利用。     

Biodiesel production from algal oil using cassava (<Emphasis Type="Italic">Manihot esculenta</Emphasis> Crantz) as feedstock

As a potential source of biomass supplies, cassava (Manihot esculenta Crantz) has been studied for bioethanol production, but not for the production of biodiesel. In this study, we used cassava hydrolysate as an alternative carbon source for the growth of microalgae (Chlorella protothecoides) which accumulated oil in vivo, with high oil content up to 53% by dry mass under a 5-L scale fermentation condition. The oils were extracted and converted into biodiesel by transesterification. The biodiesel obtained consisted of mainly unsaturated fatty acids methyl ester (over 82%), cetane acid methyl ester, linoleic acid methyl ester, and oleic acid methyl ester. This work suggests the feasibility of an alternative choice for producing biodiesel from cassava by microalgae fermentation. We report herewith the optimized condition for the fermentation and for the hydrolysis of cassava as the carbon source.     

Production of protease and lipase by solvent tolerant Pseudomonas aeruginosa PseA in solid-state fermentation using Jatropha curcas seed cake as substrate

Deoiled Jatropha seed cake was assessed for its suitability as substrate for enzyme production by solid-state fermentation (SSF). Solvent tolerant Pseudomonas aeruginosa PseA strain previously reported by us was used for fermentation. The seed cake supported good bacterial growth and enzyme production (protease, 1818 U/g of substrate and lipase, 625 U/g of substrate) as evident by its chemical composition. Maximum protease and lipase production was observed at 50% substrate moisture, a growth period of 72 and 120 h, and a substrate pH of 6.0 and 7.0, respectively. Enrichment with maltose as carbon source increased protease and lipase production by 6.3- and 1.6-fold, respectively. Nitrogen supplementation with peptone for protease and NaNO(3) for lipase production also enhanced the enzyme yield reaching 11,376 U protease activity and 1084 U lipase activity per gram of Jatropha seed cake. These results demonstrated viable approach for utilization of this huge biomass by solid-state fermentation for the production of industrial enzymes. This offers significant benefit due to low cost and abundant availability of cake during biodiesel production.