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Journal ArticleDOI

Mixotrophic cultivation of Chlorella vulgaris using industrial dairy waste as organic carbon source.

01 Aug 2012-Bioresource Technology (Elsevier)-Vol. 118, pp 61-66
TL;DR: Mixotrophic cultivation of C. vulgaris using the main dairy industry by-product could be considered a feasible alternative to reduce the costs of microalgal biomass production, since it does not require the addition of expensive carbohydrates to the culture medium.
About: This article is published in Bioresource Technology.The article was published on 2012-08-01 and is currently open access. It has received 320 citations till now. The article focuses on the topics: Chlorella vulgaris & Biomass.

Summary (2 min read)

1. Introduction

  • Microalgae cultivation has been carried out throughout the world in order to produce animal feed or high-value added products, such as cosmetics, pharmaceuticals and health supplements (Das et al., 2011) .
  • Nonetheless, this culture mode, known as photoautotrophic, presents several disadvantages including low cell densities and long cultivation periods.
  • The cost of the organic carbon substrate is estimated to be about 80% of the total cost of the cultivation medium (Bhatnagar et al., 2011) .
  • Cheese whey (CW), the liquid by-product remaining from the cheese manufacturing process constitutes a serious environmental problem of dairy industries due to its high organic matter content (Dragone et al., 2009) .

2.1. Microalgal strain and inoculum preparation

  • The freshwater microalga C. vulgaris (strain P12) was used in all experiments.
  • The microalgal inoculum was prepared according to previous studies (Fernandes et al., 2010) and conducted at 30 °C in 0.5-L glass photobioreactors under photoautotrophic conditions.

2.2. Media and culture conditions

  • Four different cultivation conditions were carried out in duplicate (Table 1 ).
  • Sweet CW powder was supplied by Lactogal (Porto, Portugal).
  • After reaching the stationary growth phase, cells were collected and centrifuged at 8750Âg for 10 min, washed with distilled water and then freeze-dried for further biochemical characterization.
  • The supernatant was also collected and frozen for subsequent sugar analyses.

2.3. Determination of microalgal cell concentration

  • Cell concentration in the photobioreactor cultures was measured regularly by using an improved Neubauer hemocytometer.
  • Biomass concentration was estimated by cell dry weight after centrifugation of the sample (8750Âg for 10 min), washing with distilled water and drying at 105 °C until constant weight.

2.6. Measurement of lipid and protein contents in microalgae

  • Total lipids were determined by the classic Folch chloroformbased lipid extraction protocol.
  • The protein content of microalgae was quantified according to the method of Lowry.

2.7. Measurement of chlorophylls and total carotenoids concentration

  • Chlorophylls and carotenoids in C. vulgaris were extracted with methanol and spectrophotometrically determined as described by Dere et al. (1998) .
  • Total pigment content was obtained by summing chlorophylls and carotenoids contents.

3.1. Growth parameters of microalgae cultivated under photoautotrophic and mixotrophic conditions

  • Specific growth rate, final biomass concentration and biomass productivity of C. vulgaris cultivated under photoautotrophic and mixotrophic conditions were compared and summarized in Table 2 .
  • These values were almost 3.5 times higher than those obtained when cells were grown in inorganic medium supplemented with non-hydrolyzed CW powder solution, and under photoautotrophic mode of nutrition.
  • It can be observed in Table 2 that the highest values of X max (3.58 g/L) and P max (0.75 g/L d) achieved in the mixotrophic culture using hydrolyzed CW powder solution resulted in 2.9-and 7.5-fold increase respectively, when compared to the values obtained in the photoautotrophic culture.
  • These results are in agreement with a previous study, which reported that mixotrophic C. vulgaris growth in glucose yielded higher biomass content and productivity than cells grown under photoautotrophic conditions (Kong et al., 2011) .
  • It is worth mentioning that the organic substrate played an important role in promoting biomass accumulation of C. vulgaris during microalgae cultivation.

3.2. Consumption of glucose and galactose by C. vulgaris

  • The above presented results demonstrated that the microalgal species used in this study was able to grow mixotrophically in the presence of glucose and galactose.
  • It was found that glucose and galactose were consumed in larger quantities during microalgal growth in the presence of the hydrolyzed CW powder solution, in comparison to the culture supplemented with a mixture of pure sugars.
  • Means in the same column followed by different letters represent significant differences (p < 0.05).
  • * l max = Specific growth rate during exponential growth phase.
  • Regardless of the media used, glucose was more efficiently assimilated than galactose by C. vulgaris cells grown under mixotrophic conditions.

3.3. Influence of nutritional modes on biochemical composition of C. vulgaris

  • The lipid content and lipid productivity of C. vulgaris under different growth conditions were compared and depicted in Fig. 1 .
  • On the other hand, the highest lipid productivity (253 mg/L d) was achieved when cells were grown in culture medium supplemented with hydrolyzed CW powder solution, due to the highest growth rate and cell density.
  • Therefore, since the starch productivity was calculated by multiplying the biomass productivity by the starch content (w/w) in microalgae, no differences on the values of this parameter were observed for the cells cultivated under mixotrophic conditions using hydrolyzed CW powder solution, and a mixture of glucose and galactose as organic carbon sources.
  • Cultivation of C. vulgaris P12 using hydrolyzed CW powder solution as organic carbon source led to the highest protein content (63.5%) and protein productivity (474 mg/L d).
  • The higher content of chlorophylls obtained in the photoautotrophic culture when compared to mixotrophic cultures confirms such observation.

4. Conclusions

  • When compared with the photoautotrophic control culture, mixotrophic microalgae grew faster, providing higher productivities of biomass, lipids, starch and proteins.
  • Furthermore, microalgal biomass production and carbohydrate consumption were enhanced by supplementing the inorganic culture medium with hydrolyzed CW powder solution, than supplementing with a mixture of pure glucose and galactose, as a consequence of stimulatory effects arising from growth-promoting nutrients in CW.

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Citations
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Journal ArticleDOI
TL;DR: This paper attempts to give a general overview of techniques that can be used for increasing the microalgal biomass carbohydrate content, and biomass conversion technologies, related to the conversion of carbohydrates into biofuels are discussed.
Abstract: Microalgal biomass seems to be a promising feedstock for biofuel generation. Microalgae have relative high photosynthetic efficiencies, high growth rates, and some species can thrive in brackish water or seawater and wastewater from the food- and agro-industrial sector. Today, the main interest in research is the cultivation of microalgae for lipids production to generate biodiesel. However, there are several other biological or thermochemical conversion technologies, in which microalgal biomass could be used as substrate. However, the high protein content or the low carbohydrate content of the majority of the microalgal species might be a constraint for their possible use in these technologies. Moreover, in the majority of biomass conversion technologies, carbohydrates are the main substrate for production of biofuels. Nevertheless, microalgae biomass composition could be manipulated by several cultivation techniques, such as nutrient starvation or other stressed environmental conditions, which cause the microalgae to accumulate carbohydrates. This paper attempts to give a general overview of techniques that can be used for increasing the microalgal biomass carbohydrate content. In addition, biomass conversion technologies, related to the conversion of carbohydrates into biofuels are discussed.

410 citations


Cites background from "Mixotrophic cultivation of Chlorell..."

  • ...For instance, Chlorella accumulates more carbohydrates under mixotrophic (Abreu et al. 2012) or heterotrophic mode (Choix et al....

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  • ...For instance, Chlorella accumulates more carbohydrates under mixotrophic (Abreu et al. 2012) or heterotrophic mode (Choix et al. 2012) than Table 2 Innate and enhanced carbohydrates biomass content after the adaptation of a cultivation technique Microalgae Innate carbohydrate, % Enhanced…...

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TL;DR: A critical account of micro-algae as an important step in wastewater treatment for enhancing the reduction of N, P and the chemical oxygen demand in wastewater, whilst utilising a fraction of the energy demand of conventional biological treatment systems.

318 citations

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TL;DR: In this review, the effects on the biomass and lipid production of microalgal Chlorella cultures using different kinds of wastewater were summarized and limitations of wastewater-based ofmicroalgal culture were commented.

266 citations


Cites background from "Mixotrophic cultivation of Chlorell..."

  • ...…such as crude glycerol from biodiesel 437 industry, sugars from industrial and agricultural waste, acetate from anaerobic digestion, 438 cellulosic materials and cane molasses can be used to replace the expensive pure 439 glucose for the cultivation of mixotrophic algae (Abreu et al., 2012)....

    [...]

  • ...Additionally, 477 Abreu et al. (2012) reported that C. vulgaris was cultivated in hydrolyzed cheese whey 478 (5 g L -1 glucose and 5 g L -1 galactose), and a lipid productivity about 250 mg L -1 d -1 479 was obtained....

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TL;DR: Prospects and challenges of application of microalgae in various areas of agriculture, including crop production, protection and natural resource management are focused on.

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TL;DR: It is demonstrated that optimization of microalgal cultivation conditions can be considered a useful strategy for maximizing CO2 bio-mitigation by C. vulgaris.

221 citations

References
More filters
Journal ArticleDOI
TL;DR: In this article, the authors reviewed the technologies underpinning microalgae-to-bio-fuels systems, focusing on the biomass production, harvesting, conversion technologies, and the extraction of useful co-products.
Abstract: Sustainability is a key principle in natural resource management, and it involves operational efficiency, minimisation of environmental impact and socio-economic considerations; all of which are interdependent. It has become increasingly obvious that continued reliance on fossil fuel energy resources is unsustainable, owing to both depleting world reserves and the green house gas emissions associated with their use. Therefore, there are vigorous research initiatives aimed at developing alternative renewable and potentially carbon neutral solid, liquid and gaseous biofuels as alternative energy resources. However, alternate energy resources akin to first generation biofuels derived from terrestrial crops such as sugarcane, sugar beet, maize and rapeseed place an enormous strain on world food markets, contribute to water shortages and precipitate the destruction of the world's forests. Second generation biofuels derived from lignocellulosic agriculture and forest residues and from non-food crop feedstocks address some of the above problems; however there is concern over competing land use or required land use changes. Therefore, based on current knowledge and technology projections, third generation biofuels specifically derived from microalgae are considered to be a technically viable alternative energy resource that is devoid of the major drawbacks associated with first and second generation biofuels. Microalgae are photosynthetic microorganisms with simple growing requirements (light, sugars, CO 2 , N, P, and K) that can produce lipids, proteins and carbohydrates in large amounts over short periods of time. These products can be processed into both biofuels and valuable co-products. This study reviewed the technologies underpinning microalgae-to-biofuels systems, focusing on the biomass production, harvesting, conversion technologies, and the extraction of useful co-products. It also reviewed the synergistic coupling of microalgae propagation with carbon sequestration and wastewater treatment potential for mitigation of environmental impacts associated with energy conversion and utilisation. It was found that, whereas there are outstanding issues related to photosynthetic efficiencies and biomass output, microalgae-derived biofuels could progressively substitute a significant proportion of the fossil fuels required to meet the growing energy demand.

4,432 citations


"Mixotrophic cultivation of Chlorell..." refers methods in this paper

  • ...More recently, microalgae have also been used for wastewater treatment, carbon dioxide (CO2) mitigation, or as a feedstock for biofuel production (Brennan and Owende, 2010)....

    [...]

Journal ArticleDOI
TL;DR: This review presents recent advances in microAlgal cultivation, photobioreactor design, and harvesting technologies with a focus on microalgal oil (mainly triglycerides) production and aims to provide useful information to help future development of efficient and commercially viable technology for microalgae-based biodiesel production.

1,662 citations


"Mixotrophic cultivation of Chlorell..." refers background in this paper

  • ...These photosynthetic microorganisms can be cultivated either in open ponds or closed photobioreactors (PBR) using CO2 and light as carbon and energy sources, respectively (Chen et al., 2011)....

    [...]

Journal ArticleDOI
TL;DR: Biomass and lipid productivities of Chlorella vulgaris under different growth conditions were investigated and it was found that C. vulgaris is mixotrophic.
Abstract: Biomass and lipid productivities of Chlorella vulgaris under different growth conditions were investigated. While autotrophic growth did provide higher cellular lipid content (38%), the lipid productivity was much lower compared with those from heterotrophic growth with acetate, glucose, or glycerol. Optimal cell growth (2 g l−1) and lipid productivity (54 mg l−1 day−1) were attained using glucose at 1% (w/v) whereas higher concentrations were inhibitory. Growth of C. vulgaris on glycerol had a similar dose effects as those from glucose. Overall, C. vulgaris is mixotrophic.

971 citations


"Mixotrophic cultivation of Chlorell..." refers background or result in this paper

  • ...Other authors (Liang et al., 2009) have also shown that the amount of lipids accumulated in C. vulgaris under photoautotrophic growth conditions may surpass that from mixotrophic growth....

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  • ...Other authors (Liang et al., 2009) have also shown that the amount of lipids accumulated in C....

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  • ...As a result, less costly organic sources have to be found in order to overcome the high carbon cost resulting from mixotrophic culture conditions (Liang et al., 2009)....

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  • ...These results were remarkable in comparison with values presented in previous studies (Liang et al., 2009)....

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Book
01 Jan 2004
TL;DR: Handbook of microalgal culture :biotechnology and applied phycology, Handbook of micro algal culture, اطلاعات رسانی کشاورزی, £20,000 (US$30,000)
Abstract: Handbook of microalgal culture :biotechnology and applied phycology , Handbook of microalgal culture :biotechnology and applied phycology , مرکز فناوری اطلاعات و اطلاع رسانی کشاورزی

965 citations

Journal ArticleDOI
TL;DR: Cheese-whey utilization has been the subject of much research as mentioned in this paper and the most representative applications of cheese whey being exploited and under research are briefly discussed in this paper.

720 citations


"Mixotrophic cultivation of Chlorell..." refers background in this paper

  • ...In addition to this carbohydrate, CW also contains proteins, lipids, water-soluble vitamins and minerals (González Siso, 1996)....

    [...]

Frequently Asked Questions (16)
Q1. What are the contributions in "Mixotrophic cultivation of chlorella vulgaris using industrial dairy waste as organic carbon source" ?

In this paper, the growth parameters and biochemical composition of the green microalga Chlorella vulgaris cultivated under different mixotrophic conditions were determined and compared to those obtained from a photoautotrophic control culture. 

The stimulatory effect of hydrolyzed CW powder solution on biomass production is probably related to the presence of some nutrients in CW powder composition, such as phosphorous and calcium. 

In particular, glucose was completely consumed and only 4% of the initial galactose concentration remained in the growth medium at the end of cultivation when hydrolyzed CW powder solution was used as carbon source. 

microalgal biomass production and carbohydrate consumption were enhanced by supplementing the inorganic culture medium with hydrolyzed CW powder solution, than supplementing with a mixture of pure glucose and galactose, as a consequence of stimulatory effects arising from growth-promoting nutrients in CW. 

The organic carbon sources used for mixotrophic cell growth were: a non-hydrolyzed CW powder solution, a mixture of pure glucose and galactose, and a hydrolyzed CW powder solution. 

Despite mixotrophic cultivation of microalgae provides higher biomass and lipid productivities than cultivation under photoautotrophic conditions, the cost of the organic carbon substrate is estimated to be about 80% of the total cost of the cultivation medium (Bhatnagar et al., 2011). 

It was found that glucose and galactose were consumed in larger quantities during microalgal growth in the presence of the hydrolyzed CW powder solution, in comparison to the culture supplemented with a mixture of pure sugars. 

since the amount of energy dissipated is minimal, mixotrophy provides higher energetic efficiency than other cultivation modes (Lalucat et al., 1984). 

When compared with the photoautotrophic control culture, mixotrophic microalgae grew faster, providing higher productivities of biomass, lipids, starch and proteins. 

a higher microalgal biomass concentration than that found in their study could have been obtained by using acid CW powder due to the higher concentrations of calcium and phosphorous presented in that type of whey (Mavropoulou and Kosikowski, 1973). 

Other authors (Liang et al., 2009) have also shown that the amount of lipids accumulated in C. vulgaris under photoautotrophic growth conditions may surpass that from mixotrophic growth. 

As shown in Table 2, supplementation of the inorganic culture medium with hydrolyzed CW powder solution led to higher biomass concentration than supplementation with a mixture of glucose and galactose. 

On the other hand, Yan et al. (in press) reported that low chlorophyll content in mixotrophic cells decreases the dependence on light. 

The specific growth rate (l, day 1) was calculated from the Eq. (1), where N1 and N2 were the concentration of cells at the beginning (t1) and at the end (t2) of the exponential growth phase, respectively.l ¼ ðln N2 ln N1Þ=ðt2 t1Þ ð1ÞBiomass productivity (Pmax, g/L d) during the culture period was calculated from the Eq. (2), where Xt was the biomass concentration (g/L) at the end of the exponential growth phase (tx) and X0 the initial biomass concentration (g/L) at t0 (day):Pmax ¼ ðXt X0Þ=ðtx t0Þ ð2ÞProductivity of starch, lipids and proteins at the end of cultivation were calculated from the Eq. (3), where Pcomponent was the productivity of starch, lipids or proteins, Pmax was the biomass productivity and Fcomponent was the mass fraction (w/w) of each component. 

1. When compared with mixotrophic cultures, higher lipid content (42%) was obtained in photoautotrophic mode at the beginning of the stationary growth phase (approximately 190 h). 

On the other hand, after nearly 90 h of cultivation, initial contents of glucose and galactose dropped 80.5% and 49.5%, respectively, in the culture supplemented with both sugars.