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POTENTIAL OF HETEROTROPHIC ALGAL OILS

No documento BIOFUELS FROM ALGAE (páginas 126-132)

In comparison to photoautotrophy, heterotrophic growth mode offers substantial advan- tages, e.g., elimination of the light requirement, ease of control for monoculture, high cell density, and great biomass productivity (Chen, 1996). Lab-scale heterotrophic production of algae has been reported in recent decades, either in shaking flasks or in small-volume fermen- ters (Cheng et al., 2009; Liang et al., 2009; Liu et al., 2010, 2011b; Yan et al., 2011).Liang et al (2009)examined the growth ofChlorella vulgarisunder both phototrophic and heterotrophic conditions and indicated heterotrophicC. vulgarishad around threefold higher biomass yield than a phototrophic one.Liu et al (2011b)investigated the growth ofChlorella zofingiensis; the alga achieved 10.1 g L–1of cell density under heterotrophic conditions compared to 1.9 g L–1 under phototrophic conditions.Chlorella protothecoides, another well-studied green alga, was reported to achieve as high as up to 17 g L–1of cell density in heterotrophic batch cultures (Cheng et al., 2009). This may be further improved through using culture techniques such as fed-batch, chemostat, and cell recycling, which have been widely used for fermentation of bacteria or yeasts. For example, the fed-batchC. protothecoidesachieved a high cell density of 97 g L–1in a 5-L fermenter (Yan et al., 2011), much higher than that obtained in photoau- totrophic culture systems (open ponds or photobioreactors) and close to the yeast yield 113

6.3 POTENTIAL OF HETEROTROPHIC ALGAL OILS

TABLE 6.1 Algae Reported with Heterotrophic Growth.

Algae Carbon Sources References

Green algae

Chlamydomonas reinhardtii Acetate Chen and Johns, 1994,1996;Zhang et al., 1999a Chlorella minutissima Glucose, starch, sucrose, glycine,

acetate, glycerin

Li et al., 2011

Chlorella protothecoides Glucose, glycerol, hydrolyzed carbohydrates, molasses, municipal wastewater

Zhang et al., 1999b; Miao and Wu, 2006; Cheng et al., 2009;Ruiz et al., 2009; Gao et al., 2010;

O’Grady and Morgan, 2011; Yan et al., 2011; Chen and walker, 2012; Zhou et al. 2012

Chlorella pyrenoidosa Glucose Running et al., 1994

Chlorella regularis Glucose, acetate Endo et al., 1977; Sansawa and Endo, 2004 Chlorella saccharophila Glucose, glycerol Tan and Johns, 1991; Isleten-Hosoglu et al., 2012

Chlorella sorokiniana Glucose Chen and Johns, 1991; Zheng et al., 2012

Chlorella vulgaris Agro-industrial co-products, glucose, sucrose, acetate, glycerol

Rattanapoltee et al., 2008; Mitra et al., 2012; Liang et al., 2009; Scarsella et al., 2009

Chlorella zofingiensis Glucose, fructose, mannose, sucrose, molasses

Ip and Chen, 2005; Liu et al., 2010, 2011b, 2012a

Haematococcus lacustris Glucose Chen et al., 1997

Haematococcus pluvialis Acetate Kobayashi et al., 1992

Micractinium pusillum Glucose, acetate Bouarab et al., 2004

Pseudococcomyxa chodatii Glucose Kiseleva and Kotlova, 2007

Tetraselmis suecica Glucose, acetate Day and Tsavalos, 1996; Azma et al., 2011 Diatom

Cyclotella cryptica Glucose Pahl et al., 2010

Nitzschia laevis Glucose Wen and Chen, 2001a,b; Chen et al., 2008

Others

Aphanothece microscopica Fish processing wastewater Queiroz et al., 2011

Crypthecodinium Cohnii Glucose Couto et al., 2010; Jiang et al., 1999; Jiang and Chen, 2000a,b

Galdieria sulphuraria Glucose Schmidt et al., 2005; Sloth et al., 2006

Ochromonas danica Phenolic mixtures Semple, 1998

Schizochytrium limacinum Glycerol Ethier et al., 2011

Schizochytrium mangrovei Glucose Fan et al., 2007

Schizochytriumsp. Glucose Ganuza et al., 2008

Spirulinasp. Glucose Chojnacka and Noworyta, 2004

Spongiococcum exetricicum Glucose Hilaly et al., 1994

Synechocystissp. Glucose Kong et al., 2003

114 6. HETEROTROPHIC PRODUCTION OF ALGAL OILS

Glc Ru5P

E4P S7P

R5P X5P G6P

F6P

GAP G3P 1

2

3

5 6 PEP

AcCoA

OAA

Mal

Fum

AKG

Suc

ICT Gln

NH3

Glu Pyr

7

8

10

11

12 15

14

13

22 23

9

20 21

4

16 17

18

19

FIGURE 6.1 Central carbon metabolism of microalgae in heterotrophic cultures based on glucose. Glu, Glucose; G6P, Glucose-6-Phosphate; F6P, Fructose-6-Phosphate; GAP, Glyceraldehyde-3-Phosphate; G3P, 3-Phosphoglycerate;

PEP, Phosphoenolpyruvate; Pyr, Pyruvate; AcCoA, Acetyl- CoA; ICT, Isocitrate; AKG,a-Ketoglutarate; Suc, Succinyl- CoA; Fum, Fumarate; Mal, Malate; OAA, Oxalacetate;

Ru5P, Ribulose-5-Phosphate; R5P, Ribose-5-Phosphate;

X5P, Xyluose-5-Phosphate; E4P, Erythrose-4-Phosphate;

S7P, Sedoheptulose-7-Phosphate; Glu, Glutamate; Gln, Glutamine. For details of the reactions with numbers, see Table 6.2.

TABLE 6.2 The Central Metabolic Network of Glucose in Heterotrophic Algae with the Stoichiometric Reactions.

Glycolytic pathway

Glc + ATP =>G6P + ADP + H 1

G6P<=>F6P 2

F6P + ATP =>2GAP + ADP + H 3

2GAP + H2O =>F6P + Pi 4

GAP + NAD + Pi+ ADP<=>G3P + ATP + NADH + H 5

G3P<=>PEP + H2O 6

PEP + ADP =>Pyr + ATP 7

Pyr + NAD + CoA =>AcCoA + NADH + CO2+ H 8

PEP + CO2+ ADP =>OAA + ATP 9

Continued

115

6.3 POTENTIAL OF HETEROTROPHIC ALGAL OILS

(Li et al., 2007b; Kurosawa et al., 2010; Zhang et al., 2011). Although the growth and biomass production of algae are species/strain dependent and may vary greatly, the overall bio- mass yield and productivity of heterotrophic algae are significantly higher than those of phototrophic ones, as illustrated byFigures 6.2aand6.2b.

Heterotrophic culture of algae offers not only high cell density but also high level of oils. The lipid contents of alga cultured heterotrophically were shown inTable 6.3. The lipid content varies from 4.8% to 60% of dry weight, depending on the algal species/strains and culture con- ditions. Commonly, stresses such as high light intensity and/or nitrogen starvation are re- quired to induce intracellular oil accumulation of algae under photoautotrophic conditions.

These stresses, however, are unfavorable for algal growth and biomass production, causing the contradiction between growth and oil synthesis. In contrast, the heterotrophic algae are able to accumulate oil while simultaneously building up biomass; for example, the intracellular oil content ofC. zofingiensisincreased from 0.25 to 0.5 g g–1(on a dry-weight basis) when the cell density increased from 5 to 42 g L–1(Liu et al., 2010). The accumulated oil contains mainly neu- tral lipids, in particular triacylglycerol (TAG). The TAG may account for up to 80% of neutral lipids or 71% of total lipids (Liu et al., 2011b). TAG is regarded as superior to polar lipids (phos- pholipids and glycolipids) for biodiesel production due to its higher content of fatty acids.

Taking into account the rapid growth and abundance of oils, heterotrophic algae usually allow TABLE 6.2 The Central Metabolic Network of Glucose in Heterotrophic Algae with the

Stoichiometric Reactions—Cont’d Tricarboxylic acid cycle

OAA + AcCOA + H2O<=>ICT + CoA + H 10

ICT + NAD<=>AKG + NADH + CO2 11

AKG + CoA + NAD =>Suc + NADH + CO2+ H 12

Suc + ADP + Pi+ FAD<=>Fum + FADH2+ATP + CoA 13

Fum<=>Mal 14

Fum + NAD + H2O<=>OAA + NADH + H 15

Pentose phosphate pathway

G6P + 2NADP + H2O =>Ru5P + CO2+ 2NADPH + 2H 16

Ru5P<=>R5P 17

Ru5P<=>X5P 18

R5P + X5P<=>S7P + GAP 19

S7P + GAP<=>F6P + E4P 20

X5P + E4P<=>F6P + GAP 21

Utilization of nitrogen

AKG + NADPH + Gln =>2Glu + NADP 22

Glu + NH3 + ATP =>Gln + ADP + Pi 23

116 6. HETEROTROPHIC PRODUCTION OF ALGAL OILS

TABLE 6.3 Oil Content of Heterotrophic Algae.

Algae Oil Content (% Dry Weight) References

Green algae

Chlorella minutissima 16.1 Li et al., 2011

Chlorella protothecoides 44.3-48.7 Li et al., 2007a

Chlorella protothecoides 44 Cheng et al., 2009

Chlorella protothecoides 52.5 Gao et al., 2010

Chlorella protothecoides 58.9 O’Grady and Morgan, 2011

Chlorella protothecoides 32 Chen and Walker, 2012

Chlorella protothecoides 49.4 De la Hoz Siegler et al., 2012

Chlorella protothecoides 28.9 Zhou et al., 2012

Chlorella saccharophila 26.7-36.3 Isleten-Hosoglu et al., 2012

Chlorella sorokiniana 20.1-46 Chen and Johns, 1991

Chlorella sorokiniana 23.3 Zheng et al., 2012

Continued 2.4 14

1.8 0.9

0.6 0.3

A 0.0 B

C D

500 400 300 200 100 Oil productivity (mg L-1 day-1)Biomass productivity (g L-1 day-1)

0

12 6 4 2 0

0 1,000 2,000 3,000 10,000 20,000

FIGURE 6.2 Biomass (a, b) and oil (c, d) productivities of phototrophic (open) and heterotrophic (filled) algae, based on the data of research articles published in the past decade. The differences in biomass and oil productivities between cultures under phototrophic and heterotrophic growth conditions were statistically significant using Duncan’s multiple-range test with the ANOVA procedure.

117

6.3 POTENTIAL OF HETEROTROPHIC ALGAL OILS

a high volumetric oil productivity (Figures 6.2cand6.2d), e.g., 7.3 g L–1day–1in the case of C. protothecoidesunder fed-batch culture conditions (Yan et al., 2011). The fatty acid character- istics of oils, e.g., carbon chain length and unsaturation degree, largely determine the properties of biodiesel such as cetane number, viscosity, cold flow, and oxidative stability (Knothe, 2005).

Although the fatty acid species of algae grown heterotrophically may show few differences in comparison to photoautotrophy, the proportions of individual fatty acid vary greatly.Liu et al.

(2011b)investigated the fatty acid profiles ofC. zofingiensis and indicated that heterotrophic cells contained low levels of C16:0, C16:3, C18:0, and C18:3 but much higher content of C18:1 than autotrophic cells. The proportion of C18:1 is regarded as an important factor for bio- diesel quality because it can provide a compromise solution between oxidative stability and low-temperature properties (Knothe, 2009). The higher the C18:1 content, the better the biodie- sel quality. The biodiesel derived from heterotrophic algae was analyzed with respect to the key properties (e.g., energy density, viscosity, flash point, cold filter plugging point, and acid value), and the results showed that most properties complied with the specifications established by the American Society for Testing and Materials (Xu et al., 2006).

In addition to the lab-scale cultures, many attempts have been made to develop industrial- scale processes for the heterotrophic cultivation of algae. The heterotrophicChlorellacultures have long been initiated in Japan and Taiwan in the late 1970s;Chlorellaspecies were cultured in stainless steel tanks using glucose and/or acetate as carbon and energy sources, with an annual production of 1,100 tons biomass (Lin, 2005). Thereafter, large-scale heterotrophic TABLE 6.3 Oil Content of Heterotrophic Algae—Cont’d

Algae Oil Content (% Dry Weight) References

Chlorella vulgaris 23-34 Liang et al., 2009

Chlorella vulgaris 32.9 Rattanapoltee et al., 2008

Chlorella vulgaris 35-58.9 Scarsella et al., 2009

Chlorella vulgaris 11-43 Mitra et al., 2012

Chlorella zofingiensis 52 Liu et al., 2010

Chlorella zofingiensis 51.1 Liu et al., 2011b

Chlorella zofingiensis 48.9 Liu et al., 2012a

Diatoms

Cyclotella cryptica 4.8-7.4 Pahl et al., 2010

Nitzschia laevis 12.8 Chen et al., 2008

Others

Aphanothece microscopica 7.1-15.3 Queiroz et al., 2011

Crypthecodinium Cohnii 19.9 Couto et al., 2010

Schizochytrium limacinum 50.3 Ethier et al., 2011

Schizochytrium mangrovei 68 Fan et al., 2007

Schizochytriumsp. 35 Ganuza et al., 2008

118 6. HETEROTROPHIC PRODUCTION OF ALGAL OILS

cultivation of several other algal strains were reported, for example,Tetraselmis suecica in 50,000-L fermenters (Day et al., 1991), Crypthecodinium cohnii with a capacity of 150,000 L (Radmer and Fisher, 1996), andSpongiococcum exetricciumfed-batch cultured in 450-L fermen- ters (Hilaly et al., 1994), though these cultures were used not for oils but for high-value prod- ucts. Recently, a scale-up heterotrophic cultivation ofC. protothecoideswas reported for oil production in 11,000-L fermenters, where the daily biomass production of 20 kg and oil pro- duction of 8.8 kg were achieved (Li et al., 2007a).

Because of the elimination of light requirements and sophisticated fermentation systems that have developed, the scale-up of heterotrophic cultures for high cell density and oil yield is rel- atively easier to achieve than that of autotrophic cultures. The production of heterotrophic algal cultures, however, is restricted, due largely to (1) the limited number of available heterotrophic species, (2) possible contamination by bacteria or fungi, (3) inhibition of growth by soluble or- ganic substrates (e.g., sugar) at high concentrations, and (4) the relatively high cost of organic carbon sources. The first limitation might be overcome by performing extensive screening an- alyses. For example,Vazhappilly and Chen (1998)intensively studied the heterotrophic poten- tial of 20 algal strains and suggested that 6 of them showed good heterotrophic growth. As the screening expands, increasing algal species/strains will be identified with heterotrophic poten- tial. In some cases, the obligate photoautotrophic algae can be metabolic engineered to grow heterotrophically.Zaslavskaia et al (2001)reported that a genetically modifiedPhaeodactylum tricornutum,through introducing a gene encoding a glucose transporter, was capable of thriv- ing on exogenous glucose in the absence of light, suggesting an alternative approach to increas- ing the available number of heterotrophically grown algae. The second problem is due mainly to the relatively slow growth of algae compared with other microorganisms such as bacteria or yeast that grow fast and finally dominate the cultures. Rigorous sterilization and aseptic oper- ation are necessary and considered to be effective to circumvent such possible contamination.

Growth inhibition is a common problem occurring in batch cultures, which has restricted the use of batch cultures in commercial production processes. The growth inhibition may be attrib- uted to the high initial concentration of substrates (e.g., sugars) or the possible buildup of cer- tain inhibitory substances produced by algae during culture periods. For example, the sugar concentration of over 20 g L–1was reported to inhibit the growth ofC. zofingiensis(Liu et al., 2010, 2012a). Advances in heterotrophic culture systems may eliminate or reduce the growth-inhibition problems, where fed-batch, chemostat, and cell recycle have been intensively investigated (Wen and Chen, 2002a; De la Hoz Siegler et al., 2011; Liu et al., 2012a). The organic carbon sources—in particular, glucose—account for the major cost of a culture medium and contribute to the relatively high cost of heterotrophic production, which makes the algal oils from heterotrophic cultures less economically viable than those from autotrophic cultures.

Cheap alternatives are sought with the goal of bringing down production costs, e.g., waste mo- lasses (Yan et al., 2011; Liu et al., 2012a), carbohydrate hydrolysate (Cheng et al., 2009; Gao et al., 2010), and biodiesel byproduct glycerol (O’Grady and Morgan, 2011).

6.4 FACTORS AFFECTING HETEROTROPHIC

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