the green solution-optimizing productivity of bi-substate microalgae cultures

1
The Green Solution Optimizing productivity of bi-substrate microalgae cultures Leng,M., Ibarra-Vidal,M., De la Hoz Siegler, H. Department of Chemical and Petroleum Engineering Background Goal Results Contact Information: [email protected] Materials and Methods Conclusions Future Work References Acknowledgements Glycerol is a waste generated from biodiesel production. We can capitalize on its low-cost and availability by utilizing it as a carbon source for cultivating Chlorella Protothecoides, an algae strain known for thriving under heterotrophic conditions. Microalgae is often employed for CO 2 capture, biofuel production and most importantly, it can be processed for antioxidants and lipids. These products are often found in health supplements and food additives, with a current market value of US$2.1 billion. Determine: Feasibility of recycled biodiesel glycerol as an alternative carbon substrate to glucose in microalgal biomass production The effect of changing glycerol to glucose ratios in achieving an optimal condition for maximizing biomass production (100:0, 25:75, 50:50, 25:75, 0:100) Interplay of nitrogen deficiency on optimal glycerol to glucose ratio (10:1, 40:1, 80:1,120:1) 0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8 2 A B C D E Biomass (g/100ml) Flask Biomass A B C D E Figure 3: Absorbance profile for nitrogen-deficient culture. D (25:75) exhibits high productivity during exponential phase only Figure 4: Preferential uptake of substrate, 50:50 Glycerol to Glucose Figure 6:Biomass 25:75, C to N 80:1 Trial Evaluate Antioxidant, Chlorophyll-A, Chlorophyll-B and lipid compositions of extractable biomass Characterize and create Kinetic model of optimal ratio between substrates and nitrogen Additional trials to confirm finding and recalibrate results [1]. Heredia-Arroyo, T., Wei, W., & Hu, B. (2010). Oil accumulation via heterotrophic/mixotrophic Chlorella protothecoides. Applied biochemistry and biotechnology, 162(7), 1978-1995. [2]. Shi, X. M., Zhang, X. W., & Chen, F. (2000). Heterotrophic production of biomass and lutein by Chlorella protothecoides on various nitrogen sources. Enzyme and Microbial Technology, 27(3), 312-318. [3]. Shi, X. M., Liu, H. J., Zhang, X. W., & Chen, F. (1999). Production of biomass and lutein by Chlorella protothecoides at various glucose concentrations in heterotrophic cultures. Process biochemistry, 34(4), 341-347. [4]. O’Grady, J., & Morgan, J. A. (2011). Heterotrophic growth and lipid production of Chlorella protothecoides on glycerol. Bioprocess and Biosystems engineering, 34(1), 121-125. [5]. Chen, Y. H., & Walker, T. H. (2011). Biomass and lipid production of heterotrophic microalgae Chlorella protothecoides by using biodiesel-derived crude glycerol. Biotechnology letters, 33(10), 1973-1983. [6]. Cerón-García, M. C., Macías-Sánchez, M. D., Sánchez-Mirón, A., García-Camacho, F., & Molina-Grima, E. (2013). A process for biodiesel production involving the heterotrophic fermentation of Chlorella protothecoides with glycerol as the carbon source. Applied Energy, 103, 341-349 Substrate Consumption Figure 5: Liquid Chromatograph of medium supernatant Optimal ratios are 25:75 Glycerol to Glucose, 10:1 Carbon to Nitrogen 25:75 Glycerol to Glucose exhibits highest productivity rate Nitrogen deficiency results in Biomass reduction Glycerol maintains Chlorophyll pigment within Chlorella protothecoides Glycerol rich cultures are more resistant to contamination Figure 9: (Top) Healthy culture vs. (Bottom) Contaminated culture Growth Rate Biomass and Antioxidant 1.189956 2.63235 0.405836 0.517534 1.936099 2.52036 0 1 2 3 4 5 6 B1 B2 μmol T/g Flasks Antioxidant Content Hexane Ethyl Acetate Water Figure 2: Absorbance profile for nitrogen-rich cultures. D (25:75) Culture exhibits high productivity during exponential phase and stagnation phase . Figure 7: Antioxidant content for Glucose/Glycerol 25:75, C to N 80:1 Trial I would like to thank everyone in the Bioprocess Development lab for their insight and guidance. Optimal Culture Figure 1: Chlorella protothecoides Figure 8: Top (Day 3), Bottom (Day 9) Variation in Chlorophyll content as a function of Glycerol to Glucose ratio. 100 : 0 Glycerol:Glucose 0:100 0 5 10 15 20 25 0 2 4 6 8 10 12 14 16 0 1 2 3 4 5 6 7 8 9 GLYCCEROL-GLUCOSE CONSUMPTION (G/L) DRY WEIGTH (GR/LT) TIME (DAYS) Biomass and Glycerol/Glucose Consumption V.S Time Biomass C GLY C GLU Glycerol Glucose 0 2 4 6 8 10 12 14 16 18 0 1 2 3 4 5 6 7 8 9 10 ABSORBANCE TIME (DAYS) ABSORBANCE V.S TIME 0 2 4 6 8 10 12 14 16 18 0 1 2 3 4 5 6 7 8 9 10 ABSORBANCCE TIME (DAYS) ABSORBANCE V.S TIME NITROGEN RICH NITROGEN DEFICIENT Medium Preparation Algal Cultivation Inoculum Sample Absorbance Centrifugation Biomass Dry Weight HPLC Analysis Sterilization Supernatant Filter Dry Oven

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Page 1: The Green Solution-Optimizing productivity of bi-substate microalgae cultures

The Green Solution Optimizing productivity of bi-substrate microalgae culturesLeng,M., Ibarra-Vidal,M., De la Hoz Siegler, H.

Department of Chemical and Petroleum Engineering

Background

Goal

Results

Contact Information: [email protected]

Materials and Methods

Conclusions

Future Work

References

Acknowledgements

Glycerol is a waste generated from biodieselproduction. We can capitalize on its low-costand availability by utilizing it as a carbon sourcefor cultivating Chlorella Protothecoides, analgae strain known for thriving underheterotrophic conditions. Microalgae is oftenemployed for CO2 capture, biofuel productionand most importantly, it can be processed forantioxidants and lipids. These products areoften found in health supplements and foodadditives, with a current market value ofUS$2.1 billion.

Determine:• Feasibility of recycled biodiesel glycerol as an

alternative carbon substrate to glucose in microalgal biomass production

• The effect of changing glycerol to glucose ratios in achieving an optimal condition for maximizing biomass production (100:0, 25:75, 50:50, 25:75, 0:100)

• Interplay of nitrogen deficiency on optimal glycerol to glucose ratio (10:1, 40:1, 80:1,120:1)

0

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

1.8

2

A B C D E

Bio

mas

s (g

/10

0m

l)

Flask

Biomass

A B C D E

Figure 3: Absorbance profile for nitrogen-deficient culture.D (25:75) exhibits high productivity during exponential phase only

Figure 4: Preferential uptake of substrate, 50:50 Glycerol to Glucose

Figure 6:Biomass 25:75, C to N 80:1 Trial

• Evaluate Antioxidant, Chlorophyll-A, Chlorophyll-B and lipid compositions of extractable biomass

• Characterize and create Kinetic model of optimal ratio between substrates and nitrogen

• Additional trials to confirm finding and recalibrate results

[1]. Heredia-Arroyo, T., Wei, W., & Hu, B. (2010). Oil accumulation via heterotrophic/mixotrophic Chlorella protothecoides. Applied biochemistry and biotechnology, 162(7), 1978-1995.[2]. Shi, X. M., Zhang, X. W., & Chen, F. (2000). Heterotrophic production of biomass and lutein by Chlorella protothecoides on various nitrogen sources. Enzyme and Microbial Technology, 27(3), 312-318.[3]. Shi, X. M., Liu, H. J., Zhang, X. W., & Chen, F. (1999). Production of biomass and lutein by Chlorella protothecoides at variousglucose concentrations in heterotrophic cultures. Process biochemistry, 34(4), 341-347.[4]. O’Grady, J., & Morgan, J. A. (2011). Heterotrophic growth and lipid production of Chlorella protothecoides on glycerol. Bioprocess and Biosystems engineering, 34(1), 121-125.[5]. Chen, Y. H., & Walker, T. H. (2011). Biomass and lipid production of heterotrophic microalgae Chlorella protothecoides by using biodiesel-derived crude glycerol. Biotechnology letters, 33(10), 1973-1983.[6]. Cerón-García, M. C., Macías-Sánchez, M. D., Sánchez-Mirón, A., García-Camacho, F., & Molina-Grima, E. (2013). A process for biodiesel production involving the heterotrophic fermentation of Chlorella protothecoides with glycerol as the carbon source. Applied Energy, 103, 341-349

Substrate Consumption

Figure 5: Liquid Chromatograph of medium supernatant

• Optimal ratios are 25:75 Glycerol to Glucose, 10:1 Carbon to Nitrogen

• 25:75 Glycerol to Glucose exhibits highest productivity rate

• Nitrogen deficiency results in Biomass reduction

• Glycerol maintains Chlorophyll pigment within Chlorella protothecoides

• Glycerol rich cultures are more resistant to contamination

Figure 9: (Top) Healthy culture vs. (Bottom) Contaminated culture

Growth Rate

Biomass andAntioxidant

1.189956

2.632350.405836

0.5175341.936099

2.52036

0

1

2

3

4

5

6

B1 B2

µm

ol T

/g

Flasks

Antioxidant Content

Hexane Ethyl Acetate Water

Figure 2: Absorbance profile for nitrogen-rich cultures. D (25:75) Culture exhibits high productivity during exponential phase and stagnation phase

.

Figure 7: Antioxidant content for Glucose/Glycerol 25:75, C to N 80:1 Trial I would like to thank everyone in the Bioprocess Development lab for their insight and guidance.

Optimal Culture

Figure 1: Chlorella protothecoides

Figure 8: Top (Day 3), Bottom (Day 9) Variation in Chlorophyll content as a function of Glycerol to Glucose ratio.

100 : 0

Glycerol:Glucose

0:100

0

5

10

15

20

25

0

2

4

6

8

10

12

14

16

0 1 2 3 4 5 6 7 8 9

GLY

CC

ERO

L-G

LUC

OSE

CO

NSU

MP

TIO

N (

G/L

)

DR

Y W

EIG

TH (

GR

/LT)

TIME (DAYS)

Biomass and Glycerol/Glucose ConsumptionV.S Time

Biomass C GLY C GLU

Glycerol

Glucose

0

2

4

6

8

10

12

14

16

18

0 1 2 3 4 5 6 7 8 9 10

AB

SOR

BA

NC

E

TIME (DAYS)

ABSORBANCE V.S TIME

0

2

4

6

8

10

12

14

16

18

0 1 2 3 4 5 6 7 8 9 10

AB

SOR

BA

NC

CE

TIME (DAYS)

ABSORBANCE V.S TIME

NITROGEN RICH NITROGEN DEFICIENT

MediumPreparation

AlgalCultivation

Inoculum

Sample

Absorbance

Centrifugation

Biomass

Dry Weight

HPLC Analysis

Sterilization

Supernatant

Filter

Dry Oven