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Detergent assisted lipid extraction for biodiesel.

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Detergent assisted lipid extraction for biodiesel

Sravan kumar yellapu, Bezawada jyothi, R.D.Tyagi

INRS Eau, Terre et Environnement, 490, rue de la Couronne, Québec, Canada, G1K 9A9

Background Problems Objective

Response surface methodology

 Four important parameters

• N-LS concentration

• N-LS volume

• Incubation time

• Incubation temperature

Experimental design Results

Box Bekhen Design

(BBD)

Four

factors

N-LS

(0.5 – 2% w/v

)

N-LS volume

(0.5 – 2 mL

)

Temperature

(25-30

o

C

)

Incubation

time

(5 – 15 min)

0 0.5 0.8 1.1 1.4 1.7 2 0.5 0.8 1.1 1.4 1.7 2 40 50 60 70 80 90 100 110 E xt ra ct io n e ff ici e n c y (% w /w ) A: NLS conc (%) B: NLS volume (mL) 5 8 11 14 17 20 0.5 0.8 1.1 1.4 1.7 2 40 50 60 70 80 90 100 110 E xt ra ct io n e ff ici e n c y (% w /w ) A: NLS conc (%) C: Incubation time (min)

ed value e 25 27 29 31 33 35 0.5 0.8 1.1 1.4 1.7 2 40 50 60 70 80 90 100 110 E xt ra ct io n e ff ici e n c y (% w /w ) A: NLS conc (%) D: Incubation temperature (oC)

5 8 11 14 17 20 0.5 0.8 1.1 1.4 1.7 2 40 50 60 70 80 90 100 110 E xt ra ct io n e ff ici e n c y (% w /w ) B: NLS volume (mL) C: Incubation time (min)

e 25 27 29 31 33 35 0.5 0.8 1.1 1.4 1.7 2 40 50 60 70 80 90 100 110 E xt ra ct io n e ff ici e n c y (% w /w )

B: NLS volume (mL)

D: Incubation temperature (oC)

Figure 2: Response surface plots for lipid extraction efficiency (%w/w) at varying concentrations

Conclusion

N-lauryl sarcosine aided cell disruption and lipid release from the cells followed by lipid extraction

using a lower volume of chloroform and methanol (1:1 v/v) revealed a high lipid extraction

efficiency of 98.2% (w/w

)

References

Martínez EJ, Raghavan V, González-Andrés F & Gómez X (2015) New Biofuel Alternatives: Integrating Waste Management and Single Cell Oil Production. International journal of molecular sciences 16(5):9385-9405

Yadav J, Bezawada J, Yan S, Tyagi RD & Surampalli RY (2014) Permeabilization of Kluyveromyces marxianus with Mild Detergent for Whey Lactose Hydrolysis and Augmentation of Mixed Culture. Applied Biochemistry and Biotechnology 172(6):3207-3222. Zhang X, Yan S, Tyagi RD, Drogui P & Surampalli RY (2014) Ultrasonication assisted lipid extraction from oleaginous microorganisms. Bioresource technology 158:253-261.

Vicente G, Bautista LF, Rodríguez R, Gutiérrez FJ, Sádaba I, Ruiz-Vázquez RM, Torres-Martínez S & Garre V (2009) Biodiesel production from biomass of an oleaginous fungus. Biochemical Engineering Journal 48(1):22-27.

Figure 1: Process flow diagram

Microwave

Pulse Electric Field

Sonication

75 80 85 90 95 100

Mw+ Enzyme PEF sonication CTAB

To ta l l ip id re co ve ry % w /w Treatments

Total lipid recovery % w/w

Literature- Comparision of

different treatments

Soya oil

Animal fats

Algae oil

Oleaginous yeast oil

Schematic diagram of Biodiesel production

Figure 1: Experimental design using Box Bekhen design

i

ii

iii

iv

v

i) NLS conc and NLS volume

ii) NLS conc and incubation time

iii) NLS conc and incubation

temperature

iv) NLS volume and incubation time

v) NLS volume and incubation

temperature

vi) Incubation time and incubation

temperature

Fatty acids

Relative amount of total fatty acid (% w/w)

Conventional chloroform

methanol (2:1 v/v)

N-lauryl sarcosine +

chloroform/methanol

Palmitic acid (C16:0)

17.2

16.2

Palmitoleate (C16:1n7)

0.3

0.3

Stearic (C18:0)

5.1

4.5

Oleic (C18:1n9)

45.6

42.5

Vaccenic (C18:1n7)

1.2

1.1

Linoleic (C18:2n6)

24.7

30.2

Linolenate (C18:3n3)

1.3

1.5

C23:0

4.6

3.7

Table 1: Comparison of fatty acid profiles between conventional and N-lauryl sarcosine

assisted lipid extraction processes

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