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Supplementary data Efficient sophorolipids production via a novel in situ separation technology by Starmerella bombicola Zhaopeng Liu a , Xiwei Tian a, *, Yang Chen a , Yumeng Lin a , Ali Mohsin a , Ju Chu a, * a State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021, Fax: +86-21- 64253702 E-mail address: [email protected] (Xiwei Tian), [email protected] (Ju Chu) Address: P.O. box 329, 130 Meilong Road, State Key Laboratory of Bioreactor Engineering, East China University
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Page 1: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

Supplementary data

Efficient sophorolipids production via a novel in situ separation technology by Starmerella bombicola

Zhaopeng Liua, Xiwei Tiana,*, Yang Chena, Yumeng Lina, Ali Mohsina, Ju Chua,*

a State Key Laboratory of Bioreactor Engineering, East China University of Science

and Technology, Shanghai 200237, China

* Corresponding author: Tel: +86-21-64253021, Fax: +86-21-64253702

E-mail address: [email protected] (Xiwei Tian), [email protected] (Ju Chu)

Address: P.O. box 329, 130 Meilong Road, State Key Laboratory of Bioreactor

Engineering, East China University of Science & Technology, Shanghai 200237, P. R.

China

Page 2: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

Fig. S1. Pictures of broth sample. Broth sample was taken at 83 h in fermentation 1 and

its microscopic image (a) was taken instantly at 1000x by SUNNY BMDH200

microscopy. After standing for 1 min in measuring cylinder, an image (b) was taken.

The oil/SLs ratio was between 0.015-0.020.

Fig. S2. HPLC analysis of SLs components in samples from fermentation 1 and 2. Six

peaks on chromatogram was identified with standards (Sigma). Error bars represent

standard deviations of triplicate tests.

Page 3: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

Fig. S3. The effect of SLs content on frothing. SLs content in tube 1-5 was respectively

139 g/L, 111 g/L, 83 g/L, 56g/L and 28 g/L. Oil of the same ratio (about 0.100) to SLs

was added to each tube. This photo was taken in 1 min after 5 tubes were shaken

vigorously.

Fig. S4. Effect of standing time on cell growth. Broth sample at146 h from fermentation

2 was used as inoculum for fresh medium in 500 mL flask. And the broth was let stand

for 0 min, 20 min, 40 min and 60 min, respectively, before inoculation. Cell

proliferation multiple was calculated as Eq. A.1. Error bars represent standard

deviations of triplicate tests.

Page 4: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

Fig. S5. Feeding strategies of Glc and oil in fermentation 1 and 2. Black represents

fermentation 1 and red represents fermentation 2. Triangle represents Glc and square

represents rapeseed oil.

Equations

Area percent of each peak (%) = An /AT*100 (S1)

where An and AT represent the peak area of each SLs peak on chromatograph and the

total area of all SLs peaks, respectively.

Gas hold up (%) = Hf /Hp*100 (S2)

where Hf and Hp (mm) represent the froth height of the samples in 50 mL measuring

cylinder and the height of crude SLs layer after complete precipitation of the froth,

respectively.

SLs recovery (%) = WSLs-f /WSLs-b *100 (S3)

where WSLs-f and WSLs-b (g) represent the weight of the SLs in the separated froth and in

the broth before each-round separation, respectively.

Glc recovery (%) = Glcup /Glcf *100 (S4)

where Glcup and Glcf (g) represent the total glucose in the upper water layer during cell

recovery and in the separated froth, respectively.

Equation for power number (as below) is used to compare the mixing power input

between fermentation 1 and 2. In both fermentations, density is assumed to be constant

as the existence of oil and SLs leaves little effect on broth density. Considering the

Page 5: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

identical fermenter, stirring diameter is also identical between them. Additionally, the

power number is commonly constant in turbulent regime. Therefore, stirring speed is

the major variable and has an cubic effect on the mixing power input [1].

P = Npρn3D5 (S5)

Where P is power, Np is power number, ρ is density, n is stirrer speed and D is stirrer

diameter.

Page 6: ars.els-cdn.com · Web viewa State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China * Corresponding author: Tel: +86-21-64253021,

Reference

[1] B.M. Dolman, C. Kaisermann, P.J. Martin, J.B. Winterburn, Integrated sophorolipid production and gravity separation, Process Biochem. 54 (2017) 162-171.


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