1
Key stress factors and parameters for batch production optimisation of silk-elastin-like proteins in E. coli Tony Collins, João Azevedo-Silva, André da Costa, Raul Machado, Margarida Casal Centre of Molecular and Environmental Biology (CBMA), Department of Biology, University of Minho, Campus de Gualtar, 4710-057 Braga, Portugal. Conclusions Maximum SELP production in shake flasks was obtained with terrific broth at 37ºC, pH7.0 with a liquid vol.:vessel vol. ratio of 1:10 and an agitation speed of 200 rpm. Maximum induction is obtained at the end of the declining exponential phase with an induction period of at least 4 hours. This allows for high cell density on induction and reduces the rate of plasmid loss after induction. Production levels of approximately 500 mg/L were obtained after purification. Rapid degradation of the selection agent used, plasmid instability on induction and high acetate byproduct formation are the principal factors preventing further improved production levels with the expression system used. We are presently investing the fed-batch approach for overcoming some of these restraints and to further increase production levels of the novel SELP. Introduction - Silk-elastin-like proteins (SELPs) are a family of biopolymers based on the highly repetitive amino acid sequence blocks of the naturally occurring fibrous proteins silk and elastin.. - In contrast to conventional synthetic polymers, the composition, sequence and length of these biopolymers can be strictly controlled, leading to monodispersed, precisely defined polymers which can be biosynthesised in an ecologically friendly manner, are biodegradable and biocompatible. - SELPs combining the physicochemical and biological properties of the high tensile strength silk with highly resilient elastin allow for the fabrication of diverse materials with a high potential for use in the pharmaceutical, regenerative medicine and materials fields, yet their development for use is restrained by their typically low production levels. - A series of novel SELPs composed of multiple blocks of the silkworm silk consensus sequence GAGAGS in various combinations with a mutated variant (VPAVG) of the natural mammalian elastin repetitive sequence block VPGVG have recently been prepared. - The genes encoding the newly designed SELPs have been synthesised and the novel recombinant polymers expressed in E. coli by use of the pET25b-E. coli BL21(DE3) expression system. Aims - To optimise the shake flask production levels of the novel SELP (S 5 E 9 ) 10 by means of a comprehensive empirical approach examining all process variables (see 1 to 4 below). - To obtain a better understanding of the factors limiting further improved recombinant protein production of shake flask cultivations with the expression system used (see 5 to 7 below). 1 . Culture Medium Highest biomass and SELP production were observed with rich buffered media such as terrific broth (TB) and super broth (SB). Variation of the sugar supplement in TB, modification of its ingredient concentrations, or use of additives such as ammonium, various amino acids, magnesium or NaCl did not improve production levels further. 2 . Temperature 37 42ºC allowed for highest production levels Highest biomass production was observed at 25ºC but SELP production was low, possibly due to repression of the T7-based expression system at this temperature. Upshifts in temperature on induction did not lead to significantly higher production levels . 0 2 4 6 8 10 12 14 16 18 0 20 40 60 80 100 120 LB LBM TB TBlac TBmod TBaim SB Sbmod SBaim Sbenrich SOC NBS NBSmod ZYB ZYBbuff M9 Ries Max. A600nm, Min. pH SELP Production: % of Max. Medium SELP Prod.: % of Maximum Max. A600nm Minimum pH 0 5 10 15 20 0 20 40 60 80 100 120 25 30 37 42 25-30 25-37 30-37 37-30 37-42 Maxumum OD600nm SELP Production: % of Max. Temperature PBP Prod. (% of Maximum) Maximum OD600nm 3 . Available Oxygen Increasing aeration, or oxygen transfer efficiency, as indicated by increasing flask vol. to liquid vol. ratio and increasing agitation, correlated with improved biomass and SELP levels up to a limit. At higher aeration rates toxic byproduct production (e.g. acetate) due to the higher growth rates observed probably interfere with production. 0 2 4 6 8 10 12 14 16 0 20 40 60 80 100 120 0 5 10 15 20 Maximum OD600nm SELP Production: % of Max. Ratio of Flask Volume to Medium Volume Flask Volume: Medium Volume Optimisation SELP Production: % of Maximum Max. A600nm 0 2 4 6 8 10 12 14 16 0 20 40 60 80 100 120 80 120 160 200 240 Maximum OD600nm SELP Production: % of Max. Agitation (rpm) Agitation SELP Production: % of Maximum Max. A600nm Fig. 4: - Effect of varying the agitation rate on biomass and SELP production.. Fig. 3 - Effect of varying the flask volume to culture medium volume ratio on biomass and SELP production. 4 . Induction In contrast to most studies which induce during the mid-log phase, we observed maximum production with induction at the end of the declining exponential phase. At least four hours induction is recommended for maximum production. 0 2 4 6 8 10 12 14 16 0 20 40 60 80 100 120 2 4 6 8 10 14 Maximum OD600nm SELP Production: % of Max. Time of Induction (hrs.) Induction Time and Induction Period SELP Production: 2 hrs. Induction SELP Production: 4 hrs. Induction SELP Production: 6 hrs. Induction Maximum OD600nm 0,1 1 10 0 2 4 6 8 10 12 14 OD600nm Time (hrs.) Growth Curve of Uninduced E.coli BL21(DE3) OD600nm 5 . Acetate Production Glycerol levels rapidly decrease during the process with a concomitant accumulation of acetate to approximately 5 g/l and a decrease of pH. At low glycerol concentrations the cells switch to a utilisation of the accumulated acetate with an accompanying pH increase. This accumulated acetate provides the carbon source during recombinant protein production. As little as 1 g/L acetate has a bacteriostatic effect while concentrations higher than 4 g/L have a bactericidal effect on the host under the conditions used. 0,1 1 10 100 0 1 2 3 4 5 6 7 8 9 0 2 4 6 8 10 12 14 16 18 20 22 24 26 OD600nm Concentration (g/L) Time (hrs) Glycerol Acetate pH OD600nm 0,1 1 10 0 2 4 6 8 10 12 OD600nm Time (hrs.) TB 0.5 g/l HOAc 1.0 g/l HOAc 1.5 g/l HOAc 2 g/l HOAc 3 g/l HOAc 4 g/l HOAc 5 g/l HOAc 6 g/l HOAc 7 . Plasmid Stability Induction with IPTG leads to rapid loss of plasmid. Plasmid stability remains at maximum for the duration of cultivation in the absence of induction. Induction at the later stages of the growth curve leads to slower loss of plasmid. 0 20 40 60 80 100 0 2 4 6 8 10 12 14 16 18 20 % plasmid bearing cells Incubation Time (hrs.) 2h 4h 8h Non Induced Cultures Fig. 6: Monitoring of glycerol (HPLC), acetate (HPLC) and biomass levels (OD600nm) as well as pH as a function of incubation time using the optimised process conditions for SELP production. The vertical line at 8 hours marks the point of induction with 0.5mM IPTG. Fig. 7 - Effect of acetic acid , added at 0 hours, on growth of E. coli BL21 DE3(+)/pET25b/SELP3 under the optimised shake flask conditions of the present study. 6 . Selection Agent Concentration The ampicillin concentration rapidly decreases during the first hour of cultivation and is already depleted at a culture OD600nm of approximately 0.2. β-lactamase encoded on the pET expression vector used leads to the observed degradation of the selection agent. Productions without the use of a selection agent have allowed for similar SELP production levels to those with ampicillin. Fig. 1: Media Optimisation. SELP production, expressed as a percentage of the maximum, biomass production (OD600nm) and minimum pH measured, as a function of the culture medium used. SELP production levels evaluated by SDS-PAGE. Fig. 2: Effect of temperature on biomass and SELP production. The right hand side of the curve (25-30, 25- 37, 30-37, 37-30, 37-42) represent the temperature shift experiments: the initial temperatures used and the temperatures used after induction. Fig. 5 - Effect of induction time and induction period on biomass and SELP production. SELP and biomass production as a function of IPTG induction time (2-14 hrs. incubation) and induction period (2, 4 and 6 hrs.) (top). Growth curve of uninduced E.coli BL21(DE3) for comparison of the induction time with the stage of growth (bottom). Fig. 8: Ampicillin concentration (measured by the Kirby Bauer assay) and biomass levels as a function of incubation time Fig. 8: Plasmid stability, with and without induction, at various time points during the cultivation. Cultures induced at 2, 4 and 8 hours (as indicated by the arrow) as well as non-induced cultures are compared. 0 20 40 60 80 100 0 0,05 0,1 0,15 0,2 0,25 0,3 0,35 0,4 0 50 100 150 200 0 20 40 60 80 100 OD600nm Ampicillin Concentration (μg/ml) Incubation Time (mins.) Amp. Concentration OD600nm This work was financed by the European Commission via the 7 th Framework Programme Project EcoPlast (FP7-NMP-2009-SME-3, collaborative project number 246176).

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Page 1: Key stress factors and parameters for batch production ...repositorium.sdum.uminho.pt/bitstream/1822/15993/1... · 25 30 37 42 25-30 25-37 30-37 37-30 37-42 OD600nm x. Temperature

Key stress factors and parameters for batch production

optimisation of silk-elastin-like proteins in E. coli Tony Collins, João Azevedo-Silva, André da Costa, Raul Machado, Margarida Casal

Centre of Molecular and Environmental Biology (CBMA), Department of Biology, University of Minho, Campus de Gualtar, 4710-057 Braga, Portugal.

Conclusions

Maximum SELP production in shake flasks was obtained with terrific broth at 37ºC, pH7.0 with a liquid vol.:vessel vol. ratio of 1:10 and an agitation speed of 200 rpm.

Maximum induction is obtained at the end of the declining exponential phase with an induction period of at least 4 hours. This allows for high cell density on induction and

reduces the rate of plasmid loss after induction.

Production levels of approximately 500 mg/L were obtained after purification.

Rapid degradation of the selection agent used, plasmid instability on induction and high acetate byproduct formation are the principal factors preventing further improved

production levels with the expression system used.

We are presently investing the fed-batch approach for overcoming some of these restraints and to further increase production levels of the novel SELP.

Introduction - Silk-elastin-like proteins (SELPs) are a family of biopolymers based on the highly repetitive amino acid sequence blocks of the naturally occurring fibrous proteins silk and elastin..

- In contrast to conventional synthetic polymers, the composition, sequence and length of these biopolymers can be strictly controlled, leading to monodispersed, precisely defined

polymers which can be biosynthesised in an ecologically friendly manner, are biodegradable and biocompatible.

- SELPs combining the physicochemical and biological properties of the high tensile strength silk with highly resilient elastin allow for the fabrication of diverse materials with a high

potential for use in the pharmaceutical, regenerative medicine and materials fields, yet their development for use is restrained by their typically low production levels.

- A series of novel SELPs composed of multiple blocks of the silkworm silk consensus sequence GAGAGS in various combinations with a mutated variant (VPAVG) of the natural

mammalian elastin repetitive sequence block VPGVG have recently been prepared.

- The genes encoding the newly designed SELPs have been synthesised and the novel recombinant polymers expressed in E. coli by use of the pET25b-E. coli BL21(DE3) expression

system.

Aims - To optimise the shake flask production levels of the novel SELP (S5E9)10 by means of a comprehensive empirical approach examining all process variables (see 1 to 4 below).

- To obtain a better understanding of the factors limiting further improved recombinant protein production of shake flask cultivations with the expression system used (see 5 to 7 below).

1. Culture Medium

• Highest biomass and SELP

production were observed with rich

buffered media such as terrific broth

(TB) and super broth (SB).

• Variation of the sugar supplement in

TB, modification of its ingredient

concentrations, or use of additives

such as ammonium, various amino

acids, magnesium or NaCl did not

improve production levels further.

2. Temperature

• 37 – 42ºC allowed for highest

production levels

• Highest biomass production was

observed at 25ºC but SELP production

was low, possibly due to repression of

the T7-based expression system at this

temperature.

• Upshifts in temperature on induction

did not lead to significantly higher

production levels.

0

2

4

6

8

10

12

14

16

18

0

20

40

60

80

100

120

LB LBM

TB TBlac

TBm

od

TBaim

SB Sbm

od

SBaim

Sben

rich

SOC

NB

S

NB

Smo

d

ZYB

ZYBb

uff

M9

Ries

Max. A

60

0n

m, M

in. p

H

SELP

Pro

du

ctio

n: %

of

Max

.

Medium SELP Prod.: % of Maximum Max. A600nm Minimum pH

0

5

10

15

20

0

20

40

60

80

100

120

25 30 37 42 25-30 25-37 30-37 37-30 37-42

Maxu

mu

m O

D6

00

nm

SELP

Pro

du

ctio

n: %

of

Max

.

Temperature

PBP Prod. (% of Maximum) Maximum OD600nm

3. Available Oxygen

• Increasing aeration, or oxygen transfer efficiency, as

indicated by increasing flask vol. to liquid vol. ratio

and increasing agitation, correlated with improved

biomass and SELP levels up to a limit.

• At higher aeration rates toxic byproduct production

(e.g. acetate) due to the higher growth rates observed

probably interfere with production.

0

2

4

6

8

10

12

14

16

0

20

40

60

80

100

120

0 5 10 15 20

Maxim

um

OD

60

0n

m

SELP

Pro

du

ctio

n: %

of

Max

.

Ratio of Flask Volume to Medium Volume

Flask Volume: Medium Volume Optimisation

SELP Production: % of Maximum Max. A600nm

0

2

4

6

8

10

12

14

16

0

20

40

60

80

100

120

80 120 160 200 240

Maxim

um

OD

60

0n

m

SELP

Pro

du

ctio

n: %

of

Max

.

Agitation (rpm)

Agitation

SELP Production: % of Maximum Max. A600nm

Fig. 4: - Effect of

varying the agitation

rate on biomass and

SELP production..

Fig. 3 - Effect of varying

the flask volume to culture

medium volume ratio on

biomass and SELP

production.

4. Induction

• In contrast to most studies which induce

during the mid-log phase, we observed

maximum production with induction at the

end of the declining exponential phase.

• At least four hours induction is

recommended for maximum production.

0

2

4

6

8

10

12

14

16

0

20

40

60

80

100

120

2 4 6 8 10 14

Maxim

um

OD

60

0n

m

SELP

Pro

du

ctio

n: %

of

Max

.

Time of Induction (hrs.)

Induction Time and Induction Period

SELP Production: 2 hrs. Induction SELP Production: 4 hrs. Induction

SELP Production: 6 hrs. Induction Maximum OD600nm

0,1

1

10

0 2 4 6 8 10 12 14

OD

60

0n

m

Time (hrs.)

Growth Curve of Uninduced E.coli BL21(DE3)

OD600nm

5. Acetate Production

• Glycerol levels rapidly decrease during the process with a concomitant

accumulation of acetate to approximately 5 g/l and a decrease of pH.

• At low glycerol concentrations the cells switch to a utilisation of the accumulated

acetate with an accompanying pH increase. This accumulated acetate provides the

carbon source during recombinant protein production.

• As little as 1 g/L acetate has a bacteriostatic effect while concentrations higher

than 4 g/L have a bactericidal effect on the host under the conditions used.

0,1

1

10

100

0

1

2

3

4

5

6

7

8

9

0 2 4 6 8 10 12 14 16 18 20 22 24 26

OD

60

0n

m

Co

nce

ntr

atio

n (

g/L)

Time (hrs) Glycerol Acetate pH OD600nm

0,1

1

10

0 2 4 6 8 10 12

OD

60

0n

m

Time (hrs.)

TB 0.5 g/l HOAc 1.0 g/l HOAc 1.5 g/l HOAc 2 g/l HOAc

3 g/l HOAc 4 g/l HOAc 5 g/l HOAc 6 g/l HOAc

7. Plasmid Stability

• Induction with IPTG leads to rapid loss of

plasmid.

• Plasmid stability remains at maximum for the

duration of cultivation in the absence of

induction.

• Induction at the later stages of the growth

curve leads to slower loss of plasmid.

0

20

40

60

80

100

0 2 4 6 8 10 12 14 16 18 20

% p

lasm

id b

ear

ing

cells

Incubation Time (hrs.)

2h 4h 8h Non Induced Cultures

Fig. 6: Monitoring of glycerol (HPLC), acetate

(HPLC) and biomass levels (OD600nm) as well as

pH as a function of incubation time using the

optimised process conditions for SELP production.

The vertical line at 8 hours marks the point of

induction with 0.5mM IPTG.

Fig. 7 - Effect of acetic acid , added at 0 hours, on

growth of E. coli BL21 DE3(+)/pET25b/SELP3

under the optimised shake flask conditions of the

present study.

6. Selection Agent Concentration

• The ampicillin concentration rapidly decreases

during the first hour of cultivation and is

already depleted at a culture OD600nm of

approximately 0.2.

• β-lactamase encoded on the pET expression

vector used leads to the observed degradation of

the selection agent.

• Productions without the use of a selection agent

have allowed for similar SELP production

levels to those with ampicillin.

Fig. 1: Media Optimisation. SELP production,

expressed as a percentage of the maximum, biomass

production (OD600nm) and minimum pH measured, as

a function of the culture medium used. SELP

production levels evaluated by SDS-PAGE.

Fig. 2: Effect of temperature on biomass and SELP

production. The right hand side of the curve (25-30, 25-

37, 30-37, 37-30, 37-42) represent the temperature shift

experiments: the initial temperatures used and the

temperatures used after induction.

Fig. 5 - Effect of induction time and induction period on

biomass and SELP production.

SELP and biomass production as a function of IPTG induction time

(2-14 hrs. incubation) and induction period (2, 4 and 6 hrs.) (top).

Growth curve of uninduced E.coli BL21(DE3) for comparison of

the induction time with the stage of growth (bottom).

Fig. 8: Ampicillin concentration (measured by the Kirby Bauer

assay) and biomass levels as a function of incubation time Fig. 8: Plasmid stability, with and without induction, at various

time points during the cultivation.

Cultures induced at 2, 4 and 8 hours (as indicated by the arrow) as

well as non-induced cultures are compared.

0 20 40 60 80 100

0

0,05

0,1

0,15

0,2

0,25

0,3

0,35

0,4

0

50

100

150

200

0 20 40 60 80 100

OD

60

0n

m

Am

pic

illin

Co

nce

ntr

atio

n (

µg/

ml)

Incubation Time (mins.) Amp. Concentration OD600nm

This work was financed by the European Commission via the 7th Framework Programme Project EcoPlast (FP7-NMP-2009-SME-3, collaborative project number 246176).