10.1002/cbic.201800157
ChemBioChem
FULL PAPER
De novo Biosynthesis.
This work was supported by the National Science Foundation
(grant 1438332 to W.N. and J.G.; REU grant 1560163) and the
Nebraska Public Power District throutgh the Nebraska Center
For Energy Sciences Research at University of Nebraska –
Lincoln (Cycle-9 grant to J.G. and W.N). The authors would like
to acknowledge assistance from the following individuals at the
University of Nebraska-Lincoln: Prof. David Berkowitz
(Department of Chemistry, chiral HPLC) and Prof. Martha
Morton (Chemistry Research Instrumentation Facility, NMR).
Fermentations were carried out in a 2.0 L working capacity
UniVessel® controlled by a Biostat® B controller (Sartorius AG).
Temperature and pH were controlled with proportional-integral-
derivative (PID) control loops. The temperature was controlled
at 37 °C. The pH was controlled at 7.0 by the addition of acid (2
N H2SO4) and base (concentrated NH4OH at the first stage or
20% NaHCO3 at the second stage). Dissolved oxygen was
measured using an OxyFerm probe. Fed-batch fermentations
were run in duplicate. Results were reported as the average of
the two runs. A seed culture was started by the introduction of a
single colony into 5 mL of M9 glucose medium. Culture was
grown at 37 °C with shaking for 16 h and subsequently
transferred into 95 mL of M9 glucose medium. The culture was
Conflict of interest
The authors declare no conflict of interest.
grown under the same condition for an additional 10 h.
A
fermentation was initiated by transferring the seed culture (100
mL) into the fermentation vessel, which contained the fed-batch
fermentation medium (850 mL) and 20 g of glucose (50 mL).
Keywords: carboxylic acid reductase • biocatalysis • carboxylic
acid • aldehyde • industrial chemical
The total initial volume of the fermentation culture was 1 L.
A
two-stage cultivation scheme was used. In the first stage, the
D.O. was maintained at 10% air saturation through sequential
ramping of impeller speed and airflow rate to the preset values
of 1100 rpm and 1.0 cubic liter per minute, respectively. At this
point, IPTG was added to a final concentration of 0.25 mM.
Following an additional 1 h of cultivation, the microaerobic stage
was initiated by reducing the airflow rate to 50 cubic centimeter
per minute. At the same time, glucose solution (600 g/L) was
fed into the fermenter at a rate of 4.17 g/h for 24 h. Throughout
the second stage, the D.O. value registered as 0% air saturation.
Samples were taken at indicated time points. Cell densities
were determined by measurement of absorption at 600 nm
(OD600). Glucose concentration was monitored by HPLC. Cell-
free broth was obtained for metabolite analysis. Cell pellets
were lysed for protein expression analysis.
[1]
[2]
[3]
R. A. Sheldon, Green Chem. 2014, 16, 950-963.
A. J. J. Straathof, Chem. Rev. 2014, 114, 1871-1908.
W. Niu, J. Guo, S. Van Dien, in Metabolic Engineering for Bioprocess
Commercialization (Ed.: S. Van Dien), Springer International Publishing,
Cham, 2016, pp. 31-52.
[4]
[5]
A. M. Weeks, M. C. Y. Chang, Biochemistry 2011, 50, 5404-5418.
J. W. Lee, D. Na, J. M. Park, J. Lee, S. Choi, S. Y. Lee, Nat. Chem. Biol.
2012, 8, 536-546.
[6]
[7]
[8]
[9]
C. E. Nakamura, G. M. Whited, Curr. Opin. Biotechnol. 2003, 14, 454-
459.
A. Burgard, M. J. Burk, R. Osterhout, S. Van Dien, H. Yim, Curr. Opin.
Biotechnol. 2016, 42, 118-125.
H. White, G. Strobl, R. Feicht, H. Simon, Eur J Biochem 1989, 184, 89-
96.
A. He, T. Li, L. Daniels, I. Fotheringham, J. P. N. Rosazza, Appl.
Environ. Microbiol. 2004, 70, 1874-1881.
Analytical Methods.
[10] B. Soehling, G. Gottschalk, Eur. J. Biochem. 1993, 212, 121-127.
[11] N. A. Leal, G. D. Havemann, T. A. Bobik, Arch. Microbiol. 2003, 180,
353-361.
An Agilent 1260 Infinity HPLC instrument (Agilent Technologies)
equipped with an Aminex HPX-87H column (300x7.8 mm) (Bio-
Rad Laboratories) was used for metabolite identification and
quantification. To prepare samples for analysis, cell-free broth
was mixed with internal standard (100 mM oxalic acid) at 95:5
(v/v) ratio, then filtered through a 0.2 µm PTFE syringe filter. A
10 µL of the prepared sample was injected. Samples were
eluted at 45 °C with 5 mM sulfuric acid (0.6 mL/min). All the
carboxylic acids were detected at 210 nm using a diode array
detector. Alcohols and glucose were detected by a refractive
index detector. Retention times of all analytes are shown in
Table S3 of Supporting Information. 1H NMR spectra were
recorded on a Bruker Avance III-HD NMR Spectrometer (300
MHz) instrument. Samples were prepared by mixing cell-free
broth with D2O at a 9:1 (v/v) ratio. The sodium salt of 3-
(trimethylsilyl)propionic-2,2,3,3-d4 acid (TSP) was included in the
[12] S. Weinitschke, K. Hollemeyer, B. Kusian, B. Bowien, T. H. M. Smits, A.
M. Cook, J. Biol. Chem. 2010, 285, 35249-35254.
[13] J. I. Harris, M. Waters, in The Enzymes, Vol. 13 (Ed.: P. D. Boyer),
Academic, 1976, pp. 1-49.
[14] H. Yim, R. Haselbeck, W. Niu, C. Pujol-Baxley, A. Burgard, J. Boldt, J.
Khandurina, J. D. Trawick, R. E. Osterhout, R. Stephen, J. Estadilla, S.
Teisan, H. B. Schreyer, S. Andrae, T. H. Yang, S. Y. Lee, M. J. Burk, S.
Van Dien, Nat. Chem. Biol. 2011, 7, 445-452.
[15] S. Atsumi, A. F. Cann, M. R. Connor, C. R. Shen, K. M. Smith, M. P.
Brynildsen, K. J. Y. Chou, T. Hanai, J. C. Liao, Metab. Eng. 2008, 10,
305-311.
[16] P. Venkitasubramanian, L. Daniels, J. P. N. Rosazza, J. Biol. Chem.
2007, 282, 478-485.
[17] D. Gahloth, M. S. Dunstan, D. Quaglia, E. Klumbys, M. P. Lockhart-
Cairns, A. M. Hill, S. R. Derrington, N. S. Scrutton, N. J. Turner, D. Leys,
Nat. Chem. Biol. 2017, 13, 975-981.
D2O as the internal standard for calibration.
A solvent
suppression program was applied to suppress the signal of
water. The optical purity analysis of 1,2-PDO from the de novo
biosynthesis was carried out following a previously reported
procedure.[26]
[18] W. Finnigan, A. Thomas, H. Cromar, B. Gough, R. Snajdrova, J. P.
Adams, J. A. Littlechild, N. J. Harmer, ChemCatChem 2017, 9, 1005-
1017.
[19] P. Venkitasubramanian, L. Daniels, J. P. N. Rosazza, in Biocatalysis in
the pharmaceutical and biotechnology industries (Ed.: R. N. Patel),
CRC Press LLC, 2007, pp. 425-440.
Acknowledgements
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