2021
DOI: 10.1016/j.ymben.2020.11.007
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Protocatechuate overproduction by Corynebacterium glutamicum via simultaneous engineering of native and heterologous biosynthetic pathways

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Cited by 27 publications
(30 citation statements)
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“…C. glutamicum shows stable growth to high cell densities (Riesenberg and Guthke, 1999;Pfeifer et al, 2017) and has been engineered for production of, e.g., N-functionalized amino acids (Mindt et al, 2020), diamines (Wendisch et al, 2018;Chae et al, 2020), alcohols (Jojima et al, 2015;Siebert and Wendisch, 2015), and organic acids (Wieschalka et al, 2013;Purwanto et al, 2018). With respect to production of molecules originating from the shikimate or isoprenoid pathways, metabolic engineering enabled production of terpenoids such as pinene (Kang et al, 2014), patchoulol (Henke et al, 2018), valencene (Frohwitter et al, 2014), or various carotenoids (Heider et al, 2014b,c;Henke et al, 2016) and of aromatic or aromatic-derived compounds such as muconic acid (Becker et al, 2018;Shin et al, 2018), phenylpropanoids (Kallscheuer et al, 2016(Kallscheuer et al, , 2017, 4-aminobenzoate (Kubota et al, 2016), shikimate (Sato et al, 2020), protocatechuate (Kogure et al, 2020), 4-hydroxybenzyl alcohol (Kim et al, 2020), and pHBA (Kitade et al, 2018;Purwanto et al, 2018).…”
Section: Introductionmentioning
confidence: 99%
“…C. glutamicum shows stable growth to high cell densities (Riesenberg and Guthke, 1999;Pfeifer et al, 2017) and has been engineered for production of, e.g., N-functionalized amino acids (Mindt et al, 2020), diamines (Wendisch et al, 2018;Chae et al, 2020), alcohols (Jojima et al, 2015;Siebert and Wendisch, 2015), and organic acids (Wieschalka et al, 2013;Purwanto et al, 2018). With respect to production of molecules originating from the shikimate or isoprenoid pathways, metabolic engineering enabled production of terpenoids such as pinene (Kang et al, 2014), patchoulol (Henke et al, 2018), valencene (Frohwitter et al, 2014), or various carotenoids (Heider et al, 2014b,c;Henke et al, 2016) and of aromatic or aromatic-derived compounds such as muconic acid (Becker et al, 2018;Shin et al, 2018), phenylpropanoids (Kallscheuer et al, 2016(Kallscheuer et al, , 2017, 4-aminobenzoate (Kubota et al, 2016), shikimate (Sato et al, 2020), protocatechuate (Kogure et al, 2020), 4-hydroxybenzyl alcohol (Kim et al, 2020), and pHBA (Kitade et al, 2018;Purwanto et al, 2018).…”
Section: Introductionmentioning
confidence: 99%
“…The strains constructed here also allowed for xylose-based production of NMePhe. Xylose is a major constituent of lignocellulose hydrolysates [66] and is an abundant and renewable feedstock for many biotechnological processes [67]. Xylose cannot be catabolized by Saccharomyces cerevisiae [66,68] Zymomonas mobilis [69] or C. glutamicum [50,51].…”
Section: Discussionmentioning
confidence: 99%
“…glutamicum MB001(DE3) prophage-free derivative of ATCC 13032 with chromosomal expression of the T7 RNA polymerase gene under control of P lacUV5 (IPTG-inducible) [15] DelAro 5 C7 P O6 -iolT1 MB001(DE3) derivative with in-frame deletions of cg0344-cg0347, cg2625-cg2640, cg1226, cg0502, and cg3349-cg3354 combined with an exchange of the native promoter of the citrate synthase gene gltA by the dapA promoter variant C7 as well as two point mutations in the promoter of the inositol transporter gene iolT1 that abolishes repression of iolT1 by the regulator protein IolR [16] DelAro 5 C7 P O6 -iolT1 Δpyk derivative of DelAro 5 C7 P O6 -iolT1 with in-frame deletion of pyk (cg2291) coding for the pyruvate kinase This study PCA GLC DelAro 5 C7 P O6 -iolT1 derivative harboring the plasmids pMKEx2_aroF*-qsuB and pEKEx3_tkt [16] PCA GLC Δpyk PCA GLC derivative with in-frame deletion of pyk (cg2291) encoding for the pyruvate kinase This study PCA tamicum is capable of utilizing PCA as sole carbon and energy source [19,20] and in both approaches followed by Okai and co-workers, the natural PCA catabolism of C. glutamicum was not inactivated. Most recently, a high-titer production process for PCA from -glucose was presented [21]. For reaching the reported titer of 82.7 g L −1 PCA a two-step fermentation approach was applied.…”
Section: Strainmentioning
confidence: 99%
“…A production titer of 1.1 g L −1 PCA was reported after 96 h of fed-batch cultivation using a mini-jar fermenter containing a complex medium [17]. Most recently, by following a two-step fed-batch approach, a much higher titer of 82.7 g L −1 PCA was realized [21]. In this approach, the engineered strain was first grown to high cell density using complex medium, and then the biotransformation step was started from 10 % (w v −1 ) of the harvested biocatalyst.…”
Section: Development Of a One-pot Pca Production Processmentioning
confidence: 99%
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