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Research progress and development trends in the biosynthesis of neutral core human milk oligosaccharides
LIU Dan, WANG Jianyu, JIANG Zhengqiang
Synthetic Biology Journal    2025, 6 (5): 1126-1144.   DOI: 10.12211/2096-8280.2025-083
Abstract   (541 HTML22 PDF(pc) (5130KB)(529)  

Human milk oligosaccharides (HMOs) are essentially functional and nutritional components found in human milk. They can be primarily classified into fucosylated, neutral core, and sialylated HMOs. Lacto-N-triose Ⅱ (LNT Ⅱ), lacto-N-neotetraose (LNnT), and lacto-N-tetraose (LNT) are common neutral core human milk oligosaccharides (ncHMOs), which can be extended to form longer-chain HMOs and play important roles in intestinal health. In recent years, the biosynthesis of ncHMOs has developed rapidly, and industrial-scale production is from theoretical possibility to practical reality. The synthesis approaches for ncHMOs include chemical synthesis, enzymatic synthesis, and microbial cell synthesis. As the rapid development in biotechnology, enzymatic and microbial cell synthesis have emerged as prominent methods in ncHMOs biosynthesis. Enzymatic synthesis is highly efficient, regioselective, and stereoselective. Currently, glycosyltransferases and glycoside hydrolases represent the two major types of enzymes used for biosynthesizing ncHMOs. Glycosidase-based enzymatic synthesis has demonstrated high conversion rates for LNT Ⅱ and LNnT production. However, the enzymatic synthesis of LNT is less efficient and requires further improvement. Notably, the production of LNnT and LNT typically relies on LNT Ⅱ as a key precursor, requiring a multi-step synthetic strategy. Microbial cell synthesis employs metabolic engineering to construct continuously synthetic pathways in microbial cells such as Escherichia coli and Bacillus subtilis. Knocking out genes in competitive pathway, optimizing genes expression, regenerating cofactors have significantly enhanced the yields of ncHMOs. The biosynthesis of ncHMOs faces several critical challenges, including the low activity and poor substrate specificity of key glycosyltransferases, such as β-1,3-N-acetylglucosaminyltransferase and β-1,3-galactosyltransferase. Additionally, the transporters of LNT Ⅱ and LNnT are not clear in microbial cell. Furthermore, the yields of LNT Ⅱ should be substantially improved for industrial-scale production. Thus, it is important to overcome the interconnected limitations in enzyme engineering (particularly glycosyltransferase specificity and activity), microbial cell modification (focusing on metabolic compatibility and pathway design), and bioprocess optimization (through rational pathway redesign) via an integrated synthetic biology and fermentation engineering approach in the future. These strategies are essential for achieving efficient, cost-effective biosynthesis of ncHMO at industrial scale.


菌株改造情况底物发酵条件发酵罐产量/(g/L)参考文献
大肠杆菌(E. coli) JM09pCW-lgtA pBB-lgtB乳糖、葡萄糖pH 6.8、28 ℃、0.2 mmol/L IPTG、矿物培养基<5(2 L)[77]
大肠杆菌(E. coli) BL21(DE3)

ΔwecBΔnagBΔlacZ

pRSF-M-US* pET-lgtA pAC-AagalT(源自A. actinomycetemcomitans NUM4039)

乳糖、甘油pH 6.8、25 ℃、0.2 mmol/L IPTG、甘油优化培养基12.1(3 L)[83]
大肠杆菌(E. coli)BL21 star (DE3)ΔlacZΔugdΔushAΔagpΔwcaJΔotsAΔwcaCΔgalM::galETKM pRSF-lgtA-galE pET-HpgalT(源自Helicobacter pylori乳糖、甘油pH 6.8、28 ℃、0.2 mmol/L IPTG、优化培养基22.07(3 L)[84]
大肠杆菌(E. coli)BL21(DE3)ΔlacZΔwecBΔugdΔgloA pAC-M-US pCD-lgtA-lgtB(源自N. meningitidis乳糖、甘油、25 ℃、0.4 mmol/L IPTG、甘油优化培养基13.25(3 L)[85]
大肠杆菌(E. coli) BL21 MG1655ΔwcaJΔlacZΔP lacY ::PJ23119 pTrc99a-PQS03-lgtA pCD-luxR-P QS33 -luxI-CP(源自S. agalactiae乳糖、甘油pH 6.8、30 ℃、—、甘油优化培养基20.33(5 L)[86]
大肠杆菌(E. coli) K-12 MG1655ΔlacZΔnagBΔugdΔwecB gsK-ybaL:: lgtA-SH3lig- HpGalT-PDZlig-PDZ-SH3 mscK-ybaM::lgtA-SH3lig-HpGalT-PDZlig-PDZ-SH3 Phr-dtpD:: ParaBAD--dCpf1 ΔfliK::PJ23119-pfkA3-zwf P tac ::P mlc乳糖、葡萄糖pH 6.8、30 ℃、0.2 mmol/L IPTG、0.5 mmol/L 阿拉伯糖、葡萄糖优化培养基23.73(3 L)[87]
大肠杆菌(E. coli) BL21(DE3)ΔlacZΔlacAΔwecBΔnagBΔugdΔgcdΔsetA pCD-lgtA-M-U-S* pET-lacY-prs pRSF-lgtB-pgm-galE-galU乳糖、甘油pH 7.2、25 ℃、0.1 mmol/L IPTG、甘油优化培养基19.4(3 L)[88]
大肠杆菌(E. coli)BL21 star (DE3)ΔlacZΔugdΔushAΔagpΔwcaJΔotsAΔwcaCΔgalM::galETK ΔlacA::lgtA-galE Δyjgx::lgtA ΔnagB::HpgalT Δyjiv::HpgalT Δydeu::HpgalT ΔcaiB::HpgalT ΔhlyE::CmSET ΔxylB::galE ΔP galU ::PT7 ΔP glmM ::PT7乳糖、葡萄糖、甘油pH 6.8、29.5 ℃、0.2 mmol/L IPTG、优化培养基112.47(5 L)[89]
大肠杆菌(E. coli) BL21(DE3)ΔlacZΔugdΔwecBΔsetA pCD-lgtA-AagalT pET-galE乳糖、甘油pH 6.8、25 ℃、—、甘油优化培养基15.53(5 L)[90]
大肠杆菌(E. coli)BL21 (DE3)ΔlacZΔlacAΔnagBΔwecB ΔugdΔgcdΔsetAΔiclR pRSF-lgtB-pgm-galU-galE-Galtpm1141 pET-lgtA-M-U-S* pCD-prsA-pgi-glf葡萄糖pH 7.0、25 ℃、0.1 mmol/L IPTG、葡萄糖优化培养基25.4(3 L)[91]
枯草芽孢杆菌(B. subtilis )168

ΔamyE::P43-lacY P43-lgtB/pP43NMK-lgtA

P43-lgtB P43-lgtB P43-pgi P43-gtaB P43-glmS P43-glmM P43-galE ΔtuaD::lox72

乳糖、葡萄糖pH 7.0、37 ℃、120 mmol/L木糖、优化培养基4.52(3 L)[92]
枯草芽孢杆菌(B. subtilis )168

P xylA -comK ΔamyE::P43-lacY 3拷贝P43-lgtB, P43-pgi P43-gtaB P43-glmS P43-glmM

P43-galE pP43NMK-lgtA ΔganA::xylR-P xylA -dCas9

P veg -sgRNA-pfkA7pyk1zwf1 P veg -sgRNA-mnaA2

ΔtuaD::lox72 P43-lgtB

乳糖、葡萄糖pH 7.0、37 ℃、120 mmol/L木糖、优化培养基5.41(3 L)[93]
法夫驹形氏酵母(Komagataella phaffii)168

HIS4::pGAP-hCas9-HIS4::pTEF1-ScRAD52-int11::pGAP-ScRAD59-Int20::pTEF1-ScMRE11

int12::lgtA-lgtB-int21::lac12-intE1::gal10

intE9::pgm-intE26::gfa-intE20-ugp-intE24::gna-intE14::qri-intE13::pcm intE10::lgtA-linker3-lgtB pfk-ɑ::X1 pfk-β::X2

乳糖、葡萄糖、甘油pH 6.5、30 ℃、—、BMGY培养基1.24(3 L)[94]
Table 6 Microbial cell factory for LNnT synthesis
Extracts from the Article
由于大肠杆菌缺乏β-1,3-N-乙酰氨基葡萄糖基转移酶,需将其引入才能利用外源添加的乳糖或N-乙酰氨基葡萄糖和内源合成的UDP-N-乙酰氨基葡萄糖(UDP-GlcNAc)合成LNT Ⅱ(图2)。内源UDP-GlcNAc合成通路包含glmMglmU以及glmS等关键基因,Zhu等[76]利用不同拷贝数质粒微调UDP-GlcNAc合成通路表达强度,并定点突变了glmS以解除前体物GlcN-6-P的反馈抑制,敲除竞争路径中wecBnagB后,5 L发酵罐中LNT Ⅱ产量高达46.2 g/L。乳糖作为合成LNT Ⅱ的直接底物,不同大肠杆菌菌株利用其效果不同。与大肠杆菌BL21(DE3)相比,大肠杆菌JM109需过表达lacY以提高乳糖渗透率[77]。此外,还需敲除lacZ防止乳糖降解[77]。Hu等[78]利用几丁质降解产物GlcNAc为底物,敲除lacZnanE阻断副反应途径减少底物浪费,过表达nagAglmMglmU以增强前体UDP-GlcNAc的供应,通过基因表达优化,3 L发酵罐中LNT Ⅱ产量为15.8 g/L,为利用生物质原料合成HMO提供了新思路。Sugita等[79]过表达大肠杆菌内源转运体基因setA显著提高了LNT Ⅱ产量,但SetA转运LNT Ⅱ具体转运机制尚不清晰。除了改造传统大肠杆菌,还可以改造益生菌大肠杆菌Nissle 1917合成LNT Ⅱ[80]。最近,Li等[81]首先确定了脑膜炎奈瑟氏菌MC58来源的LgtA具有合成LNT Ⅱ优势,基于高通量筛选平台确定高效突变体R13H/L24M/R205C,并在其C端融合InfB促融标签减少了包涵体形成,最后通过RBS工程和优化关键限速酶表达提高了LNT Ⅱ合成水平,在5 L发酵罐中产量达57.44 g/L,为目前报道最高水平。Wang等[82]采用两步法全细胞催化策略,开发了大肠杆菌-酵母耦合系统,以GlcNAc和乳糖为底物在5 L发酵罐中合成了52.34 g/L LNT Ⅱ,乳糖转化率达95.95%。
微生物细胞法合成LNnT是在LNT Ⅱ合成通路的基础上引入异源β-1,4-GalT,催化内源UDP-半乳糖的半乳糖残基转移到LNT Ⅱ上形成LNnT(图2)。目前已报道许多β-1,4-GalT用于LNnT微生物细胞合成,产量在1.24~112.47 g/L(表6)。微生物细胞法合成LNnT的研究较多,已在大肠杆菌、枯草芽孢杆菌、毕赤酵母、酿酒酵母等微生物细胞中实现了LNnT的生物合成。
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