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factor κb ligand  (R&D Systems)


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    Structured Review

    R&D Systems factor κb ligand
    Factor κb Ligand, supplied by R&D Systems, used in various techniques. Bioz Stars score: 96/100, based on 174 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
    https://www.bioz.com/result/factor κb ligand/product/R&D Systems
    Average 96 stars, based on 174 article reviews
    factor κb ligand - by Bioz Stars, 2026-05
    96/100 stars

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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different <t>E.</t> <t>coli</t> strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains <t>C600,</t> MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).
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    Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different E. coli strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains C600, MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).

    Journal: Synthetic and Systems Biotechnology

    Article Title: Engineering Escherichia coli for robust Co-utilization of glucose and xylose enables high-titer succinate production from lignocellulosic hydrolysates

    doi: 10.1016/j.synbio.2026.01.006

    Figure Lengend Snippet: Investigation of xylose transport and PTS modification for succinate production. (A) Schematic representation of glucose and xylose transport routes in different E. coli strains, highlighting the key transporters and metabolic nodes influencing carbon flux; (B) Intracellular ATP levels in strains C600, MG1655, and BW25113 during aerobic growth on xylose; (C) Comparison of succinate and by-product accumulation between the parental strain C600 and engineered strain ESC2 under anaerobic conditions; (D) Fermentation performance of PTS-modified strain ESC3, showing sugar utilization, biomass generation, and succinate production; (E–F) Growth profiles of engineered ESC3 derivatives in defined medium with xylose (E) or glucose–xylose mixtures (F). All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗p < 0.01, ∗∗∗p < 0.001).

    Article Snippet: In this study, we systematically engineered E. coli C600 (ATCC 23724) [ ], a strain with efficient and low-energy xylose transport, as the chassis for succinate production from lignocellulosic sugars.

    Techniques: Modification, Comparison, Standard Deviation, Two Tailed Test

    Construction of a succinate-producing strain from C600. (A) Metabolic map illustrating targeted knockouts ( ldhA , pflB , ptsG , adhE and pta-ackA ) and expression/integration of pck to redirect flux toward succinate; (B) Two-stage fermentation scheme comprising aerobic growth using shaking flasks and followed by anaerobic production in serum bottles; (C–D) Succinate fermentation of six engineered strains cultured on xylose (C) or glucose–xylose mixtures (D). All experimental data were performed in triplicate, and error bars represent the standard deviation.

    Journal: Synthetic and Systems Biotechnology

    Article Title: Engineering Escherichia coli for robust Co-utilization of glucose and xylose enables high-titer succinate production from lignocellulosic hydrolysates

    doi: 10.1016/j.synbio.2026.01.006

    Figure Lengend Snippet: Construction of a succinate-producing strain from C600. (A) Metabolic map illustrating targeted knockouts ( ldhA , pflB , ptsG , adhE and pta-ackA ) and expression/integration of pck to redirect flux toward succinate; (B) Two-stage fermentation scheme comprising aerobic growth using shaking flasks and followed by anaerobic production in serum bottles; (C–D) Succinate fermentation of six engineered strains cultured on xylose (C) or glucose–xylose mixtures (D). All experimental data were performed in triplicate, and error bars represent the standard deviation.

    Article Snippet: In this study, we systematically engineered E. coli C600 (ATCC 23724) [ ], a strain with efficient and low-energy xylose transport, as the chassis for succinate production from lignocellulosic sugars.

    Techniques: Expressing, Cell Culture, Standard Deviation

    Evaluation of exogenous xylose utilization pathways and library-based strain selection. (A) Schematic comparison of the endogenous XI pathway with the Dahms and Weimberg pathways; (B) Design of pathway plasmid libraries and RBS variants controlling expression of key genes for Dahms and Weimberg pathways. The Weimberg library plasmid carries XylA , XylX , and XylB from C. crescentus , while the Dahms library plasmid contains XylB from C. crescentus . The helper plasmid harbors xylC from C. crescentus and the endogenous yjhG from E. coli . RBS sequences were designed with 32 mutations, enabling gene expression levels ranging from 4 to 57,523 au; (C) Growth and succinate production of four representative ESC7 derivatives (ESC7-W1, ESC7-W2, ESC7-D1, ESC7-D2), which were randomly selected from the Weimberg (W1, W2) or Dahms (D1, D2) pathway libraries, compared with ESC6 (XI pathway); (D) Fermentation performance of the same four ESC7 clones carrying the helper plasmid (harboring XylC and yjhG ), compared with ESC6; (E) Validation of pathway combinations in the ESC6 background using the same four representative plasmids, integrating XI with Dahms/Weimberg routes and help plasmid; (F) Screening of library colonies identified six optimal variants, which were reconstructed in ESC6 and evaluated for succinate production from glucose–xylose mixtures. All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗∗ p < 0.001).

    Journal: Synthetic and Systems Biotechnology

    Article Title: Engineering Escherichia coli for robust Co-utilization of glucose and xylose enables high-titer succinate production from lignocellulosic hydrolysates

    doi: 10.1016/j.synbio.2026.01.006

    Figure Lengend Snippet: Evaluation of exogenous xylose utilization pathways and library-based strain selection. (A) Schematic comparison of the endogenous XI pathway with the Dahms and Weimberg pathways; (B) Design of pathway plasmid libraries and RBS variants controlling expression of key genes for Dahms and Weimberg pathways. The Weimberg library plasmid carries XylA , XylX , and XylB from C. crescentus , while the Dahms library plasmid contains XylB from C. crescentus . The helper plasmid harbors xylC from C. crescentus and the endogenous yjhG from E. coli . RBS sequences were designed with 32 mutations, enabling gene expression levels ranging from 4 to 57,523 au; (C) Growth and succinate production of four representative ESC7 derivatives (ESC7-W1, ESC7-W2, ESC7-D1, ESC7-D2), which were randomly selected from the Weimberg (W1, W2) or Dahms (D1, D2) pathway libraries, compared with ESC6 (XI pathway); (D) Fermentation performance of the same four ESC7 clones carrying the helper plasmid (harboring XylC and yjhG ), compared with ESC6; (E) Validation of pathway combinations in the ESC6 background using the same four representative plasmids, integrating XI with Dahms/Weimberg routes and help plasmid; (F) Screening of library colonies identified six optimal variants, which were reconstructed in ESC6 and evaluated for succinate production from glucose–xylose mixtures. All experimental data were performed in triplicate, and error bars represent the standard deviation. Statistical analysis was performed using a two-tailed Student's t -test (∗∗∗ p < 0.001).

    Article Snippet: In this study, we systematically engineered E. coli C600 (ATCC 23724) [ ], a strain with efficient and low-energy xylose transport, as the chassis for succinate production from lignocellulosic sugars.

    Techniques: Selection, Comparison, Plasmid Preparation, Expressing, Gene Expression, Clone Assay, Biomarker Discovery, Standard Deviation, Two Tailed Test