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Restek Corporation restek rtx vms capillary column
Restek Rtx Vms Capillary Column, supplied by Restek Corporation, used in various techniques. Bioz Stars score: 86/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/capillary+column+restek+rtx-vms/capillary+column/10__1039_slash_d4gc04832f-70-1-1
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restek rtx vms capillary column - by Bioz Stars, 2026-10
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Article Title: Selective conversion of hemicellulose into furfural over low-cost metal salts in a γ-valerolactone/water solution
Article Snippet: Thermochemical conversion of biomass into platform chemicals and fuels is recognized as the most promising process for the partial substitution of fossil resources.. Notably, selective liquefaction is a critical step for the integrated utilization of waste lignocellulosic biomass resources.. Herein, we demonstrated an efficient and environmentally benign liquefied process for converting hemicellulose and waste lignocellulosic residues into furfural in a γ-valerolactone/water solution using inexpensive Al2(SO4)3 as the catalyst.

Article Title: Characterization of isolated starch from Isatis indigotica Fort. root and anhydro-sugars preparation using its decoction residues
Article Snippet: LGO, HMF, and furfural were analyzed using a GC (Shimadzu, GC-2010 Plus equipped with a flame ionization detector and a Restek RTX-VMS capillary column).

Article Title: Rates of levoglucosanol hydrogenolysis over Brønsted and Lewis acid sites on platinum silica-alumina catalysts synthesized by atomic layer deposition
Article Snippet: Product Analysis Gas chromatography (GC): A Shimadzu GC equipped with flame ionization detector (FID) was used, equipped with a Restek RTX-VMS capillary column (length: 30 m, inner diameter: 0.25 mm, film thickness: 1.4 μm).

Article Title: Effect of carbon supports on RhRe bifunctional catalysts for selective hydrogenolysis of tetrahydropyran-2-methanol
Article Snippet: View Article Online DOI: 10.1039/C6CY01763K liquid products were also analyzed using a gas chromatograph (Shimadzu, GC-2010) equipped with a flame ionization detector (FID) and a Restek RTX-VMS capillary column.



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Restek Corporation restek rtx vms capillary column
Restek Rtx Vms Capillary Column, supplied by Restek Corporation, used in various techniques. Bioz Stars score: 86/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/capillary+column+restek+rtx-vms/capillary+column/10__1039_slash_d4gc04832f-70-1-1
Average 86 stars, based on 1 article reviews
restek rtx vms capillary column - by Bioz Stars, 2026-10
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The influence of different catalysts and concentrations on <t>LG,</t> <t>LGO,</t> total carbon yield. (1) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of 15 mM catalyst (TsOH, MSA, H 2 SO 4 ), and 100 mL Diox. (2) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of H 2 SO 4 concentrations (10 mM, 15 mM, 25 mM, 30 mM), and 100 mL Diox. Note: \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{Total carbon}} \left(\mathrm{\%}\right)$$\end{document} Yield Total carbon % = \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} <t>\begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{HMF}}</t> \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{FF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LG}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LGO}} \left(\mathrm{\%}\right)$$\end{document} Yield HMF % + Yield FF % + Yield LG % + Yield LGO % , and these yields were the highest yield
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The influence of different catalysts and concentrations on <t>LG,</t> <t>LGO,</t> total carbon yield. (1) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of 15 mM catalyst (TsOH, MSA, H 2 SO 4 ), and 100 mL Diox. (2) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of H 2 SO 4 concentrations (10 mM, 15 mM, 25 mM, 30 mM), and 100 mL Diox. Note: \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{Total carbon}} \left(\mathrm{\%}\right)$$\end{document} Yield Total carbon % = \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} <t>\begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{HMF}}</t> \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{FF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LG}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LGO}} \left(\mathrm{\%}\right)$$\end{document} Yield HMF % + Yield FF % + Yield LG % + Yield LGO % , and these yields were the highest yield
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The influence of different catalysts and concentrations on <t>LG,</t> <t>LGO,</t> total carbon yield. (1) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of 15 mM catalyst (TsOH, MSA, H 2 SO 4 ), and 100 mL Diox. (2) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of H 2 SO 4 concentrations (10 mM, 15 mM, 25 mM, 30 mM), and 100 mL Diox. Note: \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{Total carbon}} \left(\mathrm{\%}\right)$$\end{document} Yield Total carbon % = \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} <t>\begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{HMF}}</t> \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{FF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LG}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LGO}} \left(\mathrm{\%}\right)$$\end{document} Yield HMF % + Yield FF % + Yield LG % + Yield LGO % , and these yields were the highest yield
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The influence of different catalysts and concentrations on LG, LGO, total carbon yield. (1) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of 15 mM catalyst (TsOH, MSA, H 2 SO 4 ), and 100 mL Diox. (2) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of H 2 SO 4 concentrations (10 mM, 15 mM, 25 mM, 30 mM), and 100 mL Diox. Note: \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{Total carbon}} \left(\mathrm{\%}\right)$$\end{document} Yield Total carbon % = \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{HMF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{FF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LG}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LGO}} \left(\mathrm{\%}\right)$$\end{document} Yield HMF % + Yield FF % + Yield LG % + Yield LGO % , and these yields were the highest yield

Journal: Biomass Conversion and Biorefinery

Article Title: Characterization of isolated starch from Isatis indigotica Fort. root and anhydro-sugars preparation using its decoction residues

doi: 10.1007/s13399-023-03892-9

Figure Lengend Snippet: The influence of different catalysts and concentrations on LG, LGO, total carbon yield. (1) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of 15 mM catalyst (TsOH, MSA, H 2 SO 4 ), and 100 mL Diox. (2) Experimental conditions: 1 g of IIR residues, 190 °C, 2 h, 40 μL of H 2 SO 4 concentrations (10 mM, 15 mM, 25 mM, 30 mM), and 100 mL Diox. Note: \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{Total carbon}} \left(\mathrm{\%}\right)$$\end{document} Yield Total carbon % = \documentclass[12pt]{minimal} \usepackage{amsmath} \usepackage{wasysym} \usepackage{amsfonts} \usepackage{amssymb} \usepackage{amsbsy} \usepackage{mathrsfs} \usepackage{upgreek} \setlength{\oddsidemargin}{-69pt} \begin{document}$${\left[\mathrm{Yield}\right]}_{\mathrm{HMF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{FF}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LG}} \left(\mathrm{\%}\right)+{\left[\mathrm{ Yield}\right]}_{\mathrm{LGO}} \left(\mathrm{\%}\right)$$\end{document} Yield HMF % + Yield FF % + Yield LG % + Yield LGO % , and these yields were the highest yield

Article Snippet: LGO, HMF, and furfural were analyzed using a GC (Shimadzu, GC-2010 Plus equipped with a flame ionization detector and a Restek RTX-VMS capillary column).

Techniques: