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restek rtx vms capillary column  (Restek Corporation)

 
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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/restek+rtx-vms+column/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
    86/100 stars

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    other:

    Article Title: Natural Biodegradation of Vinyl Chloride and cis-Dichloroethene in Aerobic and Suboxic Conditions.
    Article Snippet: Chlorinated ethene (CE) groundwater contamination is commonly treated through anaerobic biodegradation (i.e., reductive dechlorination) either as part of an engineered system or through natural attenuation.. Aerobic biodegradation has also been recognized as a potentially significant pathway for the removal of the lower CEs cis-1,2-dichloroethene (cDCE) and vinyl chloride (VC).. However, the role of aerobic biodegradation under low oxygen conditions typical of contaminated groundwater is unclear.

    Article Title: Enhancement of biomass retention in an EGSB reactor used to treat 1-methoxy-2-propanol
    Article Snippet: BACKGROUND: An expanded granular sludge bed (EGSB) reactor is commonly used in anaerobic treatment of industrial wastewater.. To develop applications to remove solvents, the granular sludge retention within the reactor must be improved.. RESULTS: This work evaluated the addition of chitosan as a strategy to enhance granulation in an EGSB reactor used to treat a wastewater containing 1-methoxy-2-propanol and ethanol.

    Article Title: Production of hydrogen, alkanes and polyols by aqueous phase processing of wood-derived pyrolysis oils
    Article Snippet: The reactants and products were also verified by GC-MS. A Restek Rtx-VMS (Catalog No. 19915) column was used with a constant column linear velocity of 31.3 cm s-1.

    Article Title: Removal of char particles from fast pyrolysis bio-oil by microfiltration
    Article Snippet: Bio-oil formed by the fast pyrolysis of biomass has tremendous potential as a renewable feedstock to make liquid transportation fuels.. However, the presence of char particles in the bio-oil causes problems in storage and end-use.. Currently there is no well-established technology to remove char particles less than 10 m in size.

    Article Title: Hydrodeoxygenation of the aqueous fraction of bio-oil with Ru/C and Pt/C catalysts
    Article Snippet: The levoglucosan, glucose and sorbitol standards were analyzed by HPLC while all the other standard compounds (levoglucosan included) were detected and quantified by HP Gas Chromatograph (Model 7890A) with a Restek Rtx-VMS column using a constant column Page 6 of 30 Ac ce pt ed M an us cr ip t linear velocity of 1.24 mL/s.

    Article Title: Neutrophil Immunomodulatory Activity of Natural Organosulfur Compounds
    Article Snippet: A Restek Rtx-VMS column (30 m × 0.25 mm, 1.40 μm film thickness) was used with He as the carrier gas (2.0 mL/min).

    Article Title: Stormwater quality performance of a macro-pervious pavement car park installation equipped with channel drain based oil and silt retention devices.
    Article Snippet: Separation was achieved using a Restek Rtx-VMS column (20 m 0.18 mm 1.0 mm).



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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/restek+rtx-vms+column/capillary+column/10__1039_slash_d4gc04832f-70-1-1
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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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    restek rtx-vms column  (Restek Corporation)
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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 <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: