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  • 1
    Digitale Medien
    Digitale Medien
    Springer
    Catalysis letters 16 (1992), S. 27-38 
    ISSN: 1572-879X
    Schlagwort(e): Methane ; chlorination ; solid acid ; zeolites
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Chemie und Pharmazie
    Notizen: Abstract Chlorination of methane was studied over amorphous silica-alumina, silicalite as well as H-mordenite, X, Y, NaL and H-ZSM-5 zeolite catalysts. The heterogeneous transformations were carried out in a continuous flow reactor in the 200–425 °C temperature range, under atmospheric pressure (methane to chlorine ratio 4:1, GHSV 600 ml/ g h). Chlorination of methane over zeolites in the 200–300 °C temperature range proceeds without selectivity indicating a radical mechanism. Above 300–350 °C, depending on the nature of zeolite, selective monochlorination takes place indicating the dominance of an ionic mechanism. H-mordenite was found to give the best monochlorination at the lowest temperature (99.2% CH3Cl at 350 °C). The observed selectivity of the investigated zeolites is strongly time limited. All investigated catalysts lose their selectivity after five hours on-stream due to extraction of aluminum from the framework of zeolites by hydrogen chloride. Amorphous silica-alumina above 350 °C also catalyzes ionic chlorination. The chlorination of methane over silicalite proceeds via the nonselective radical pathway at the investigated temperatures.
    Materialart: Digitale Medien
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  • 2
    Digitale Medien
    Digitale Medien
    Springer
    Catalysis letters 25 (1994), S. 11-19 
    ISSN: 1572-879X
    Schlagwort(e): Methane ; chlorination ; solid superacids ; sulfated zirconia
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Chemie und Pharmazie
    Notizen: Abstract Catalytic chlorination of methane was studied over SO 4 2− /ZrO2, Pt/SO 4 2− /ZrO2, and Fe/Mn/SO 4 2− /ZrO2 solid superacid catalysts. The reactions were carried out in a continuous flow reactor under atmospheric pressure, at temperatures below 240°C, with a gaseous hourly space velocity of 1000 ml/g h and a methane to chlorine ratio of 4 to 1. At 200°C with 30% chlorine converted the selectivity in methyl chloride exceeds 90%. At more elevated temperatures, the selectivity decreases but stays above 80% in methyl chloride at 225°C using the sulfated zirconia catalysts. The selectivity can be enhanced by adding platinum to sulfated zirconia catalysts. An iron and manganese-doped catalyst exhibited excellent selectivities at somewhat lower conversions. Methyl chloride is obtained at 235°C in selectivities greater than 85%. No chloroform or carbon tetrachloride is formed. The electrophilic insertion involves electron-deficient metal-coordinated chlorine into the methane C-H bond.
    Materialart: Digitale Medien
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  • 3
    ISSN: 1572-879X
    Schlagwort(e): alkylation ; isobutane ; isobutylene ; trifluoromethanesulfonic acid ; temperature dependence
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Chemie und Pharmazie
    Notizen: Abstract The effect of the acid-hydrocarbon ratio and temperature on the isobutane-isobutylene alkylation with trifluoromethanesulfonic acid was studied over the temperature range of 40
    Materialart: Digitale Medien
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  • 4
    ISSN: 1572-879X
    Schlagwort(e): alkylation ; isobutane ; isobutylene ; HF ; PPHF ; H2SO4 ; trifluoromethanesulfonic acid ; liquid CO2
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Chemie und Pharmazie
    Notizen: Abstract Liquid carbon dioxide was studied as a solvent for the isobutane–isobutylene alkylation. The acid catalysts in the reaction were anhydrous HF (AHF), pyridinium–poly(hydrogen fluoride) complex (PPHF), concentrated sulfuric acid and trifluoromethanesulfonic acid (TFSA). The effect of the acid–hydrocarbon volume ratio, temperature and residence time on the alkylate quality were studied over the temperature range of 50 ⩾ T ⩾ 0 °C. Carbon dioxide as a competing weak base decreases the acidity of the system which parallels the alkylate quality. In the case of HF and TFSA catalysts, solvent CO2 increased the octane number of the alkylate product (RON 95.6 for HF‐ and 88.0 for TFSA‐catalyzed alkylation with CO2 solvent).
    Materialart: Digitale Medien
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