2216-77-5Relevant articles and documents
Heterogeneous catalytic conversion of glycerol with n-butyl alcohol
Samoilov,Ramazanov,Nekhaev,Maksimov
, p. 125 - 130 (2016/04/20)
The etherification of glycerol with n-butyl alcohol at 140°C in the presence of sulfonated cation-exchange resins and zeolite catalysts in an autoclave reactor has been studied. It has been shown that styrene - divinylbenzene ion-exchange resins are effective catalysts for the production of glycerol n-butyl ethers: the glycerol conversion is about 98% with an n-butyl ether selectivity of about 88 mol % (140°C, 5 h, 5 wt % Amberlyst 36 catalyst, and 10 wt % glycerol in n-butanol). Zeolites Y and β in the H+ form exhibit comparable specific activity (glycerol conversion of no more than 25% under similar conditions) in combination with high selectivity for glycerol di-n-butyl ethers (up to 28%).
Thermodynamic characteristics of the sorption of glycerol ethers on stationary phase OV-101
Zhabina,Krasnykh,Levanova
, p. 1590 - 1593 (2014/10/16)
Retention characteristics, temperature dependences of the retention characteristics, and thermodynamic characteristics of sorption on the nonpolar OV-101 phase are determined for 33 glycerol mono-, di-, and triethers with linear and branched monobasic alc
POLYOL ETHERS AND PROCESS FOR MAKING THEM
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Page/Page column 8, (2010/03/31)
New polyol ether compounds and a process for their preparation. The process comprises reacting a polyol, a carbonyl compound, and hydrogen in the presence of hydrogenation catalyst, to provide the polyol ether. The molar ratio of polyol to carbonyl compound in the process is greater than 5:1.