5694-72-4Relevant articles and documents
Method for preparing ketal glycerine and/or acetal glycerine by catalyzing glycerine
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Paragraph 0178-0179; 0193, (2020/07/02)
The invention relates to a method for preparing ketal glycerine and/or acetal glycerine by catalyzing glycerine. The method comprises the following steps: contacting glycerine and a reaction raw material with a catalyst in a reactor, and reacting to obtain a product containing ketal glycerine and/or acetal glycerine, wherein the reaction raw materials contains aldehyde and/or ketone, the molar ratio of glycerine to aldehyde and/or ketone is 1:(1-10), the reaction temperature is 30-180 DEG C, the reaction time is 1-10 hours, the catalyst contains a tin-silicon molecular sieve, and the weight ratio of glycerine to the tin-silicon molecular sieve based on dry basis weight is (1-40):1, the tin-silicon molecular sieve contains a silicon element, a tin element and an oxygen element, a cavity orcavity structure is formed in all or part of crystal grains, the total specific surface area is larger than or equal to 300 m/g, and the proportion of the external specific surface area to the total specific surface area is larger than or equal to 10%. The method provided by the invention has high aldehyde/ketone conversion rate and high acetal/ketal glycerine selectivity.
Clay catalysed rapid valorization of glycerol towards cyclic acetals and ketals
Pawar, Radheshyam R.,Gosai, Kalpeshgiri A.,Bhatt, Adarsh S.,Kumaresan,Lee, Seung Mok,Bajaj, Hari C.
, p. 83985 - 83996 (2015/10/28)
Biodiesel production usually results in a huge amount of glycerol, raising a critical need to transform it into high value products. The present study highlights that solvent-free, conventional thermal activation, and non-conventional microwave/ultrasonic activation in the liquid phase are able to selectively transform glycerol into cyclic acetals and ketals using an optimised acid activated clay catalyst. Several parameters for the acid activation of bentonite clay were optimized under mild reaction conditions with a high concentration of clay (6%) and varying the acid concentration in the range of 6 to 15 N. The acid-activated clay samples were characterized by XRD, FT-IR, BET, and XRF analysis. The active sites of the catalyst were examined by volumetric titration and confirmed by pyridine adsorbed FT-IR and advanced NH3-TPD analyses. The activation performed at relatively mild conditions, i.e.; 6 N H2SO4 and 6% w/v clay, reproducibly resulted in an improved surface area (180 m2 g-1) and surface acidity (23 mg KOH g-1), with superior quantitative Br?nsted and Lewis acidic sites. Moreover, the eco-friendly process involving a catalyst, microwave, or ultra-sonication were successfully utilized to achieve a commercially valuable hyacinth fragrance, in addition to furan-based fuel additive precursors exhibiting a high conversion of glycerol and excellent selectivity within much less activation time (2 min).