Supporting data information for "Continuous Production of Biorenewable, Polymer-Grade Lactone Monomers through Sn-β-Catalyzed Baeyer-Villiger Oxidation with hydrogen peroxide”
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https://research-data.cardiff.ac.uk/articles/dataset/Supporting_data_information_for_Continuous_Production_of_Biorenewable_Polymer-Grade_Lactone_Monomers_through_Sn-_-Catalyzed_Baeyer-Villiger_Oxidation_with_hydrogen_peroxide_/27277080/1
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Data set contains kinetic information of 2-substituted and 4-substituted cyclohexanone (R-CyO) Baeyer Villiger oxidation (BVO) reactions using hydrogen peroxide as oxidant and 2%Sn-Beta as heterogeneous catalyst, in batch mode. Reaction conditions: 0.33M R-CyO in 1,4-dioxane (10 mL), H2O2/R-CyO=1.5:1, 1 mol% Sn at 100 C for a periof of 6 h.Substrates tested are: Cyclohexanone (CyO), 2-Methylcylcohexanone (2-Me-CyO), 2-Ethylcyclohexanone (2-Eth-CyO), 2-Isopropylcyclohexanone (2-iPr-CyO), 2-tertbutylcyclohexanone (2-tBu-CyO), 4-Methylcylcohexanone (4-Me-CyO), 4-Ethylcyclohexanone (4-Eth-CyO), 4-Isopropylcyclohexanone (4-iPr-CyO) and 4-tertbutylcyclohexanone (4-tBu-CyO).Columns describe: Conversion of R-Cyclohexanone (X, %), Yield of R-Caprolactone (Y, %), Selectivity of R-Caprolactone (S, %), Carbon Balance (C Bal, %) and Turnover frequency (TOF, h-1) at different times (min) for each substrate tested. It includes also a comparison of initial TOF (at 10 min of reaction, h-1) of 2-R-CyO and 4-R-CyO as function of R.Data set contains also kinetic information of BVO reaction of Cyclohexanone and 4-iPr-CyO in continuous mode (plug flow reactor (PFR)) for a period of 60 h. Reaction conditions: Reactant feed of 0.33M cyclohexanone and 0.5M H2O2 in 1,4-dioxane with a contact time of 5.5 min under a pressure of 10 bar, at 100 C.Columns describe: Conversion of R-Cyclohexanone (X, %), Selectivity of R-Caprolactone (S, %), Turnover (TON), Turnover frequency (TOF, h-1) and Space-time yield (STY, g prod kg-1 cat cm-3 h-1) as function of time (min).Research results based upon these data are published at http://doi.org/10.1002/cssc.201701298
本数据集收录了以过氧化氢为氧化剂、2%Sn-Beta为非均相催化剂,在批次模式下进行的2-取代和4-取代环己酮(R-CyO)拜耳-维利格氧化(BVO)反应的动力学信息。反应条件包括:0.33M的R-CyO溶于10毫升1,4-二氧六环中,H2O2与R-CyO的摩尔比为1.5:1,添加1摩尔百分比的Sn,在100摄氏度下反应6小时。测试的底物包括:环己酮(CyO)、2-甲基环己酮(2-Me-CyO)、2-乙基环己酮(2-Eth-CyO)、2-异丙基环己酮(2-iPr-CyO)、2-叔丁基环己酮(2-tBu-CyO)、4-甲基环己酮(4-Me-CyO)、4-乙基环己酮(4-Eth-CyO)、4-异丙基环己酮(4-iPr-CyO)和4-叔丁基环己酮(4-tBu-CyO)。数据列描述了:R-环己酮的转化率(X,%)、R-己内酯的产率(Y,%)、R-己内酯的选择性(S,%)、碳平衡(C Bal,%)以及在不同时间点(分钟)对每种底物进行测试时的周转频率(TOF,h-1)。此外,还包括了2-R-CyO和4-R-CyO在R作为函数下的初始周转频率(反应10分钟时的h-1)的比较。数据集还包含了环己酮和4-iPr-CyO在连续模式(填料床反应器(PFR))下BVO反应的动力学信息,持续时间为60小时。反应条件为:在10巴的压力下,以5.5分钟的接触时间,在1,4-二氧六环中,将0.33M的环己酮和0.5M的H2O2作为反应物进料,在100摄氏度下进行。数据列描述了:R-环己酮的转化率(X,%)、R-己内酯的选择性(S,%)、周转数(TON)、周转频率(TOF,h-1)和时空产率(STY,g prod kg-1 cat cm-3 h-1)随时间(分钟)的变化。基于这些数据的研究成果已发表在http://doi.org/10.1002/cssc.201701298。
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Cardiff University



