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首页> 外文期刊>The Journal of Supercritical Fluids >Hydroformylation of 1-hexene in supercritical carbon dioxide using a heterogeneous rhodium catalyst. 1. Effect of process parameters
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Hydroformylation of 1-hexene in supercritical carbon dioxide using a heterogeneous rhodium catalyst. 1. Effect of process parameters

机译:使用非均相铑催化剂在超临界二氧化碳中1-己烯的加氢甲酰化。 1.工艺参数的影响

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The hydroformylation of 1-hexene in supercritical carbon dioxide is catalyzed with a heterogeneous rhodium catalyst that is active, selective, and stable for the formation of heptanal. The aldehyde yield and regioselectivity can be affected through changes in catalyst support structure, CO_2 solvent pressure, and reaction temperature. A complex reaction pathway model is described that allows determination of rate constants, which are in turn, evaluated as a function of temperature and pressure. Analysis reveals an activation volume of -474 cm~3/mol and activation energy of 31.9 kJ/mol for the hydroformylation pathways.
机译:1-己烯在超临界二氧化碳中的加氢甲酰化反应是利用具有活性,选择性和对形成庚醛稳定的非均相铑催化剂进行的。醛的产率和区域选择性可以通过催化剂载体结构,CO_2溶剂压力和反应温度的变化来影响。描述了一种复杂的反应路径模型,该模型可以确定速率常数,然后根据温度和压力对速率常数进行评估。分析表明加氢甲酰化途径的活化体积为-474 cm〜3 / mol,活化能为31.9 kJ / mol。

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