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NaOH modified WO3/SiO2 catalysts for propylene production from 2-butene and ethylene metathesis

机译:NaOH改性WO3 / SiO2催化剂,用于丙烯生产的2-丁烯和乙烯复分解

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摘要

A WO3/SiO2 catalyst is used in industry to produce propylene from 2-butene and ethylene metathesis. Catalysts with various WO3 loading (4% to 10%) were prepared by impregnation and tested for the metathesis of ethene and trans-2-butene. Ion exchange of NaOH onto the WO3/SiO2 catalyst was used to mitigate the acidity of the catalysts in a controlled way. At low WO3 loading, the treatment with large amounts of NaOH resulted in a significant decrease in metathesis activity concomitant with significant W leaching and marked structural changes (XRD, Raman). At higher WO3 loading (6% to 10%), the treatment with NaOH mainly resulted in a decrease in acidity. FT-IR experiments after adsorption of pyridine showed that the Lewis acidic sites were poisoned by sodium. Nevertheless, the metathesis activity remained constant after the NaOH treatment. This suggested that the remaining acidity on the catalyst was enough to ensure the efficient formation of the carbene active sites. Interestingly, Na poisoning resulted in some modification of the selectivity. The mitigation of acidity was shown to favor propene selectivity over the formation of isomerization products (cis-2-butene, 1-butene, etc.). Moreover, treatment with NaOH led to a shorter induction period and reduced coke formation on the WO3/SiO2 catalyst.
机译:WO3 / SiO2催化剂用于工业中,以产生来自2-丁烯和乙烯复分解的丙烯。通过浸渍制备具有各种WO3负载(4%至10%)的催化剂,并测试乙烯和反式-2-丁烯的复位。 NaOH在WO3 / SiO 2催化剂上的离子交换用于以受控方式减轻催化剂的酸度。在低WO3负载下,大量NaOH的处理导致复分解活性的显着降低,伴随着显着的W浸出和显着的结构变化(XRD,拉曼)。在较高的WO3载荷(6%至10%)时,用NaOH的处理主要导致酸度降低。吡啶吸附后的FT-IR实验表明,Lewis酸性位点被钠中毒。然而,在NaOH治疗后,复分解活性保持不变。这表明催化剂上的剩余酸度足以确保肉食活性位点的有效形成。有趣的是,Na中毒导致了一种选择性的修饰。显示酸度的减轻,有利于对异构化产物的形成(CIS-2-丁烯,1-丁烯等)的丙烯选择性。此外,用NaOH处理导致诱导期更短,并在WO3 / SiO 2催化剂上减少焦炭形成。

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