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Zeolite catalysed dehydration of alcohol to linear ether

机译:沸石催化醇的醇到线性乙醚

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The liquid-phase dehydration of 1-hexanol and 1-pentanol to di-n-hexyl ether (DNHE) and di-n-pentyl ether (DNPE), respectively, has been studied over H-ZSM-5, H-Beta, H-Y, and other zeolites at 160-200°C and 2.1 MPa. Among zeolites with a similar acid sites concentration, large pore H-Beta and H-Y show higher activity and selectivity to ethers than those with medium pores, although activity of H-ZSM-5 (particularly in 1-pentanol) is also noticeable. Increased Si/Al ratio in H-Y zeolites results in lower conversion of pentanol due to reduced acid site number and in enhanced selectivity to ether. Selectivity to DNPE is always higher than to DNHE.
机译:在H-ZSM-5,H-Beta中,分别研究了1-六烷醇和1-戊醇至二己醇和二己醇醚(DNHE)和二氢戊醚(DNPE)的液相脱水。 HY和其他160-200°C和2.1MPa的其他沸石。在具有相似酸位点的沸石中,大的孔隙H-β和H-γ比醚的活性和选择性比中孔较高,尽管H-ZSM-5(特别是1-戊醇)的活性也是明显的。 H-Y沸石中的Si / Al比增加导致戊醇的转化率降低,因为酸点数还原,并增强了对乙醚的选择性。对DNPE的选择性总是高于DNHE。

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