Shunli Zhou, Chengxi Zhang, Yongxiang Li, 等. A pre-mix synthesis strategy for zeolite Y-based alkylation catalysts: enhanced acidity and stability via zeolite–binder interactions[J]. 清洁能源(英文), 2026,(5).
Shunli Zhou, Chengxi Zhang, Yongxiang Li, Ye Buehler, Xiuzhi Gao, Xingtian Shu, A pre-mix synthesis strategy for zeolite Y-based alkylation catalysts: enhanced acidity and stability via zeolite–binder interactions, Clean Energy, Volume 10, Issue 5, October 2026, Pages 54–65, https://doi.org/10.1093/ce/zkag041
Shunli Zhou, Chengxi Zhang, Yongxiang Li, 等. A pre-mix synthesis strategy for zeolite Y-based alkylation catalysts: enhanced acidity and stability via zeolite–binder interactions[J]. 清洁能源(英文), 2026,(5).DOI: 10.1093/ce/zkag041.
Shunli Zhou, Chengxi Zhang, Yongxiang Li, Ye Buehler, Xiuzhi Gao, Xingtian Shu, A pre-mix synthesis strategy for zeolite Y-based alkylation catalysts: enhanced acidity and stability via zeolite–binder interactions, Clean Energy, Volume 10, Issue 5, October 2026, Pages 54–65, https://doi.org/10.1093/ce/zkag041DOI:
A pre-mix synthesis strategy for zeolite Y-based alkylation catalysts: enhanced acidity and stability via zeolite–binder interactions
摘要
Abstract
With increasingly stringent environmental regulations on gasoline composition
the replacement of hazardous liquid acid catalysts [hydrogen fluoride (HF) and H2SO4] with solid acid alternatives for isobutane–butene alkylation has become imperative. Zeolite Y-based catalysts offer promising eco-friendly alternatives; however
their commercial application remains limited by rapid deactivation caused by insufficient Brønsted acid site (BAS) density and unfavorable oligomerization side reactions. Herein
we report a mechanism-guided pre-mix synthesis strategy that eliminates one high-temperature calcination step and maximizes zeolite–binder interactions to substantially enhance catalyst acidity and stability. The designed NH4Y–Al2O3 catalyst exhibits a total BAS density that is 1.9 times higher and a strong BAS density that is 2.6 times higher than conventionally prepared HY–Al2O3. Comprehensive characterization by X-ray diffraction
magic-angle spinning nuclear magnetic resonance (3Q
27Al
and 29Si)
temperature-programmed desorption of NH3
and pyridine adsorption infrared spectroscopy reveals that the enhanced acidity originates from: (i) enhanced framework Al retention and local structural stability due to reduced thermal dealumination
evidenced by increased unit cell parameter from 2.448 to 2.459 nm; and (ii) migration of Al species from the Al2O3 binder to ion-exchange positions and framework sites
forming distorted tetrahedral Al species. The pre-mix method reduces zeolite agglomeration
increases interfacial contact area
and lowers energy consumption. In isobutane–butene alkylation
NH4Y–Al2O3 demonstrates exceptional catalytic performance: deactivation time is extended by 70% (48 h vs. 28 h)
C8 selectivity increases by 7 percentage points
and alkylate yield reaches 94.35%
surpassing conventional H2SO4 (93.10%) and HF (91.50%) systems. The hydrogen transfer rate doubles that compared to conventional catalysts
effectively suppressing oligomerization and coke formation. These findings establish design principles for zeolite-based alkylation catalysts and demonstrate an energy-efficient synthesis route that reduces carbon emissions and offers potential for industrial scale-up.
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