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Catalytic chlorination and bromination of diamantane with halomethanes was performed under the action of zeolites NaY-mmm, HY-mmm, and FeHY-mmm. Optimal ratios of the catalyst, reagents and conditions for selective synthesis of chloro- and bromo-substituted diamantanes were found.  相似文献   
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Kinetics and Catalysis - The effect of the aging stage on the chemical and phase composition and pore structure characteristics of aluminophosphate gels synthesized using boehmite and phosphoric...  相似文献   
54.
Selective synthesis of dimers of cycloolefins C6-C8 was carried out in the presence of highly dispersed zeolite catalysts HY, HBeta, and HZSM-12 and granulated zeolite HY-WB, which differ in acidic properties and pore structure. The high selectivity of microporous zeolite HZSM-12 in cyclohexene dimerization (100%) and micromesoporous zeolite HY-WB in cycloheptene and cyclooctene dimerization (90–95%) was established.  相似文献   
55.
The possibility of the ion-exchange of Na+ and K+ cations contained in OFF-type zeolite for H+, Ni2+, Cu2+, Co2+, and La3+ cations is investigated. Chemical and phase compositions, the morphology of crystals, and the adsorption properties of synthesized samples are studied via X-ray fluorescence and X-ray diffraction analysis, IR spectroscopy, scanning electron microscopy, and adsorption measurements.  相似文献   
56.
Aniline and its derivatives undergo methylation when treated with dimethyl carbonate in the presence of binder-free micro-, meso-, and macroporous zeolites KNaX, NaY, and HY leading to the formation of N-methyl- and N,N-dimethylanilines.  相似文献   
57.
Hydrogenation of α-methylstyrene linear dimers and of 4-methyl-2,4-diphenylpentane on commercial Pd-containing and Ni (GM-3 grade) catalysts was studied under the following conditions: T = 75–190°C, P(H2) = 0.2–0.8 MPa, G c = 2.5–10 wt %, and τ = 1–4 h.  相似文献   
58.
Co-aggregation of fullerene C60 and thiophene has been studied calorimetrically in cyclohexene at 25 °C. The total aggregation heat is found to depend on initial concentration of thiophene and fall between −1.9 and −5.8 kJ mol−1. The corresponding thiophene/fullerene molar ratio (“co-aggregation number”) ranges from 7 to 12. The data are rationalized by formation of heteromolecular nanoaggregates with intermolecular contacts of both fullerene–thiophene and fullerene–fullerene types. A physical model describing interaction between fullerenes and π-donors in solution is substantiated and used to explain heterogeneity of composites containing fullerenes.  相似文献   
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Kinetics and Catalysis - The catalytic properties of a number of FAU (Y) zeolite samples (microporous zeolite H-Y, granular hierarchical zeolite H-Yh, zeolite H-USYh dealuminated by...  相似文献   
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