Synthesis and Granulation of a 5A Zeolite-Based Molecular Sieve and Adsorption Equilibrium of the Oxidative Coupling of Methane Gases

被引:21
作者
Garcia, Leonel [1 ]
Poveda, Yuly A. [1 ]
Khadivi, Mohammadali [2 ]
Rodriguez, Gerardo [1 ]
Goerke, Oliver [3 ]
Esche, Erik [2 ]
Godini, Hamid Reza [2 ]
Wozny, Guenter [2 ]
Orjuela, Alvaro [1 ]
机构
[1] Univ Nacl Colombia, Dept Chem & Environm Engn, Grp Invest Proc Quim & Bioquim, Bogota 111321, Colombia
[2] Tech Univ Berlin, Chair Proc Dynam & Operat, Sekr, KWT 9, Str 17 Juni135, D-10623 Berlin, Germany
[3] Tech Univ Berlin, Inst Mat Sci & Technol, FG Keram Werkstoffe, Sekr BA3 Hardenbergstr 40, D-10623 Berlin, Germany
关键词
BED CHROMATOGRAPHIC REACTOR; ELECTRIC QUADRUPOLE-MOMENTS; CARBON-DIOXIDE; ETHYLENE/ETHANE SEPARATION; HYDROCARBON SEPARATIONS; CATALYTIC CONVERSION; ETHANE; CH4; MEMBRANE; NITROGEN;
D O I
10.1021/acs.jced.7b00061
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work presents a detailed description of the synthesis of a SA zeolite and its further granulation into molecular sieve beads. The XRD spectrum of synthesized crystals showed the characteristic peaks of a type A sodium zeolite, and XRF results of the ion-exchanged material with a calcium chloride solution allowed us to verify the formation of a SA zeolite structure. The analysis of SEM images indicated that the granulated process generated a core shell structure with suitable mechanical properties for industrial use. The granulated material exhibited similar properties (roundness, 96%; crush strength, 57 N; packing density, 607 kg/m(3); and Langmuir surface area, 410.5 m(2)/g) to most commercial molecular sieves. However, its lower water sorption capacity (0.142 kg/kg) reveals that zeolite adsorption is affected by the cementing material. Adsorption equilibrium studies at different temperatures with oxidative coupling of methane (OCM) effluent gases indicated that the material showed a higher affinity for CO2, followed by ethylene, ethane, and methane, whereas nitrogen was barely retained. The affinity trend was in agreement with the observed heats of adsorption, which were in the range of 13-30 kJ/mol for tested gases. Isotherms were fitted with a Langmuir model, and adsorption parameters were obtained. Regressed equilibrium equations can be used for further modeling of a swing adsorption separation for OCM effluent gases.
引用
收藏
页码:1550 / 1557
页数:8
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