期刊文献+

低硅体系下SAPO-34分子筛的合成 被引量:1

Synthesis of SAPO-34 Molecular Sieves from Gels with Low Silicon Concentration
下载PDF
导出
摘要 以三乙胺和吗啉为模板剂,考察了硅含量和晶化温度对合成SAPO-34分子筛的影响,研究了低硅条件下SAPO-34分子筛的晶化规律。在n(SiO2)∶n(Al2O3)=0.1的低硅体系中合成出了高结晶度的SAPO-34分子筛,发现将晶化温度从200℃降至170℃更有利于低硅条件下SAPO-34分子筛的合成。根据合成结果初步认为,低硅条件下SAPO-34分子筛的合成可能符合低温成核、高温生长机理,并用分段晶化实验加以证实。实验结果表明,在低硅体系下,先在170℃晶化一段时间再在200℃晶化一段时间(总晶化时间48 h),不仅可获得高结晶度SAPO-34分子筛,且能缩短晶化时间;若将分段晶化温度顺序调换,即先在200℃晶化再在170℃晶化,则无法获得纯相SAPO-34分子筛,说明先低温后高温的分段晶化更有利于低硅体系下纯相SAPO-34分子筛的合成。 The synthesis of SAPO-34 molecular sieves in a system with low silica content was investigated.It was found that lowering the crystallization temperature from 200 ℃ to 170 ℃ was beneficial to the formation of pure SAPO-34 phase in the low silica system.At 170 ℃,high crystalline SAPO-34 was obtained from the gel with molar ratio of SiO2 to Al2O3 0.1 with triethylamine or morpholine as the template.The synthesis might accord with low-temperature nucleation and high-temperature growth mechanism,which was confirmed by a multistep crystallization,namely first at 170 ℃ for t h and then at 200 ℃ for 48-t h in the low silicon system.The high crystalline SAPO-34 could be synthesized in a short crystallization period.
出处 《石油化工》 CAS CSCD 北大核心 2012年第5期510-514,共5页 Petrochemical Technology
基金 国家自然科学基金项目(20873069) 天津市自然科学基金项目(12JCYBJC12700) 国家重大基础研究发展计划项目(2009CB623502)
关键词 低硅体系 SAPO-34分子筛 分段晶化 甲醇制烯烃催化剂 low silicon system SAPO-34 molecular sieve multistep crystallization methanol to olefin catalyst
  • 相关文献

参考文献18

  • 1Liang Juan,Li Hongyuan,Zhao Sugin,et al.Characteristicsand Performance of SAPO-34 Catalyst for Methanol-to-OlefinConversion[J].Appl Catal,1990,64(1):31-40.
  • 2Xu Yan,Grey C P,Thomas J M,et al.An Investigation intothe Conversion of Methanol to Hydrocarbons over a SAPO-34Catalyst Using Magic-Angle-Spinning NMR and Gas Chroma-tography[J].Catal Lett,1990,4(3):251-260.
  • 3Chen D,Rebo H P,Gr nvold A,et al.Methanol Conversionto Light Olefins over SAPO-34:Kinetic Modeling of CokeFormation[J].Microporous Mesoporous Mater,2000,35/36(1):121-135.
  • 4IzadbakhshA,Farhadi F,Khorasheh F,et al.Key Parametersin Hydrothermal Synthesis and Characterization of Low SiliconContent SAPO-34 Molecular Sieve[J].Microporous Mesopo-rous Mater,2009,126(1):1-7.
  • 5Sastre G,Lewis D W,Catlow C R A.Modeling of SiliconSubstitution in SAPO-5 and SAPO-34 Molecular Sieves[J].JPhys Chem B,1997,101(27):5249-5261.
  • 6Vomscheid R,Briend M,Peltre M J,et al.The Role of theTemplate in Directing the Si Distribution in SAPO Zeolites[J].J Phys Chem,1994,98(38):9614-9618.
  • 7Wilson S,Barger P.The Characteristics of SAPO-34 WhichInfluence the Conversion of Methanol to Light Olefins[J].Mi-croporous Mesoporous Mater,1999,29(1/2):117-126.
  • 8Aguayo A T,Gayubo A G,Vivanco R,et al.Role of Aci-dity and Microporous Structure in Alternative Catalysts for theTransformation of Methanol into Olefins[J].Appl Catal,A,2005,283(122):197-207.
  • 9ExxonMobil Chemical Patents,Inc.Synthesis of MolecularSieves of CHA Framework Type:US,6835363 B1[P].2004-12-28.
  • 10ExxonMobil Chemical Patents,Inc.Synthesis of MolecularSieves Having the CHA Framework Type:US,6793901 B2[P].2004-09-21.

同被引文献9

引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部