Earticle

초록

영어

In this work, ZSM-5, a size selective heterogeneous catalyst was employed for the synthesis of p-xylen from durene by cracking. The reaction was carried out in gas phase using a fix bed reactor. During the reaction, benzene was used as solvent together with durene. To optimize the reaction conditions, temperature, feed ratio, feed flow rate, reaction time and catalyst load weight were investigated. The products were analyzed by gas chromatography (GC). The selectivity of p-xylene and the conversion of durene was 20.04% and 40.09% respectively when the reaction was carried out at 450 ˚C for 1 h using 1.0 g catalyst with feed ratio 1: 8 and flow rate 2.0 ml/h.

목차

Abstract
 1. Introduction
 2. Experimental
  2.1. Materials
  2.2. Preparation of catalyst
  2.3. Catalyst characterization
  2.4. Catalytic cracking of durene over ZSM-5
 3. Results and Discussion
  3.1. Characteristics of catalyst
  3.2. Catalyst activity study
 4. Conclusions
 Acknowledgements
 References

키워드

저자

• Mei Mei Peng [ Department of Chemical Engineering, Hanseo University ]
• Abidov Aziz [ Department of Chemical Engineering, Hanseo University ]
• Muthiahpillai Palanichamy [ Department of Chemical Engineering, Hanseo University ]
• Seung Gil Lee [ Department of Life Science, Hanseo University, Seosan-si 356-706, South Korea ]

참고문헌

발행기관

간행물

표지보기 관심저널 등록

• 간행물명

  International Journal of Control and Automation

• 간기

  월간

• pISSN

  2005-4297

• 수록기간

  2008~2016

• 십진분류

  KDC 505 DDC 605