期刊文献+

Research on Optimized Utilization of Naphtha Resources Based on Adsorptive Separation with Zeolite 被引量:8

Research on Optimized Utilization of Naphtha Resources Based on Adsorptive Separation with Zeolite
下载PDF
导出
摘要 By means of molecular scale management, the technology of separating normal paraffins from naphtha through adsorption using 5A molecular sieves was studied with the purpose of optimizing the utilization of naphtha. The raw materials used in steam cracking and catalytic reforming processes could be allocated properly. During the adsorption process, the separation efficiency of the normal paraffins was above 99.9% with the purity of normal paraffins in the desorption oil exceeding 98.2%. With the use of the desorption oil as the feedstock of steam cracking, the ethylene yield increased from 29.7%-35.0% to 41.4%- 49.2% compared to that of the naphtha in the existing plant under similar operation conditions. The potential aromatic content of the raffinate oil rose from 30.6% to 43.5% compared to that in naphtha. The research octane number of the raffinate oil reached more than 85 with an increase of 20 units compared to that of naphtha, so the raffinate oil is more suitable for use as a blending component for high-octane clean gasoline. By means of molecular scale management, the technology of separating normal paraffins from naphtha through adsorption using 5A molecular sieves was studied with the purpose of optimizing the utilization of naphtha. The raw materials used in steam cracking and catalytic reforming processes could be allocated properly. During the adsorption process, the separation efficiency of the normal paraffins was above 99.9% with the purity of normal paraffins in the desorption oil exceeding 98.2%. With the use of the desorption oil as the feedstock of steam cracking, the ethylene yield increased from 29.7%-35.0% to 41.4%-49.2% compared to that of the naphtha in the existing plant under similar operation conditions. The potential aromatic content of the raffinate oil rose from 30.6% to 43.5% compared to that in naphtha. The research octane number of the raffinate oil reached more than 85 with an increase of 20 units compared to that of naphtha, so the raffinate oil is more suitable for use as a blending component for high-octane clean gasoline.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2005年第1期49-55,共7页 中国炼油与石油化工(英文版)
关键词 NAPHTHA n-paraffin ADSORPTION molecular scale management 石脑油 沸石 吸附技术 分离工艺 加工工艺
  • 相关文献

参考文献6

  • 1[1]Qu Guohua. Optimization of Steam Cracking Feedstock.Ethylene Industry, 2002, 14(4): 61- 65. 被引量:1
  • 2[2]Jose A C, Silva Francisco A. Separation of n/iso-paraffins by PSA. Separation and Purification Technology, 20(2000): 97- 110 被引量:1
  • 3[3]He Jie, Yan Aizhen. Study on Performance of 5A Zeolite.Acta Petrolei Sinica(Petroleum Processing), 1990, 6(4): 8-14. 被引量:1
  • 4[4]Ralph T. Yang. Gas Separation by Adsorption Process.Edition 1, New York: Butterworth Publishers, 1987, 178. 被引量:1
  • 5[5]Zhang Chengcong, Ma Xiang, Yang Wenfan. Fast Determination of Gasoline Octane Number by High Resolution Gas Chromatography. Yunnan University Journal, 1999, 21(4): 291 - 293. 被引量:1
  • 6[6]Gorana Protic-Lovasic, Nada Jambrec, Djurdja Deur-Sifiar.Determination of Catalytic Reformed Gasoline Octane Number by High Resolution Gas Chromatography. FUEL, 1990,69:525-528 被引量:1

同被引文献56

引证文献8

二级引证文献42

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