期刊文献+

超声强化C8芳烃中乙苯结晶分离工艺研究

Research on Ultrasonic Enhanced Separation of Ethyl benzene,Crystals from C8 Aromatic Hydrocarbons
下载PDF
导出
摘要 通过改变超声波的功率,研究不同功率超声波对C8芳烃异构体形貌以及动力学行为的影响。研究结果表明,将40 W、20 kHz超声波引入C8芳烃结晶分离过程,不仅可以避免晶体的爆发成核,使形成的晶体形貌变为尺寸更小、更加规整的球形颗粒,不易包藏母液,从而提高C8芳烃中乙苯组分分离效率,使二甲苯晶体的含湿率降低至2%;同时大幅降低结晶分离所需的冷量,使混合C8芳烃物料初次析晶温度由-47.2℃提升至-8.9℃,提高结晶分离二甲苯晶体后的乙苯母液纯度至99.0%,从而实现乙苯的单级高效连续结晶分离,生成出能够直接进入苯乙烯装置的高浓度、高纯度乙苯。 By changing the power of ultrasonic waves,the effects of different power ultrasonic waves on the morphology and dynamic behavior of C8 aromatic isomers were studied.The research results indicate that introducing 40W and 20 kHz ultrasonic waves into the C8 aromatics crystallization and separation process can not only avoid crystal nucleation,but also transform the formed crystal morphology into smaller and more regular spherical particles,making it diffi cult to encapsulate the mother liquor,thereby improving the separation effi ciency of ethylbenzene components in C8 aromatics and reducing the moisture content of xylene crystals to 2%;At the same time,the required cooling capacity for crystallization separation is signifi cantly reduced,increasing the initial crystallization temperature of the mixed C8 aromatic materials from-47.2℃to-8.9℃,and increasing the purity of the ethylbenzene mother liquor after crystallization separation of xylene crystals to 99.0%,thereby achieving singlestage efficient and continuous crystallization separation of ethylbenzene,generating high concentration and highpurity ethylbenzene that can directly enter the styrene unit.
作者 李琳鸽 陈强 盛维武 李小婷 魏嘉 陈险峰 LI Linge;CHEN Qiang;SHENG Weiwu;LI Xiaoting;WEI Jia;CHEN Xianfeng
出处 《化工设计通讯》 CAS 2024年第6期20-21,30,共3页 Chemical Engineering Design Communications
基金 中国石化科技开发项目(123035)。
关键词 超声波强化 结晶 动力学 热力学 ultrasonic enhancement crystallization dynamics thermodynamics
  • 相关文献

参考文献4

二级参考文献24

  • 1李希宏,李克明,冷家厂,张宝忠.二甲苯吸附分离装置运行状态初步分析[J].精细石油化工,2004,21(4):54-55. 被引量:2
  • 2[4]Institut Francais du Petrole. Process for co - production and separation of ethylbenzene and paraxylene[P]. US 6177604,2001 - 01 - 23.
  • 3[6]UOP. Separation of ethylbenzene with adsorbent comprising SR and K exchanged X or Y zeolite[P]. US 4079094,1978 - 03 - 14.
  • 4[7]Universal Oil Products Company. Process for the separation of ethylben zene by selective adsorption on zeolitic adsorbent[P]. US 3943182, 1976 - 03 - 09.
  • 5[8]UOP. Process for the separation of ethylbenzene [ P]. US 4497972, 1985 - 02 - 05.
  • 6[9]Exxon Research and Engineering Company. Process for separating ethyl benzene from xylene by selective adsorption on A Rubidium substituted X zeolite[P] .US 4613725,1986 - 09 - 23.
  • 7[10]UOP. Process for adsorptive separation of ethylbenzene from aromatic hydrocarbons[ P] .US 5453560,1995 - 09 - 26.
  • 8Broughton D B, Neuzil R W, Pharis J M, et al. [ J]. Chemical Engineering Progress, 1970,66(9) :70 - 75.
  • 9Broughton D B. [J]. Preprints-Division of Petroleum Chemistry, Areerican Chemical Society, 1983,28(4): 1072 - 1079.
  • 10Broughton D B. [J]. Separation Science and Technology, 1984, 19( 11 - 12) :723 - 736.

共引文献18

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