An analysis of the relative errors in measuring the number of theoretical plates in a continuous distillation column

2007 ◽  
Vol 27 (3) ◽  
pp. 465-478
Author(s):  
Marcel Mussche ◽  
Lucien Verhoeye
2004 ◽  
Vol 51 (1) ◽  
pp. 7-12
Author(s):  
Yuzoh Asano ◽  
Yuriko Iiyama ◽  
Tetsuo Kubota ◽  
Hiroshi Ochi ◽  
Teruhiko Mizota ◽  
...  

1972 ◽  
Vol 27 (1) ◽  
pp. 129-136 ◽  
Author(s):  
H. Mizuno ◽  
Y. Watanabe ◽  
Y. Nishimura ◽  
M. Matsubara

2016 ◽  
Vol 18 (1) ◽  
pp. 33-39
Author(s):  
Zhibo Wang ◽  
Shuairong Li ◽  
Caijiao Wang ◽  
Xianghai Guo ◽  
Peng Bai

Abstract In the B10 isotope enrichment industry, the purification of anisole mixture makes great sense. A dynamic-accumulative operation policy of continuous distillation (DACD) with repeated filling and dumping of the still is proposed for the separation of trace heavy impurities in the recycled anisole. To simulate and optimize the purification process of anisole, a mathematical model of DACD is derived, and the computer codes are developed in the MATLAB environment. Moreover, the experiment is performed in a pilot-scale distillation column. The results show that the experimental date agrees well with simulation results. DACD could solve the difficulty of flow rate control when the bottom flow rate is very small in continuous distillation. The size of the still in this operation mode is also smaller than that in batch distillation. And the yield of anisole is raised to 99.91%. In a word, DACD is especially suitable for separating trace heavy impurities from the recycled anisole.


2012 ◽  
Vol 84 ◽  
pp. 628-637 ◽  
Author(s):  
Rui Cao ◽  
Guolei Fu ◽  
Yansheng Liu ◽  
Chaoyu Yan ◽  
Yan Wu ◽  
...  

2002 ◽  
Vol 49 (12) ◽  
pp. 801-807
Author(s):  
Yuzoh Asano ◽  
Yuriko Iiyama ◽  
Tetsuo Kubota ◽  
Keiji Iwatsuki ◽  
Kazuyoshi Sotoyama

1983 ◽  
Vol 16 (1) ◽  
pp. 36-42 ◽  
Author(s):  
YUJI NAKA ◽  
KIKUO KOBAYASHI ◽  
HITOSHI OCHI ◽  
TAKEICHIRO TAKAMATSU

2018 ◽  
Vol 3 (1) ◽  
pp. 8-13 ◽  
Author(s):  
Andras Jozsef Toth ◽  
Eniko Haaz ◽  
Tibor Nagy ◽  
Ariella Janka Tarjani ◽  
Daniel Fozer ◽  
...  

Abstract The work is motivated by an industrial problem, which is alcohol removal from pharmaceutical process wastewater. The aim of the study was to develop a complete hybrid operation is investigated. Ethanol dehydration, in combination with distillation and hydrophilic pervaporation, is used to investigate about the extent of separation of the ethanol-water mixture. The aim of this research is to rigorously model and optimize this hybrid operation in professional flowsheet simulator environment. The number of minimal theoretical plates of distillation column and minimal effective membrane transfer area are determined. Cost estimation is also examined according to Douglas methodology. Considering our results it can be concluded that, the distillation and hydrophilic pervaporation processes are suitable for separation ethanol and water in 99.5 weight percent purity


Sign in / Sign up

Export Citation Format

Share Document