Energy-Efficient Diabatic Distillation Using a Horizontal Distillation Column

2013 ◽  
Vol 52 (42) ◽  
pp. 14927-14935 ◽  
Author(s):  
Byoung Chul Kim ◽  
Ho Hwan Chun ◽  
Young Han Kim
2017 ◽  
Vol 142 ◽  
pp. 2636-2641
Author(s):  
Muhammad Afiq Zubir ◽  
Ahmad Nafais Rahimi ◽  
Muhammad Fakhrul Islam Zahran ◽  
Munawar Zaman Shahruddin ◽  
Kamarul Asri Ibrahim ◽  
...  

2004 ◽  
Vol 43 (23) ◽  
pp. 7566-7571 ◽  
Author(s):  
Edward Steven Jimenez ◽  
Peter Salamon ◽  
Ricardo Rivero ◽  
Consuelo Rendon ◽  
Karl Heinz Hoffmann ◽  
...  

2014 ◽  
Vol 61 ◽  
pp. 2550-2553 ◽  
Author(s):  
Mohd Faris Mustafa ◽  
Noor Asma Fazli Abdul Samad ◽  
Kamarul Asri Ibrahim ◽  
Mohd Kamaruddin Abd Hamid

2011 ◽  
Vol 219-220 ◽  
pp. 424-427
Author(s):  
Lan Yi Sun ◽  
Jun Li ◽  
Xue Nuan Liu ◽  
Qing Song Li

In this paper, an energy-efficient heat coupled distillation column (HCDC) which is industrially viable is constructed for propylene–propane mixture separation and the sensitivity analysis was performed. Some comparative studies are made with conventional distillation column (CC) and a column with a vapor recompression system (VRC). The results show that the thermal efficiency of the HCDC appears to be strongly sensitive to the compression ratio between rectification section and stripping section.


2017 ◽  
Vol 142 ◽  
pp. 2630-2635 ◽  
Author(s):  
Muhammad Afiq Zubir ◽  
Ahmad Nafais Rahimi ◽  
Muhammad Fakhrul Islam Zahran ◽  
Munawar Zaman Shahruddin ◽  
Kamarul Asri Ibrahim ◽  
...  

2019 ◽  
Vol 62 (1) ◽  
pp. 15-27 ◽  
Author(s):  
Jasdeep Kaur ◽  
Tinkle Chugh ◽  
Vikas K. Sangal

2010 ◽  
Vol 14 (2) ◽  
pp. 317-328 ◽  
Author(s):  
Momcilo Spasojevic ◽  
Milovan Jankovic ◽  
Damir Djakovic

Previous approach to direct numerical minimization of entropy production in diabatic distillation column in order to determine heat quantity to be exchanged at trays was based on temperatures on trays as control variables and it was applied only to simple binary columns. Also, previously developed theoretical models for determining optimal exchanged heat profile were determined only at such columns and while they were approximated they produced worse results than numerical minimum of entropy production. In this paper, as control variables for minimization, exchanged heat on the trays is used. It enables application to complex multicomponent diabatic columns. Ishii-Otto global method, based on model linearization and iterative solution by Newton-Raphson technique, is applied for solving column mathematical model. Needed thermodynamical properties for ideal systems are calculated using Lewis-Randall ideal solution model, and for non-ideal slightly polar systems they are calculated using Soave equation of state. Five direct methods are used for numerical optimization. Applied approach is successfully demonstrated at frequently used example of distillation of benzene and toluol mixture by using for these purposes specially written program. Simplex method appeared to be the most convenient optimization method for the considered problem.


Sign in / Sign up

Export Citation Format

Share Document