Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water) via heterogeneous azeotropic distillation by energy-saving dividing-wall column: Process design and control strategies
Authors:
- Puyun ShiPSPuyun Shi
- Dongmei XuDXDongmei Xu
- Jinfu DingJDJinfu Ding
- Jingyu WuJWJingyu Wu
- Yixin MaYMYixin Ma
- Jun GaoJGJun Gao
- Yinglong WangYWYinglong Wang
- 1 July 2018
- journal article
- research article
- Published by Elsevier in Chemical Engineering Research and Design
- Vol. 135, 52-66
Abstract
No abstract availableKeywords
Funding Information
- National Scientific Research Foundation of China (21776145)
- Shandong Provincial Key Research & Development Project (2018GGX107001)
This publication has 22 references indexed in Scilit:
- Isobaric Vapor–Liquid Equilibrium for Binary Systems of 2,2,3,3-Tetrafluoro-1-propanol + 2,2,3,3,4,4,5,5-Octafluoro-1-pentanol at 53.3, 66.7, 80.0 kPaJournal of Chemical & Engineering Data, 2016
- Enhanced bioethanol dehydration by extractive and azeotropic distillation in dividing-wall columnsSeparation and Purification Technology, 2012
- Energy efficient control of a BTX dividing-wall columnComputers & Chemical Engineering, 2011
- Remixing Control for Divided-Wall ColumnsIndustrial & Engineering Chemistry Research, 2011
- Applying Model Predictive Control to Dividing Wall ColumnsChemical Engineering & Technology, 2011
- A control perspective on process intensification in dividing-wall columnsChemical Engineering and Processing - Process Intensification, 2011
- New Control Structure for Divided-Wall ColumnsIndustrial & Engineering Chemistry Research, 2009
- Control of the Heterogeneous Azeotropic n-Butanol/Water Distillation SystemEnergy & Fuels, 2008
- Dividing Wall Distillation Columns: Optimization and Control PropertiesChemical Engineering & Technology, 2008
- Peptide dissociation in solution or bound to a polymer: comparative solvent effectTetrahedron, 2004