Erratum: Towards sustainable separation and recovery of dichloromethane and methanol azeotropic mixture through process design, control, and intensification

Abstract

Journal of Chemical Technology & BiotechnologyEarly View ErratumFree Access Erratum: Towards sustainable separation and recovery of dichloromethane and methanol azeotropic mixture through process design, control, and intensification This article corrects the following: Towards sustainable separation and recovery of dichloromethane and methanol azeotropic mixture through process design, control, and intensification Zong Yang Kong, Ao Yang, Juan Gabriel Segovia-Hernández, Aditya Putranto, Jaka Sunarso, Volume 98Issue 1Journal of Chemical Technology & Biotechnology pages: 213-229 First Published online: October 14, 2022 First published: 03 April 2023 https://doi.org/10.1002/jctb.7372AboutSectionsPDF ToolsRequest permissionExport citationAdd to favoritesTrack citation ShareShare Give accessShare full text accessShare full-text accessPlease review our Terms and Conditions of Use and check box below to share full-text version of article.I have read and accept the Wiley Online Library Terms and Conditions of UseShareable LinkUse the link below to share a full-text version of this article with your friends and colleagues. Learn more.Copy URL It has recently come to our attention that Figures 4-7 in our original research article entitled ‘Towards sustainable separation and recovery of dichloromethane and methanol azeotropic mixture through process design, control, and intensification’ published in Wiley Online Library in the Journal of Chemical Technology and Biotechnology on 12 September 2022, 98 (1): 213–229 (https://onlinelibrary.wiley.com/doi/10.1002/jctb.7237) are not consistent with those in the final version of the proof provided by the journal and approved by the authors. This erratum aims to correct the figures. Figure 4Open in figure viewerPowerPoint Inventory control loop employed in this work for the SSED. Figure 5Open in figure viewerPowerPoint Control structure for CED (Extracted from previous work1). Figure 6Open in figure viewerPowerPoint Effect of different entrainers on VLE of dichloromethane and methanol. Figure 7Open in figure viewerPowerPoint The proposed (a) SSED, (b) TCED, and (c) EDWC using DMF. REFERENCE 1Kong ZY, Yang A, Segovia-Hernández JG, Putranto A and Sunarso J, Towards sustainable separation and recovery of dichloromethane and methanol azeotropic mixture through process design, control, and intensification. J Chem Technol Biotechnol 98: 213– 229 (2023). Early ViewOnline Version of Record before inclusion in an issue FiguresReferencesRelatedInformation