TUHH Open Research
Help
  • Log In
    New user? Click here to register.Have you forgotten your password?
  • English
  • Deutsch
  • Communities & Collections
  • Publications
  • Research Data
  • People
  • Institutions
  • Projects
  • Statistics
  1. Home
  2. TUHH
  3. Publications
  4. Rapid multi-criteria screening of energy-integrated distillation processes for nonideal mixtures
 
Options

Rapid multi-criteria screening of energy-integrated distillation processes for nonideal mixtures

Citation Link: https://doi.org/10.15480/882.15774
Publikationstyp
Journal Article
Date Issued
2025-12-19
Sprache
English
Author(s)
Adami, Momme  orcid-logo
Systemverfahrenstechnik V-4  
Espert, Dennis  
Systemverfahrenstechnik V-4  
Skiborowski, Mirko  orcid-logo
Systemverfahrenstechnik V-4  
TORE-DOI
10.15480/882.15774
TORE-URI
https://hdl.handle.net/11420/57002
Journal
Separation and purification technology  
Volume
377
Article Number
134463
Citation
Separation and purification technology 377: 134463 (2025)
Publisher DOI
10.1016/j.seppur.2025.134463
Scopus ID
2-s2.0-105011544821
Publisher
Elsevier
Several thousand distillation columns are industrially employed for various separations, accounting for a substantial share of the industrial energy demand. In order to reduce their energy requirements various means for energy integration, such as direct heat integration, multi-effect distillation, thermal coupling, or vapor recompression can be applied. Considering these options and combinations of these, several hundred possible process configurations can be designed even for separations into three product streams, while the choice for a best option depends strongly on the specific separation task and system properties. In order to enable a reliable case-specific evaluation, which avoids simplified heuristics or simplified thermodynamics, this article presents a computationally efficient, algorithmic framework for a multi-criteria evaluation of more than 750 energy-integrated distillation sequences for multicomponent separations in three product streams. The framework employs thermodynamically sound pinch-based shortcut models that do not rely on constant relative volatility and constant molar overflow assumptions, making it applicable to nonideal and azeotropic mixtures. Based on the minimum energy duties and the respective flowsheet information, classical estimation methods for equipment sizes, operating costs, and capital investment, are employed. Several case studies demonstrate the framework's applicability to azeotropic systems, its computational efficiency benefits that enable performing sensitivity analyses for varied process, thermodynamic, and economic scenarios.
Subjects
Distillation | Dividing Wall Column | Heat integration | Process intensification | Shortcut screening | Thermal coupling | Vapor recompression
DDC Class
660.6: Biotechnology
621: Applied Physics
Funding(s)
Projekt DEAL  
Lizenz
https://creativecommons.org/licenses/by/4.0/
Publication version
publishedVersion
Loading...
Thumbnail Image
Name

1-s2.0-S1383586625030606-main.pdf

Type

Main Article

Size

9.66 MB

Format

Adobe PDF

TUHH
Weiterführende Links
  • Contact
  • Send Feedback
  • Cookie settings
  • Privacy policy
  • Impress
DSpace Software

Built with DSpace-CRIS software - Extension maintained and optimized by 4Science
Design by effective webwork GmbH

  • Deutsche NationalbibliothekDeutsche Nationalbibliothek
  • ORCiD Member OrganizationORCiD Member Organization
  • DataCiteDataCite
  • Re3DataRe3Data
  • OpenDOAROpenDOAR
  • OpenAireOpenAire
  • BASE Bielefeld Academic Search EngineBASE Bielefeld Academic Search Engine
Feedback