583 Process Intensification through Process Systems Engineering


Description:
Process intensification (PI) is a rapidly developing field that can be exploited for high throughput, resulting in lowering capital and operating cost. Various options for PI include multiple processes integration, mass and heat transfer enhancement, and process simplification, etc. Options for PI can be identified and realized on different scales of a chemical process and include e.g. the realization of new reaction routes (new catalysts), the use of innovative solvents, novel reactors, integrated processes (e.g. reactive or hybrid separations) or new (e.g. dynamic) operating modes. Papers on practical implementations as well as methodological contributions are equally welcome.

Sponsor:
Systems and Process Design
Co-Sponsor(s):
Process Intensification & Modular Chemical Processing (T6B)


Chair:
M. M. Faruque Hasan
Texas A&M University
Artie McFerrin Department of Chemical Engineering
College Station, TX
77843
Email: hasan@tamu.edu

Co-Chair:
Ankur Kumar
Development Specialist
Praxair Technology Center
Global Productivity and Analytics
1 University Station C0400
Tonawanda, NY
78712
Email: Ankur_Kumar@Praxair.Com


Papers:
A Reactive Distillation Optimization Model for Low- and High-Temperature Fischer–Tropsch Syntheses for Multiphase Product Recovery
Yanyan Hu, Carnegie Mellon University; Naien He, Carnegie Mellon University; Yizu Zhang, Carnegie Mellon University; Cornelius Mduduzi Masuku, Carnegie Mellon University; Lorenz T. Biegler, Carnegie Mellon University
Design and Intensification of Sorption-Enhanced Reaction Processes for Methanol Production
Akhil Arora, Texas A&M University; Shachit S. Iyer, Texas A&M University; Ishan Bajaj, Texas A&M University; M. M. Faruque Hasan, Texas A&M University
Comparison of Adsorptive Separation Performance of a Hollow Fiber Bed and a Packed Bed: A Modeling Study Using Zeolite 13X and a Mixture of Propylene and Propane
Trisha Sen, Georgia Institute of Technology; Yoshiaki Kawajiri, Georgia Institute of Technology; Matthew J. Realff, Georgia Institute of Technology
Towards a Systematic Process Intensification Framework for Advanced Distillation Systems
Yuhe Tian, Texas A&M University; M. Sam Mannan, Texas A&M University; Efstratios N. Pistikopoulos, Texas A&M Energy Institute, Texas A&M University
Compact, Nonsmooth Operators for Single-Component Mass and Water Integration
Caroline Nielsen, Process Systems Engineering Laboratory, Massachusetts Institute of Technology; Paul I. Barton, Massachusetts Institute of Technology
Optimal Mass Exchanger Network Synthesis Using a 2-Step Hybrid Algorithm Including Packed Column Design
Michael Short, Carnegie Mellon University; Lorenz T. Biegler, Carnegie Mellon University; Adeniyi J. Isafiade, University of Cape Town
Mathematical Optimization of Sustainable Water Desalination Processes Using Directional Solvent Extraction
Alejandro Garciadiego, University of Notre Dame; Tengfei Luo, University of Notre Dame; Alexander W. Dowling, University of Notre Dame
Abstract Submissions Closed
See more of this Group/Topical: Computing and Systems Technology Division