Control and Safety Analysis of Intensified Chemical Processes /

Bibliographic Details
Corporate Author: Knovel (Firm)
Other Authors: Patle, Dipesh Shikchand (Editor), Rangaiah, Gade Pandu (Editor)
Format: eBook
Language:English
Published: Weinheim : Wley-VCH, [2024]
Subjects:
Online Access:Connect to the full text of this electronic book
Table of Contents:
  • Preface
  • Part I Overview and Background
  • 1 Introduction 3 Dipesh Shikchand Patle and Gade Pandu Rangaiah
  • 1.1 Process Intensification
  • 1.2 Need for Control and Safety Analysis of Intensified Chemical Processes
  • 1.3 Studies on Control and Safety Analysis of Intensified Chemical Processes
  • 1.4 Scope and Organization of the Book
  • 1.5 Conclusions
  • References
  • 2 Applications and Potential of Process Intensification in Chemical Process Industries 15 Chirla C.S. Reddy
  • 2.1 Introduction
  • 2.2 Benefits of Process Intensification Techniques
  • 2.3 Static Mixers
  • 2.4 Process Intensification for Separation Vessels
  • 2.5 Process Intensification for Distillation
  • 2.6 Process Intensification for Heating
  • 2.6.1 Steam Injection Heater
  • 2.6.2 Steam/Electric Heaters as a Replacement for Fired Heaters
  • 2.6.3 Process Intensification for Flue Gas Heat Recovery
  • 2.6.4 Process Heat Exchangers
  • 2.6.5 Sonic Horn
  • 2.7 Steam Compression
  • 2.8 Process Intensification for Carbon Capture
  • 2.9 Process Intensification for Vacuum Systems
  • 2.10 Process Intensification for Water Deaeration
  • 2.11 Process Intensification for Development of Inherently Safer Design (isd)
  • 2.12 Process Intensification for Reducing Pressure Relief and Handling Requirements
  • 2.12.1 Non-safety Instrumented Solutions for Pressure Relief Systems
  • 2.12.2 Safety Instrumented System (SIS) Solutions for Reducing Pressure Relief Requirements
  • 2.13 Process Intensification for Wastewater Recovery
  • 2.14 Challenges of Process Intensification Techniques
  • 2.15 Conclusions
  • References
  • Part II Procedures and Software for Simulation, Control and Safety Analysis
  • 3 Simulation and Optimization of Intensified Chemical Processes 49 Zemin Feng and Gade Pandu Rangaiah
  • 3.1 Introduction
  • 3.2 Simulation of Chemical Processes
  • 3.2.1 Usefulness of Process Simulation
  • 3.2.2 Commercial Process Simulators
  • 3.2.3 Free Process Simulators
  • 3.2.4 Computational Methods for Process Simulation
  • 3.3 Procedure for Simulation of (Intensified) Chemical Processes
  • 3.3.1 Problem Analysis
  • 3.3.2 Basic Process Flow Design
  • 3.3.3 Process Intensification and Integration
  • 3.3.4 Model Construction
  • 3.3.5 Simulation and Convergence
  • 3.3.6 Results Analysis
  • 3.4 Optimization of (Intensified) Chemical Processes
  • 3.4.1 Mathematical Optimization Methods
  • 3.4.2 Optimization of Chemical Processes with a Process Simulator
  • 3.4.2.1 Optimization Using MATLAB
  • 3.4.2.2 Optimization Using Python
  • 3.5 Challenges in the Simulation/Optimization of Intensified Chemical Processes
  • 3.6 Case Study
  • 3.6.1 Problem Analysis
  • 3.6.2 Process Flow Design
  • 3.6.3 Model Construction
  • 3.6.4 Simulation and Convergence
  • 3.6.4.1 Process Simulation
  • 3.6.4.2 Economic Evaluation Criterion
  • 3.6.4.3 Process Optimization
  • 3.6.5 Results and Analysis
  • 3.7 Conclusions
  • References
  • 4 Dynamic Simulation and Control of Intensified Chemical Processes 83 Zemin Feng and Gade Pandu Rangaiah
  • 4.1 Introduction
  • 4.2 Dynamic Simulation of Chemical Processes
  • 4.2.1 Understanding Dynamic Simulation
  • 4.2.2 Applications of Dynamic Simulation
  • 4.2.3 Dynamic Simulation Software
  • 4.3 Dynamic Simulation and Control Procedure
  • 4.4 Dynamic Simulation and Control of Intensified Chemical Processes
  • 4.4.1 Challenges Due to Process Intensification
  • 4.5 Process Control
  • 4.5.1 Controlled, Manipulated, and Disturbance Variables
  • 4.5.2 Typical Control Loop
  • 4.5.3 Control Degrees of Freedom
  • 4.6 Case Study
  • 4.6.1 Steady-state Simulation and Optimization
  • 4.6.2 Preparation/Initialization for Dynamic Simulation
  • 4.6.3 Control Structure Design
  • 4.6.3.1 Composition Control Scheme
  • 4.6.3.2 Temperature Control Scheme
  • 4.6.4 Tuning of Controller Parameters
  • 4.6.5 Analysis of Dynamic Simulation Results
  • 4.7 Conclusions
  • References
  • 5 Safety Analysis of Intensified Chemical Processes 125 Masrina Mohd Nadzir, Zainal Ahmad, and Syamsul Rizal Abd Shukor
  • 5.1 Introduction
  • 5.2 Safety Analysis in Chemical Process Industry
  • 5.2.1 Safety Analysis Tools
  • 5.2.1.1 Hazard Identification
  • 5.2.1.2 Risk Assessment
  • 5.2.1.3 Inherently Safer Design (ISD)
  • 5.2.1.4 Safety Instrumented Systems
  • 5.2.1.5 Human Factors and Safety Culture
  • 5.2.1.6 Regulatory Framework and Compliance
  • 5.2.1.7 Monitoring and Continuous Improvement
  • 5.3 Process Intensification and Safety Analysis
  • 5.3.1 Impacts of Process Intensification on Safety
  • 5.3.2 Safety Analysis in Intensified Process Design
  • 5.3.2.1 Hazard Identification Techniques for Process Intensification Technologies
  • 5.3.2.2 Risk Assessment for Process Intensification Technologies
  • 5.3.3 Inherently Safer Design Principles Intensified Processes
  • 5.4 Safety Management Systems for Intensified Processes
  • 5.5 Safety Training and Competency for Intensified Processes
  • 5.5.1 Importance of Safety Training and Competency
  • 5.5.2 Developing Safety Training and Competency Programs
  • 5.5.3 Utilizing a Blended Learning Approach
  • 5.5.4 Assessing Training Effectiveness and Continual Improvement
  • 5.5.5 Benefits of Effective Safety Training and Competency Management
  • 5.6 Case Studies of Safety Analysis in Intensified Processes
  • 5.7 Conclusions
  • References
  • Part III Control and Safety Analysis of Intensified Chemical Processes
  • 6 Control of Hybrid Reactive-Extractive Distillation Systems for Ternary Azeotropic Mixtures 157 Zong Yang Kong and Hao-Yeh Lee
  • 6.1 Introduction
  • 6.2 Steady-state Design of the RED
  • 6.3 Dynamic Simulation Setup
  • 6.4 Inventory Control Setup
  • 6.5 Sensitivity Analysis
  • 6.6 Quality Control Structures
  • 6.6.1 Control Structure 1 (CS 1) - Simple Temperature Control
  • 6.6.2 Control Structure 2 (CS 2) - Triple Point Temperature Control
  • 6.6.3 Control Structure 3 (CS 3) - Triple Point Temperature Control Using SVD Analysis
  • 6.6.4 Feedforward Control Structure 3 (FF-CS 3)
  • 6.7 Control Performance Evaluation
  • 6.8 Conclusions
  • Acknowledgements
  • Acronyms
  • Nomenclature
  • References
  • 7 Process Design and Control of Reactive Distillation in Recycle Systems 183 Mihai Daniel Moraru, Costin Sorin Bildea, and Anton Alexandru Kiss
  • 7.1 Introduction
  • 7.2 Design of Reactive Distillation Processes
  • 7.3 Control of Reactive Distillation Processes
  • 7.4 Case Study: RD Coupled with a Distillation-Reactor System and Recycle
  • 7.4.1 Basis of Design and Basic Data
  • 7.4.2 Process Design
  • 7.4.3 Process Control
  • 7.4.4 Discussion
  • 7.5 Conclusions
  • References
  • 8 Dynamics and Control of Middle-vessel Batch Distillation with Vapor Recompression 209 Radhika Gandu, Akash Burolia, Dipesh Shikchand Patle, and Gara Uday Bhaskar Babu
  • 8.1 Introduction
  • 8.2 Conventional Middle-vessel Batch Distillation
  • 8.2.1 A Systematic Simulation Approach of CMVBD
  • 8.2.1.1 Model Equations
  • 8.2.2 Constant Composition Control
  • 8.3 Single-stage Vapor Recompression in Middle-vessel Batch Distillation
  • 8.3.1 A Systematic Simulation Approach of SiVRMVBD
  • 8.4 Performance Specifications
  • 8.4.1 Energy Savings
  • 8.4.2 Total Annual Cost
  • 8.4.3 Greenhouse Gas Emissions
  • 8.5 Results and Discussion
  • 8.5.1 Conventional Middle-vessel Batch Distillation Column
  • 8.5.1.1 Dynamic Composition Profiles
  • 8.5.2 Single-stage Vapor Recompression in Middle-vessel Batch Distillation
  • 8.5.3 Energetic, Economic, and Environmental Performance: CMVBD vs. SiVRMVBD
  • 8.5.4 Constant Composition Control
  • 8.5.4.1 SiVRMVBD-GSPI
  • 8.5.5 Energetic, Economic, and Environmental Performance: CMVBD vs. Controlled CMVBD and SiVRMVBD
  • 8.6 Conclusions
  • References
  • 9 Safety Analysis of Intensified Distillation Processes Using Existing and Modified Safety Indices 237 Savyasachi Shrikhande, Gunawant K. Deshpande, Gade Pandu Rangaiah, andDipeshShikchandPatle
  • 9.1 Introduction
  • 9.2 Safety Indices for Process Safety Assessment
  • 9.3 Description of Distillation Systems
  • 9.3.1 Conventional Sequence of Columns
  • 9.3.2 Dividing-Wall Column
  • 9.3.3 Dividing-Wall Column with Mechanical Vapor Recompression
  • 9.4 Selection of Safety Indices
  • 9.5 Results and Discussion
  • 9.5.1 Conventional Sequence of Columns
  • 9.5.2 Dividing-Wall Column
  • 9.5.3 Dividing-Wall Column with Mechanical Vapor Recompression
  • 9.5.4 Comparative Analysis
  • 9.6 Survey of Engineers and Discussion of their Responses
  • 9.7 Improved PRI
  • 9.8 Conclusions.