CO2 capture by reactive absorption-stripping : modeling, analysis and design /
| Main Authors: | , , |
|---|---|
| Corporate Author: | |
| Format: | eBook |
| Language: | English |
| Published: |
Cham, Switzerland :
Springer,
[2019]
|
| Series: | SpringerBriefs in energy.
|
| Subjects: | |
| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Intro; Contents; 1 Introduction; 1.1 Pollution and Carbon Dioxide; 1.2 Brief History of Climate Change Science; 1.3 The Climate Change in the Political Debate; 1.4 The Role of the Public Opinion; 1.5 Carbon Capture and Storage Technologies; 1.6 Book Motivations and Objectives; 1.7 Book Overview; References; 2 Process Modeling in Aspen Plus®; 2.1 Process Description; 2.2 Building the Model in Aspen Plus®; 2.3 Properties Environment; 2.3.1 Components; 2.3.2 Thermodynamics; 2.4 Simulation Environment; 2.4.1 Streams Characterization; 2.4.2 Chemical Reactions; 2.5 The Aspen Plus® RadFrac" Model
- 2.5.1 Equilibrium Stages Mode2.5.2 Rate-Based Mode; 2.5.2.1 Bulk Modeling; 2.5.2.2 Film Modeling-Resistances; 2.5.2.3 Film Modeling-Liquid Film Discretization; 2.5.2.4 Rate-Based Model Parameters Evaluation; 2.6 Analysis of the Fluid Dynamics; 2.6.1 Axial Diffusion/Dispersion-Peclet Number Analysis; 2.6.2 Backmixing Due to the Countercurrent; 2.6.3 The Number of Segments Analysis; References; 3 Model Validation for the Absorber; 3.1 Absorption Section Case Studies; 3.2 The Temperature Bulge; 3.3 Peclet Number Analysis; 3.4 Backmixing Due to the Countercurrent Effect
- 3.5 Rate-Based Model Set-Up3.5.1 Rate-Based Correlations; 3.5.2 Liquid Film Discretization Parameters; 3.6 Laboratory-Scale Plant: Run T22; 3.6.1 Number of Segments Analysis; 3.6.2 Comparison with the Experimental Data; 3.7 Large-Scale Plant: Run 1-A2; References; 4 Model Validation for the Stripper; 4.1 Introduction to the Stripping Section Modeling; 4.2 Stripping Section Case Studies; 4.3 Stripper Degrees of Freedom; 4.4 Peclet Number Analysis; 4.5 SINTEF Plant: Run 1; 4.6 UTA Plant: Run 47; References; 5 Absorption Section Design Analysis
- 5.1 Introduction to the Design of an Industrial CO2-MEA Reactive Absorption Plant5.2 Process Description; 5.3 Feed Streams Characterization; 5.4 Absorber Analysis and Design Implications; 5.4.1 Evaluation of the Minimum Number of Absorbers and the Minimum Solvent Flow Rate; 5.4.2 The Role of the Temperature Bulge in the Absorber Design; 5.4.3 Evaluation of the Effective Solvent Flow Rate and the Effective Column Dimensions; 5.4.3.1 L/V Ratio Analysis; 5.4.3.2 Absorber Liquid Temperature Profiles; 5.4.3.3 Absorber Dimensions; 5.5 Absorber Design Procedure Summary; References
- 6 Stripping Section Design Analysis6.1 Introduction to the Design of an Industrial CO2-MEA Reactive Stripping Plant; 6.2 Stripper Configuration; 6.3 Stripper Operating Conditions; 6.3.1 Stripper Pressure; 6.3.2 Condenser Temperature; 6.3.3 Stripper Performance; 6.4 Stripper Analysis and Design Implications; 6.4.1 Rich Solvent Characterization; 6.4.2 Effect of the Packing Height; 6.5 Stripper Design Procedure Summary; References; 7 Complete Flowsheet and Economic Evaluation; 7.1 Introduction; 7.2 Complete Flowsheet; 7.3 Cross Heat-Exchanger; 7.3.1 Effect of the Stripper Feed Temperature