Thermochemical conversion of lignocellulosic materials : theory, design, and applications for the future /
Thermochemical Conversion of Lignocellulosic Materials: Theory, Design, and Applications for the Future proposes a generalized methodology for the design and study of thermochemical conversion reactors independent of the feedstock used and the technology analyzed.
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| Format: | eBook |
| Language: | English |
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Amsterdam ; Cambridge, MA :
Elsevier,
[2025]
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| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Intro
- Thermochemical Conversion of Lignocellulosic Materials
- Copyright
- Contents
- Contributors
- Preface
- Chapter 1: The role of biomass to address global energy and environmental challenges
- Abbreviations
- 1.1. Population growth, energy, and socioeconomic development
- 1.2. Energy production and greenhouse gas emissions
- 1.3. Energy intensity
- 1.4. Social progress index
- 1.5. National energy balance/energy matrix
- 1.6. Historic evolution of energy consumption
- 1.7. Bioenergy in national energy matrixes
- 1.8. The unique role of biomass in the global C cycle
- 1.9. Accounting for the environmental services of renewable energy
- 1.10. Measuring performance through carbon abatement cost
- 1.11. Questions
- References
- Chapter 2: Biomass resources and supply chains
- 2.1. Introduction
- 2.2. Biomass inventories
- 2.3. Supply chain
- 2.3.1. Biomass collection
- 2.3.2. Grasses and agricultural residues
- 2.3.3. Forest residues
- 2.3.4. Urban wood waste
- 2.3.5. Oilseeds
- 2.4. Transport
- 2.5. Depot and depot sitting
- 2.6. Biomass storage/processing center location
- 2.6.1. Storage warehouse location using the weighted factors method
- 2.6.2. Storage warehouse location using the Brown-Gibson method
- 2.6.3. Storage warehouse location with the center of gravity method
- 2.6.4. Storage warehouse location with the Break-Even method
- 2.6.5. Location of a storage warehouse with the northwest corner method
- 2.6.6. Exhaustive search exact algorithm method
- 2.7. Questions
- References
- Chapter 3: Introduction to thermochemical reactors
- 3.1. Biomass conversion technologies
- 3.2. Camp fire experience
- 3.3. Thermochemical reactions
- 3.4. Thermochemical reactors
- 3.5. Equivalence ratio
- 3.6. Dry thermochemical conversion technologies
- 3.6.1. Torrefaction
- 3.6.2. Carbonization.
- 3.6.3. Fast pyrolysis
- 3.6.4. Gasification with O2
- 3.6.5. Steam gasification
- 3.6.6. Combustion
- 3.7. Wet thermochemical conversion technology
- 3.7.1. Hydrothermal liquefaction
- 3.7.2. Organic solvent liquefaction (solvolysis)
- 3.7.3. Hydrothermal gasification
- 3.7.4. Wet oxidation
- 3.8. Questions
- References
- Chapter 4: Lignocellulosic materials
- 4.1. Introduction
- 4.2. Multiscale structure of lignocellulosic materials
- 4.3. Cellulose
- 4.4. Hemicellulose
- 4.5. Lignin
- 4.6. Extractives
- 4.6.1. Types of extractives
- Phenolics
- Terpenes
- Alkaloids
- Fatty acids
- 4.6.2. Extraction and characterization methods
- 4.7. Quantifying the content of cellulose, hemicellulose, and lignin
- Quantification of cellulose, hemicellulose, and lignin
- 4.8. Mineral composition
- 4.8.1. Inductively coupled plasma spectroscopy (ICP)
- Ashing
- Ash digestion
- 4.8.2. Atomic absorption spectroscopy (AAS)
- 4.8.3. Laser-induced breakdown spectroscopy (LIBS)
- 4.8.4. X-ray fluorescence (XRF)
- 4.8.5. Energy dispersive X-ray (EDX)
- 4.9. Questions
- References
- Chapter 5: Drying, particle size reduction, and densification of lignocellulosic materials
- 5.1. Biomass particles
- 5.1.1. Particle shape
- 5.1.2. Particle size
- 5.1.3. Particle size distribution
- 5.1.4. Mechanical properties
- Youngs modulus
- Tensile strength
- Shearing strength
- Bending strength (also known as flexural strength)
- 5.1.5. Other properties of lignocellulosic powders
- Porosity
- Moisture content
- Flow properties
- 5.2. Biomass particle size reduction process
- 5.3. Grinding of lignocellulosic materials
- 5.4. Factors affecting size reduction mechanical operations
- 5.5. Grinding energy calculations
- 5.6. Biomass feeding in thermochemical reactors
- 5.7. Biomass drying
- 5.7.1. Biomass dryers.
- 5.8. Biomass densification
- 5.9. Biomass particles compression experiments
- 5.10. Questions and problems
- References
- Chapter 6: Experimental techniques to study thermochemical reactions
- 6.1. Thermochemical reactions
- 6.2. The role of parametric studies
- 6.2.1. Effect of temperature
- 6.2.2. Heating rate effect
- 6.2.3. Effect of external pressure
- 6.2.4. Particle size effect
- 6.2.5. Effect of biomass loading (interparticle secondary reactions)
- 6.2.6. Effect of vapors residence time
- 6.3. Thermal analysis
- 6.4. Thermogravimetric analysis
- 6.4.1. Heating layouts and commercial oven types
- 6.4.2. Sampling and sample containers
- 6.4.3. Pressure and reaction environment
- 6.4.4. Temperature measurement
- 6.4.5. Calibration
- 6.4.6. Analysis of the data
- 6.4.7. Challenges in the use of thermogravimetric analysis to study primary reactions
- 6.4.8. Proximate composition
- 6.5. Evolved gas analysis-EGA (TG-MS, TG-FTIR)
- 6.5.1. TG- mass spectrometry (MS)
- 6.5.2. TG-FTIR
- 6.6. Differential thermal analysis and differential scanning calorimetry
- 6.6.1. Differential thermal analysis (DTA)
- 6.6.2. Calorimetric DTA
- 6.6.3. Differential scanning calorimetry (DSC)
- 6.6.4. Power compensated DSC (Fig. 6.29)
- 6.6.5. Modulated temperature differential scanning calorimetry (MTDSC)
- 6.6.6. Quantitative aspects of DTA and DSC curves
- 6.7. Py-MS and Py-GC/MS
- 6.7.1. Pyrolysis gas chromatography-mass spectrometry (Py-GC/MS)
- 6.7.1.1. Furnace pyrolyzer
- 6.7.1.2. Courie-point pyrolyzer
- 6.7.1.3. Resistively filament pyrolyzer
- 6.7.1.4. Py-MS
- 6.8. Py-DART-MS
- 6.9. Spoon reactors
- 6.10. Fluidized bed reactors
- 6.11. Wire mesh reactors
- 6.12. Pulse-heated analysis of solid reactions (PHASR)
- 6.13. Hot rod reactor
- 6.14. Entrained flow reactor.
- 8.5. Estimation of product yields from stoichiometric and kinetic information
- 8.6. Secondary reactions in gas phase
- 8.7. Char oxidation reactions
- 8.7.1. Nonisothermal conditions
- 8.8. Questions
- References
- Chapter 9: Single particle models
- 9.1. Experimental determination of total conversion time
- 9.2. General methodology for the development of single particle models
- 9.3. State of the art of biomass pyrolysis single particle models
- 9.4. Estimation of effective conductivity in biomass and char particles
- 9.4.1. Effective conductivity perpendicular to the fibers
- 9.4.2. Siau model
- 9.4.3. Saastamoinen and Richard model
- 9.4.4. Effective thermal conductivity along the fibers
- 9.5. Particle-scale models for biomass pyrolysis
- 9.6. Analytical solutions for limit cases
- 9.7. Simplified Bamfords pyrolysis single particle model
- 9.8. Single particle models in gasification
- 9.9. Effective diffusivity
- 9.10. Single particle model for gasification
- 9.11. Dimensionless local balance equations
- 9.12. Solutions of the local mass balance equation under limit conditions
- 9.13. Advanced gasification models
- 9.13.1. Solutions of the local mass balance equation under limit conditions for the biochar gasification reaction
- 9.14. Effect of particle size distribution and flow pattern
- 9.15. Questions
- References
- Chapter 10: Estimation of thermodynamic properties
- 10.1. Introduction
- 10.2. Boiling point
- 10.3. Critical properties
- 10.4. Heat capacity
- 10.5. Hansen solubility parameters
- 10.6. Gas enthalpy of formation
- 10.7. Gas standard Gibbs free energy
- References
- Chapter 11: Mass balances in thermochemical processes
- 11.1. Generalities of thermochemical reactions
- 11.2. Concentration expression based on aggregate states
- 11.2.1. Forms to express concentration in solids.