Thermo-economic approach to energy from waste /
Clasificación: | Libro Electrónico |
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Otros Autores: | |
Formato: | Electrónico eBook |
Idioma: | Inglés |
Publicado: |
Amsterdam :
Elsevier,
[2022]
|
Temas: | |
Acceso en línea: | Texto completo |
Tabla de Contenidos:
- Front Cover
- A Thermo-Economic Approach to Energy From Waste
- Copyright Page
- Contents
- About the authors
- Preface
- Acronyms and abbreviations
- 1 Pyrolysis of waste biomass: toward sustainable development
- 1.1 Introduction
- 1.2 Component of lignocellulosic biomasses
- 1.2.1 Cellulose
- 1.2.2 Hemicellulose
- 1.2.3 Lignin
- 1.2.4 Ash
- 1.2.5 Extractives
- 1.3 Types of pyrolysis
- 1.3.1 Slow pyrolysis
- 1.3.2 Intermediate pyrolysis
- 1.3.3 Fast pyrolysis
- 1.4 Mechanism of pyrolysis
- 1.4.1 Mechanism of cellulose pyrolysis
- 1.4.2 Mechanism of hemicellulose pyrolysis
- 1.4.3 Mechanism of lignin pyrolysis
- 1.5 Reactor configurations
- 1.5.1 Fluidized-bed reactor
- 1.5.2 Circulating fluidized-bed reactor
- 1.5.3 Ablative plate reactor
- 1.5.4 Auger/screw reactor
- 1.5.5 Rotating cone reactor
- 1.5.6 Cyclone/vortex reactor
- 1.6 Upgradation techniques for pyrolyzed bio-oil
- 1.6.1 Physical upgradation of crude bio-oil
- 1.6.1.1 Hot vapor filtration
- 1.6.1.2 Emulsification
- 1.6.1.3 Solvent addition
- 1.6.2 Chemical upgradation of bio-oil
- 1.6.2.1 Aqueous phase processing/reforming
- 1.6.2.2 Mild Cracking
- 1.6.2.3 Esterification
- 1.6.3 Catalytical upgradation of bio-oil
- 1.6.3.1 Hydrotreating
- 1.6.3.2 Catalytic cracking
- 1.6.3.3 Hydrodeoxygenation
- 1.6.3.4 Steam reforming
- 1.6.3.5 Supercritical fluids
- 1.7 Energy recovery for heating or process applications
- 1.8 Conclusion
- References
- 2 Biomass pyrolysis system based on life cycle assessment and Aspen plus analysis and kinetic modeling
- 2.1 Introduction
- 2.2 Current Indian scenario of waste-to-energy conversion technologies
- 2.3 From biomass to biofuel through pyrolysis
- 2.4 Life cycle assessment methodology for pyrolysis-based bio-oil production
- 2.4.1 Steps followed for studying LCA
- 2.4.2 Setting require for LCA.
- 2.4.3 Inventory data collection
- 2.4.4 Analysis of life cycle inventory
- 2.4.5 Impact assessment of LCA
- 2.4.6 Sensitivity analysis
- 2.5 Aspen plus approach to biomass pyrolysis system
- 2.6 Kinetics of biomass pyrolysis
- 2.7 Isoconversional techniques
- 2.8 Other kinetic models
- 2.9 Application of biomass pyrolysis products
- 2.9.1 Bio-oil applications
- 2.9.1.1 Biochemicals
- 2.9.1.2 Biofuel
- 2.9.1.3 Biopolymer
- 2.9.2 Biochar application
- 2.9.2.1 Soil amendment
- 2.9.2.2 Solid biofuel
- 2.9.2.3 Activated carbon
- 2.10 Conclusions
- References
- 3 Biomass gasification integrated with Fischer-Tropsch reactor: techno-economic approach
- 3.1 Introduction
- 3.2 Surplus biomass available in India
- 3.2.1 Conflicting applications for crop residue biomass
- 3.2.2 Biomass
- 3.2.3 Challenges in biomass utilization
- 3.2.4 Biomass to energy conversion processes
- 3.3 Pretreatment of biomass
- 3.3.1 Torrefaction
- 3.3.1.1 Changes pertaining to that structure
- 3.3.1.2 Physiochemical properties
- 3.3.1.3 Moisture content
- 3.3.2 Types of pretreatment
- 3.3.2.1 Physical pretreatment
- 3.3.2.2 Mechanical methods
- 3.3.2.3 Biological pretreatment
- 3.3.2.4 Enzymatic pretreatment
- 3.3.2.5 Microbial and fungus prevention pretreatment
- 3.3.2.6 Other latest pretreatment
- 3.4 Kinetics of biomass gasification for syngas generation
- 3.4.1 Gasification mechanism
- 3.4.1.1 Drying zone or bunker section
- 3.4.1.2 Pyrolysis or thermal decomposition zone
- 3.4.1.3 Partial oxidation or combustion zone
- 3.4.1.4 Reduction zone
- 3.4.2 Syngas conditioning
- 3.5 Gasification integrated with Fischer-Tropsch reactor
- 3.5.1 Bioenergy potential calculations and estimation
- 3.5.2 Fischer-Tropsch synthesis
- 3.5.3 Fischer-Tropsch catalysts
- 3.5.4 Fischer-Tropsch mechanism.
- 3.5.5 Biofuel synthesis from Fischer-Tropsch reactor
- 3.5.5.1 Slurry bubble column reactors
- 3.6 Techno-economic analysis of Fischer-Tropsch reactor with biomass gasification
- 3.7 Conclusion
- References
- 4 Energy recovery from biomass through gasification technology
- 4.1 Introduction
- 4.2 Thermochemical conversion
- 4.2.1 Combustion
- 4.2.2 Pyrolysis
- 4.2.3 Gasification
- 4.2.4 Principles of anaerobic digestion
- 4.3 Production and use of aquatic biomass
- 4.3.1 Potential of biomass waste
- 4.4 Lignocellulose biomass pretreatment
- 4.4.1 Physical methods
- 4.4.2 Chemical Methods
- 4.4.3 Biological pretreatment
- 4.5 Bioconversion and downstream processing of biomass-derived molecules' conversion to chemicals
- 4.6 Energy recovery for heating or process applications
- 4.6.1 Steam cycle
- 4.6.2 Engine
- 4.6.3 Gas turbine
- 4.6.4 Biogas
- 4.7 Conversion of lignocellulosic biomass-derived intermediates lignin biorefinery biogas from waste biomass
- 4.7.1 Hydrolysis
- 4.7.2 Acidogenesis
- 4.7.3 Acetogenesis
- 4.7.4 Methanogenesis
- 4.8 Parameters affecting anaerobic digestion process
- 4.8.1 Temperature
- 4.8.2 Solid to water content
- 4.8.3 pH level
- 4.8.4 Retention period
- 4.8.5 Organic loading rate
- 4.8.6 C/N ratio
- 4.9 The concept of gasification and its types of reactors
- 4.9.1 Fixed bed gasification
- 4.9.2 Updraft gasifier
- 4.9.3 Downdraft gasifier
- 4.9.4 Cross-flow gasifier
- 4.9.5 Fluidized bed gasification
- 4.9.6 Bubbling fluidized bed gasification
- 4.10 Life cycle analysis of gasification process
- 4.10.1 Scope of analysis and definition
- 4.10.2 Boundary system and analysis of related legislation
- 4.10.3 Proper selection of environmental performance indicators
- 4.10.4 Inventory analysis
- 4.10.5 Environmental impact assessment
- 4.10.6 Life cycle assessment.
- 4.11 Aspen plus approach to the biomass gasification system
- 4.12 Conclusion
- References
- 5 Life Cycle Assessment applied to waste-to-energy technologies
- 5.1 Introduction
- 5.2 What is life cycle assessment?
- 5.2.1 Historical development
- 5.2.2 Applications of LCA
- 5.2.3 Steps and procedures for an LCA study
- 5.2.4 Definition of the objective and scope
- 5.2.5 Analysis of the life cycle inventory
- 5.2.6 Life cycle impact assessment
- 5.2.7 Interpretation
- 5.3 Use of LCA to analyze waste-to-energy technologies
- 5.3.1 Main applications
- 5.4 Highlights in LCA studies for waste-to-energy technologies
- 5.4.1 Functional unit
- 5.4.2 Type of residue
- 5.4.3 Form of energy use
- 5.4.4 Energy recovery
- 5.4.5 Sensitivity and uncertainty analyses
- 5.5 Main results found in the literature
- 5.6 Conclusion
- References
- 6 Waste disposal in selected favelas (slums) of Rio de Janeiro
- 6.1 Historical background
- 6.1.1 Some numbers about subnormal clusters
- 6.1.2 The favela of Catumbi
- 6.2 Survey and study of solid waste in 37 slums and in Catumbi
- 6.3 Final considerations
- References
- 7 Transesterification process of biodiesel production from nonedible vegetable oil sources using catalysts from waste sources
- 7.1 Introduction
- 7.2 Biodiesel production as an alternative source of energy
- 7.3 Transesterification: reaction and mechanism
- 7.4 Catalysts
- 7.4.1 Chemical catalysts
- 7.4.1.1 Homogeneous catalysts
- 7.4.1.2 Heterogeneous catalysts
- 7.4.1.3 Preparation of natural derived heterogeneous catalyst
- 7.4.1.4 Nanocatalysts
- 7.4.2 Biochemical catalysts
- 7.4.3 Impact on kinetics of transesterification and modeling
- 7.4.3.1 Determination of kinetic parameters in a batch process
- 7.4.3.2 Modeling of batch reactor design
- 7.4.3.3 Modeling for continuous reactor design.
- 7.5 Hydrocarbon feed stocks for biodiesel
- 7.5.1 Edible oils
- 7.5.2 Nonedible oils
- 7.6 Various novel technologies for biodiesel production
- 7.6.1 Ultrasonic-assisted biodiesel production
- 7.6.2 Micro reactive transesterification
- 7.6.3 Microwave-assisted biodiesel production
- 7.6.4 Reactive distilled transesterification
- 7.6.5 Supercritical technology of biodiesel production (noncatalytic)
- 7.7 Techno-economic analysis of biodiesel production
- 7.7.1 One-time costs
- 7.7.2 Raw material and operating cost
- 7.7.3 Fixed cost and maintenance cost
- 7.7.4 Cost calculation with respect to production rate
- 7.8 Perspectives and conclusion
- References
- Index
- Back Cover.