- •Energy Saving Technologies Riga Technical University
- •Content
- •Introduction 10
- •1. Energy Saving Technologies in generation, conversion of electrical energy 11
- •Executive summary
- •Introduction
- •1.Energy Saving Technologies in generation, conversion of electrical energy
- •1.1.Cogeneration
- •1.1.1.Introduction
- •1.1.2.Performance indices of cogeneration systems
- •1.1.3.Types of cogeneration systems
- •Comparison of Fuel Cell Systems [12].
- •1.1.4.Distributed energy resources
- •Characteristics of cchp Systems [15].
- •References
- •1.2.Smart metering concept
- •1.2.1.Introduction
- •1.2.2.Communication concept of smart metering
- •1.2.2.1.Customer domain
- •1.2.2.2.Critical infrastructure energy domain
- •1.2.2.3.The utility business market communication domain
- •1.2.2.4.Third parties services - data analysis
- •Ip service provider’s domain
- •1.2.3.Wireless sensor networks in smart metering
- •1.2.3.1.Main characteristics of wireless sensor networks
- •1.2.3.2.Examples of application of wireless sensor networks
- •1.2.4.Security issues
- •1.2.5.The future of smart metering
- •1.3. Energy from biomass
- •1.3.1. Biomass resources
- •Yeld of Som Biomass Types [2].
- •Yield of Agricultural Residues [2].
- •1.3.1.Biomass conversion technologies
- •Characteristics of Solid Biofuels and their Effects.
- •Ultimate Analysis of Different Solid Biofuels (Dry Basis) [5, 6, 7].
- •Proximate Analysis of Solid Biofuels (Dry Basis) [5, 6, 7].
- •Characteristics of Compacted Biomass [2].
- •Higher Heating Value of Solid Biofuels [8, 9, 10].
- •Composition of Biomass Ash [5, 13].
- •Types of Biomass Furnaces [14].
- •Heat Capacity of Combustible Gas [17].
- •Contaminants in Combustible Gas: Problems and Cleanup Methods [17].
- •Syngas Quality Parameters.
- •Operating Parameters of Pyrolysis Processes.
- •1.4.Energy Storage
- •1.4.1.Introduction
- •1.4.2.Classification of energy storage technologies
- •Types of Energy Storage Technologies and Their Applications [2].
- •1.4.3.Characteristics of energy storage techniques
- •1.4.4.Direct electric storage
- •1.4.5.Electrochemical energy storage
- •1.4.6.Mechanical energy storage
- •The response time of sudden changes in electrical demand for power plants [5].
- •1.4.7.Thermal energy storage
- •Physical Properties of Sensible Energy Storage Media [7, 8]
- •Commercial Phase Change Materials which can be Used for Heat Storage in the Buildings [10].
- •Properties of Some Phase Change Materials Produced by eps Ltd, uk [11].
- •Properties of Some Phase Change Materials Produced by teap Energy, Australia [11].
- •Properties of some phase change materials (paraffins) produced by the Rubitherm GmbH Germany [11].
- •Chemical Storage Materials and Reactions [8].
- •Main Characteristics of Energy Storage Materials [8].
- •References
- •1.5.Waste heat recovery
- •1.5.1.Characteristics of waste heat
- •Sources of waste heat at high-temperature range [2].
- •Sources of Waste Heat at Medium-Temperature Range [2].
- •Sources of Waste Heat at Low-Temperature Range [2].
- •1.5.2.Waste heat recovery systems
- •Waste Heat Recovery Systems [3].
- •Heat Exchangers Characteristics.
- •References
- •1.6.Energy Saving Technologies of the Thermochemical Conversion of Biomass and lignocarbonaceous Waste
- •1.6.1.Introduction
- •1.6.2.Pyrolysis
- •1.6.3.1.2 Torrefaction
- •1.6.4.1.3 Fast pyrolysis
- •1.6.5.1.4. Flash and ultra-rapid pyrolysis
- •1.6.6.1.5. Solar driven pyrolysis
- •1.6 Pyrolizer types
- •1.7.Gasification
- •1.8. Poly-generation of heat, power and biofuel
- •1.9.Design of renewable energy systems for small (local) consumers - description of a software for design and examples of design exercises.
- •1.9.1.Introduction.
- •1.9.2.A software for design renewable energy systems.
- •1.9.3.Description of the polysun platform
- •1.9.3.1.Polysun modules
- •1.9.3.2.User Interface
- •1.9.3.2.1.Menu bar
- •1.9.3.2.2.Icon bar
- •1.9.3.2.3.Managing the project.
- •1.9.3.2.4.Project tools
- •1.9.4.Creating a project
- •1.9.4.1.Design steps of the simple solar system.
- •1.9.4.2.Design steps of the pv system.
- •1.9.5.Result analysis and reports
- •1.9.5.1.The results of simulation
- •1.9.5.2.Reports
- •1.9.6.Literature
- •Conclusion
- •2.Energy Saving Technologies in transmission, distribution of electrical energy Energy Cost and Power Loss Minimization in Distribution Networks with Distributed Generation
- •Introduction
- •2.1.Opf problem formulation for distribution networks
- •2.1.1.Objective function
- •2.1.2.Constraints
- •Dg units modeling for optimal power flow
- •Opf Solution Using Multi-objective Genetic Algorithm
- •Opf Solution Using Gravitational Search Algorithm
- •2.2.Dc transmission systems
- •3. Energy Saving Technologies: in industry
- •3.1. Electric Motors
- •3.2. Electrical Drives
- •3.1.Waste heat utilization technologies
- •Introduction
- •1 Sources of waste heat
- •2 Main definitions used for heat waste assessment
- •3 Using of waste heat for heating and hot water supply. Equipment for using of industrial waste heat
- •3.1 Closed-circuit schemes of waste heat utilization
- •3.2 Opened-circuit schemes of waste heat utilization
- •Indirect Contact Condensation Recover
- •4. Utilization of low-temperature heat waste
- •4.1 Heat pumps
- •Common types of industrial heat pumps
- •4.2 Applications of heat pumps in drying process
- •4.2.1 Closed-cycle mechanical heat pumps for lumber drying
- •4.2.2 Evaporation - open-cycle mechanical vapour compression (mvc) for sugar solution concentration
- •4.2.3 Thermo-compression for paper-dryer flash steam recovery
- •4.3 Heat pumps working fluids
- •5 Using of waste heat for power generation
- •5.1 The opportunity for waste heat to power generation
- •5.2 Applicable Technologies
- •5.3 Applications
- •Using of combustible waste
- •7 Economic efficiency analysis of heat waste utilization
- •4.Energy Saving Technologies: in public and private sector
- •4.1.Building: fundamental physical processes in buildings and building envelopes. Reduction of heat losses. Heating and conditioning. Heat pumps.
- •5.Supercapacitors
- •Viesturs Brazis
- •5.1.Supercapacitor energy storage
- •5.1.1.Introduction
- •5.1.2.Supercapacitor design
- •5.1.3.Supercapacitor energy storage systems
- •5.1.4.Simulation of supercapacitor energy storage system
- •5.1.5.Ess scaling
- •5.1.6.Conclusions
- •5.1.7.Tasks
- •References
- •5. Standartisation and legal bases on existing Energy Saving Technologies
- •5.2.Introduction
- •5.3.Legistlative base mandatory for eu Member states
- •5.4.Legistlative base non - mandatory for eu Member states
- •5.5.Eu supported actions for development of Energy Saving Technologies
- •5.6.Iso 50001 - Energy management
- •5.7.Conclusions
- •References
1.3.1.Biomass conversion technologies
Except the cases the direct combustion is suitable, raw biomass requires conversion into solid, liquid or gaseous fuels, which can be used for the production of heat and electricity and as a fuel for transportation. This conversion is carried out by mechanical, thermo-chemical or biological processes (Fig. 1). The mechanical processes are used for biomass pre-treatment as: waste sorting and compacting, wood residues compacting in bales, pellets and briquettes, chopping of straw and stalks and oilseeds pressing.
Figure 1. Main conversion processes of biomass.
A comparison of energy carriers produced from biomass can be made based on their ability to produce heat, electricity and transportation fuels. A useful way of comparing biomass and fossil fuels is based on their ratios O/C and H/C, known as Van Krevelen diagram (Fig. 2). The energy content of fuels is higher when the ratios are lower.
Figure 2. Chemical composition of solid fuels [2].
1.2.2.1. Biomass combustion
During the combustion process, a biomass particle passes through several phases, more or less distinct. First, the particle is dried until the temperature reaches 100C and then pyrolysis and/or gasification occurs followed by gas phase oxidation and combustion of char (Fig. 3). The time used for each reaction depends on the fuel size and properties, temperature and conditions of combustion. Combustion of a small particle shows a distinct separation with time between volatile and char combustion phases. At large particle combustion the phases overlap to a certain extent. In the continuously operating combustion systems the consecutive reactions occur simultaneously at different places in the furnace. A distinct separation of different combustion steps allows combustion optimisation by furnace design. The relative importance of each phase depends on the type of biomass, technology and process. Drying is realised by heat absorbing from the environment. The maximum water content of biomass to support combustion should not exceed 60% (mass). Humidity is a very important biomass property which influences the combustion plant design and the progress of combustion process.
Figure 3. Combustion phases of a biomass particle [2].
The main combustion parameter is the excess air ratio (λ) defined as the ratio between the available and the stoichiometric amount of combustion air.
Considering that CH1.44O0.66 is the average composition of typical solid biofuel, the combustion reaction can be described with the following equation [3]:
(1)
The conversion efficiency of biomass into electricity is about (20-25)%. Biomass can be burned directly or burned together with coal (co-combustion). Modern boilers are designed to use the co-combustion to reduce CO2 emissions. In the design of the combustion system the characteristics of the fuel that is to be used, environmental legislation, cost and performance of the available equipment are taken into account.
The solid biofuel combustion is influenced by its physical characteristics and chemical composition.
Properties of solid biofuels
Biomass differs from coal in respect of organic and inorganic materials content, heating value and physical properties. Biomass has generally less carbon, aluminum and iron and more oxygen, silica, and potassium, lower calorific value, higher water content, lower density and lower friability. Biomass combustion process differs from coal combustion due to the biomass composition, especially higher volatile content. pulverized biomass combustion is dominated by devolatilisation and gas phase combustion as opposed to coal combustion, which is dominated by the formation of char and gas-solid oxidizing. The calorific value of biomass is much lower than that of the coal because of the high content of moisture and oxygen. Solid biofuels have higher volatile matter content (70-80%) than coal (10-15%).
Combustion properties of biomass can be classified into physical, chemical, thermal and mineral. The physical properties have large variation and those like density, porosity and inner surface are connected to the wood specie, and the bulk density and granulation are related to preparation methods of solid biofuel. Chemical properties are: elemental analysis, proximate analysis, higher heating value, calorific value of volatiles and calorific value of char. The values of thermal properties such as specific heat, thermal conductivity and emissivity vary with the moisture content, temperature and degree of thermal decomposition. The products of thermal decomposition of wood-based fuels are: moisture, volatile, char and ash. Some properties vary with species and growing conditions of biomass. Other properties depend on the combustion conditions. Biomass characteristics that influence combustion are: granulation, ash and moisture content and content of the structural constituents (cellulose, hemi-cellulose and lignin). table V shows the properties of solid biofuels and their main effects.
