- •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
1.4.4.Direct electric storage
The energy can be stored directly in ultracapacitors and superconducting magnetic energy storage units [1, 2].
A capacitor stores energy in the electric field between two electrodes in the form of thin rolled plates with a dielectric between them. The ultracapacitor, also known as supercapacitor, electrochemical capacitor, or electric double layer capacitor (EDLC) is a capacitor which uses a thin electrolyte instead of a dielectric and electrodes made of porous carbon in order to increase the energy density. The specific energy obtained is about 15Wh/kg.
Ultracapacitors are useful for power-quality management and for regulating voltage in automotive systems during regular driving conditions. They can also work in tandem with batteries and fuel cells to relieve peak power needs.
Supercapacitors generally are very durable (10–12 years life span), have very high cycle life (over 500 000 cycles) and efficiency (95%) and 5% per day self-discharge.
The energy storage in superconducting magnetic energy storage (SMES) system is achieved in the magnetic field created by inducing direct current into a coil made of superconducting material which operates at very low temperature (-270°C). The cryogenically cooled, superconducting material has very low electrical resistance. The energy loss of only 0.1% is duet of energy required by cooling system. SMES systems can operate at (97–98)% efficiency and are useful for providing reactive power on demand. A SMES system can provide full power within 100 ms. A SMES system with capacity of 18000 GJ requires a coil with diameter of 300-1000 m. These systems are capable of discharging the near totality of the stored energy, as opposed to batteries.
1.4.5.Electrochemical energy storage
The technologies which store energy as electrochemical energy are the following:
rechargeable batteries (Lead–acid, Lithium-ion, Nickel–cadmium, Nickel–metal hydride, Zebra, Sodium–sulfur);
flow batteries (Vanadium redox, Polysulfide bromide, Zinc bromide);
electrolytic hydrogen.
The storage battery is known as a secondary cell because its electrochemical reactions are electrically reversible.
There is a wide range of technologies used in fabrication of rechargeable batteries which can provide high energy densities (up to 200 Wh/kg for Lithium-ion) [1]. The main disadvantage is their relatively low durability for large-amplitude cycling (a few 100 to a few 1000 cycles). Relative positioning of different storage battery types is shown in Fig. 5.
Figure 5. positioning of the different storage batteries according to their energy density and power [1].
Gaseous hydrogen (H2) can be manufactured using electrolysis, an electric current applied to water separates it into O2 and H2. The resulting hydrogen can be stored and later combusted to provide heat or work, or to power a fuel cell.
Unlike secondary batteries, the flow batteries store and release electrical energy in two liquid electrolytes by means of reversible electrochemical reaction that occur in a set of cells connected in series and/or parallel (Fig. 6). A cell has two compartments separated by an ion exchange membrane. The aqueous electrolytic solutions are contained in separate tanks and during the normal operation are pumped through the electrochemical cell where the reactions occur, with ion or proton exchange through the membrane and electron exchange through the external electric circuit. during the charge process, the electrolyte A is oxidized at the anode, while the electrolyte B is reduced at the cathode.
Figure 6. Description of flow battery energy storage system [4].
the main advantages of the flow batteries are: the capacity can be increased by simply increasing the quantity of liquid electrolytes; the battery can be fully discharged without side effects; have little loss of electrolyte over time and have one of lowest self-discharge rates. The installation cost becomes lower with the increase of system size. The power capacity depends on the cell number and the size of the electrodes [4]. There are three types of flow batteries on commercialization: vanadium redox, polysulfide bromide, and zinc bromide. The overall electricity storage efficiency is about 75%. They are useful in utility-scale power shaping and smoothing application and might be adaptable for distributed-generation use [2].
