- •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
2 Main definitions used for heat waste assessment
- Waste heat - the energy of heat that is produced in a technological process and could be used in another process, such as heating feedwater or air, power generation, etc, or dumped heat that can still be used;
- The amount of recoverable heat – the total heat that could potentially be recovered from waste heat for space heating, hot water supply or power generation and etc. in heat waste exchanger or other device; it can be calculated using this formula:
where, Q - is the heat content in kcal; V - is the flow rate of the substance in m3/hr; r - is density of the flue gas in kg/m3; Cp - is the specific heat of the substance in kCal/kg 0C; ∆T - is the temperature difference in 0C.
The annual heat saving – the amount of recoverable heat that can be saved per year due to waste heat utilization;
- Fuel saving – the amount of gas, oil, etc., that can be saved due to recoverable heat from waste heat utilization.
- Payback period - the period of time required for the return on an investment to "repay" the sum of the original investment.
- Secondary energy resources.
3 Using of waste heat for heating and hot water supply. Equipment for using of industrial waste heat
The industrial sector accounts for approximately one third of all energy used.
Efforts to improve industrial energy efficiency focus on reducing the energy consumed by the equipment used in manufacturing (e.g., boilers, furnaces, dryers, reactors, separators, motors, and pumps) or changing the processes or techniques to manufacture products. A valuable alternative approach to improving overall energy efficiency is to capture and reuse the lost or "waste heat" that is intrinsic to all industrial manufacturing. In some cases, such as industrial furnaces, efficiency improvements resulting from waste heat recovery can improve energy efficiency by 10% to as much as 50%.
Captured and reused waste heat is an emissionfree substitute for costly purchased fuels or electricity. Numerous technologies are available for transferring waste heat to a productive enduse. Nonetheless, a great amount of waste heat energy remains unrecovered as a consequence of industrial manufacturing.
Three essential components are required for waste heat recovery: 1) an accessible source of waste heat, 2) a recovery technology, and 3) a use for the recovered energy. Topics investigated for each waste heat source include waste heat quantity and quality, available recovery technologies, and barriers to implementing heat recovery. The results of this analysis are used as the basis for identifying needs that can increase industrial energy efficiency by improving waste heat recovery technologies.
Each waste heat stream is investigated in terms of its waste heat quantity (the approximate energy contained in the waste heat stream), quality (typical exhaust temperatures), current recovery technologies and practices, and barriers to heat recovery. Energy content of waste heat streams is a function of mass flow rate, composition, and temperature, and is evaluated based on process energy consumption, typical temperatures, and mass balances. The work potential (based on Carnot efficiency) is a measure of the maximum energy that could be recovered by using the waste heat to drive a heat engine. Quantifying work potential allows a better comparison of waste heat sources with different exhaust temperatures.
The potential for heat recovery is further scoped out by discussing current waste heat recovery practices and barriers to heat recovery for each unit assessed. Finally, the results from the bottomup analysis of waste heat sources are used to identify technology development needs for wider implementation of industrial waste heat recovery. Technology needs are discussed in the context of existing technologies, which can be further optimized, as well as developing technologies that may provide new opportunities for heat recovery.
Investigation of current waste heat recovery practices shows that waste heat is generally recovered from clean, hightemperature waste heat sources in large capacity systems. Key opportunities are available in optimizing existing systems, developing technologies for chemically corrosive systems, recovering heat from nonfluid heat sources, and recovering lowtemperature waste heat.
Waste heat recovery systems are frequently implemented, but constrained by factors such as temperature limits and costs of recovery equipment. There are a number of cases where heat recovery equipment is installed, but the quantity of heat recovered does not match the full recovery potential. Key barriers include heat exchanger material limits and costs for extending recovery to lower temperature and higher temperature regimes.
Most unrecovered waste heat is at low temperatures.
The waste heat streams analyzed in this study showed that roughly 60% of unrecovered waste heat is low quality (i.e., at temperatures below 232°C). While lowtemperature waste heat has less thermal and economic value than hightemperature heat, it is ubiquitous and available in large quantities. Comparison of total work potential from different waste heat sources showed that the magnitude of lowtemperature waste heat is sufficiently large that it should not be neglected in pursuing opportunities for waste heat recovery. New technologies are developing that may provide significant opportunities for lowtemperature heat recovery.
There are certain industrial subsectors where heat recovery is less common, due to the factors such as heat source’s chemical composition. Hightemperature, highquality heat is wasted in some subsectors due to corrosive/fouling chemicals contained in the waste heat stream.
Losses from nontraditional waste heat sources are difficult to recover, but significant. This study focused on exhaust gas waste heat losses; however, it was found that alternate sources of waste heat are also significant. These include heat lost from hot product streams (e.g., hot cast steel) and hot equipment surfaces (e.g., aluminum sidewalls).
Industrial waste heat can be used in opened, closed and opened-closed circuit schemes.
In closed-circuit scheme waste heat is used for main process equipment (preheating combustion components, load preheating).
Opened-circuit schemes are characterized by using of waste heat for external purposes not related to the main process equipment, which is the source of waste heat (steam generation, space heating, hot water supply for other technological process or consumers, etc.).
The third way - combined facilities in which waste heat is used for both internal and external applications (close-open circuit schemes).
