- •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
1.5.2.Waste heat recovery systems
Commercial waste heat recovery systems may be divided into passive systems and active systems. The passive systems do not require significant mechanical or electrical consumption for their operation as the heat is transferred from a higher temperature source to a lower temperature stream. these systems are used in recycling energy back into the same industrial process or recovering energy for other on-site uses. The active systems require mechanical or electrical energy for their operation and they are used to increase the waste heat temperature or to generate electricity. Examples of active systems are: cogeneration systems, heat pumps, absorption systems.
Table XXVIII shows examples of the waste-heat recovery systems used for the various heat sources from the industrial process heating systems [3].
Waste Heat Recovery Systems [3].
Waste heat ecovery equipment |
Temperature range (°C) |
Waste heat sources |
Uses |
Radiation recuperator |
High |
Boiler flue gas |
Air preheating |
Convective recuperator |
Medium-high |
Soaking/annealing oven, melting furnace, afterburners, reheat furnace |
Air preheating |
Furnace |
High |
Glass/steel-melting |
Air preheating |
Metallic heat wheel |
Low-medium |
Curing/drying oven, boiler |
Air preheating, space heating |
Ceramic heat wheel |
Medium-high |
Large boiler flue gas |
Air preheating |
Passive regenerator |
Low-high |
Drying/curring/baking oven |
Air preheating, space heating |
Finned-tube regenerator |
Low-medium |
Boiler flue gas |
Make-up water preheating |
Heat pipes |
Low-medium |
Drying/curring/baking oven/waste steam/ air dryers/kilns/recerberator furnace |
Air preheating, make-up water preheating, space heating |
Gas/steam turbines |
Medium-high |
High-pressure stream reduced for low-pressure application, waste steam |
Generation of mechanical/electrical power |
The components of a waste heat recovery system are [4]:
for low to high temperature heat sources:
• heat exchangers;
• power generation equipment (ex. ORC turbine, steam turbine);
• auxiliary equipment (ex. pumps and fans);
• equipment for handling difficult waste heat sources.
for low temperature heat sources: heat pumps and absorption units.
Heat exchangers
Heat exchangers are the devices that provide efficient heat transfer between two or more fluids at different temperatures. The fluids may be separated by a solid wall to prevent mixing or they may be in direct contact [6].
Heat exchangers are available in many configurations and designs to meet the different needs, materials, temperatures and operating conditions.
The heat exchangers can be classified as follows:
by physical configuration:
shell-and-tube;
concentric tube;
plate-and-frame;
finned-tube;
spiral;
heat wheels;
heat pipes;
waste heat boilers.
by fluid streams between which heat is transferred:
gas-to-gas;
gas-to-liquid;
liquid-to-liquid.
by heat transfer mechanisms:
single phase;
two phase.
by flow arrangements:
parallel flow;
counter flow;
cross flow.
According to the operating principle, heat exchangers can be classified as:
recuperative exchangers;
regenerative exchangers;
run-around coils;
direct contact heat exchangers.
In recuperative heat exchangers hot and cold fluids circulate through the device simultaneously, and heat is transferred through the wall separating the fluids. In the regenerative exchangers, the same heat exchange surface is exposed alternately to both hot and cold fluid; the heat taken from the hot fluid is accumulated in the walls of the device and then transferred to the cold fluid. In a run-around coil, an independent circulating fluid is used to transport heat between the hot and cold streams. In direct contact heat exchangers, heat transfer process is accomplished through direct contact and mixing the hot and cold fluids
According to the working regime, heat exchangers are divided into two categories:
continuous flow heat exchangers (recuperative exchangers with or without heat agents mixture), where heat exchange occurs under steady state;
discontinuous flow heat exchangers, where heat transfer occurs intermittently (accumulator exchangers in which heat is stored when available and then delivered on demand);
periodic flow heat exchangers (regenerative exchangers, where cyclically, the heat carried away by the hot fluid accumulates in an inert material which does not react chemically with heat carriers and then is transferred to the cold fluid).
Another classification of heat exchangers is by typical use. These types can have various physical configurations such as:
recuperators which are typically used to recover heat from flue gases to heat air;
economizers which are typically used to recover heat from flue gases to heat boiler make-up water;
regenerators used to recover heat from exhaust to preheat air using thermal mass accumulator;
heat recovery steam generators (HRSG) used to recover heat for steam generation;
waste heat boilers used to recover heat for water heating or steam generation.
The characteristics of commercial heat exchangers used in waste heat recovery application are given in Tab. V.
