- •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
Syngas Quality Parameters.
Parameter |
Boilers |
Internal combustion engines |
Gas turbines |
|
Combustion |
Co-combustion |
|||
Lower heating value (kJ/Nm3) |
> 4000 |
- |
> 4000 |
> 4000 |
Particulates (mg/Nm3) |
- |
- |
< 5-50 |
< 5-7 |
Tars (mg/Nm3) |
- |
- |
< 0.5 |
< 0.1-0.5 |
alkali metals (ppm) |
- |
- |
< 1-2 |
< 0.2-1 |
Pyrolysis is the most efficient process of biomass conversion producing combustible materials with high fuel-to-feed ratios (about 95.5%) [20]. The process can be guided in the direction of generating the desired product: char, oil or gas. Temperature is the most important factor that influences the proportion of products (Table XV). Production of combustible gas is maximized at high temperature, low heating rate and long gas residence time. Production of char is maximized at low temperature and low heating rate and production of oils is maximized at low temperature, high heating rate and short residence time.
Catalytic pyrolysis takes place at moderate temperature (775 K) in the absence of air and produce oils that can be used as fuel or as feedstock for chemical production. In order to maximize process production high heating rates and short residence times are required [20].
The pyrolysis process can be classified into: conventional pyrolysis, fast pyrolysis and flash pyrolysis. Conventional pyrolysis has slow heating rate and produces mainly char. fast pyrolysis takes place at high temperature with high heating rates and produces (60-75)% liquid, (15-25)% char and (10-20)% gas.
The pyrolysis oil is known as bio-oil, wood liquid, liquid smoke, wood distillates or pyroligneous tar.
Operating Parameters of Pyrolysis Processes.
Technology |
Residence time of solid (s) |
Heating rate (K/s) |
Particle size (mm) |
Temperature (K) |
Conventional |
450-550 |
0.1-1 |
5-50 |
550-950 |
Fast |
0.5-10 |
10-200 |
< 1 |
850-1250 |
Flash |
< 0.5 |
> 1000 |
< 0.2 |
1050-1300 |
Fast pyrolysis is used for production of chemicals and liquid fuels. The produce liquid fuels have can be storable and transportable. Fast pyrolysis could be more energy efficient and could have lower investments costs than other conversion process.
Flash pyrolysis is used for bio-oil production with an efficiency of up to 70%. The bio-oil can be used in internal combustion engines and gas turbines paying attention to poor thermal stability and corrosivity or as feedstock for refinery.
The use of bio oils in boilers, internal combustion engines and gas turbines may cause problems due to properties of bio-oils such as: poor volatility, high viscosity, acidity, poor thermal stability, high coking and deposition.
fig. 19 shows schematically a pyrolysis reactor.
energyfromwasteandwood.weebly.com
Figure 19. Pyrolysis system.
Ion V. Ion, associate professor, mechanical engineering: “Dunarea de Jos” University of Galati, Faculty of Mechanical Engineering, Thermal Systems and Environmental Engineering Department, 111, Domneasca St., off. G102, Galati, 800201, Romania, tel. +40 740566214, e-mail: ion.ion@ugal.ro
References
http://epp.eurostat.ec.europa.eu/statistics_explained/index.php/Renewable_energy_statistics
S. Van Loo, J. Koppejan, Handbook of Biomass Combustion and Co-firing, Twente University Press, 2002.
Th. Nussbaumer, Combustion and Co-combustion of Biomass: Fundamentals, Technologies, and Primary Measures for Emission Reduction, Energy & Fuels 2003, 17, 1510-1521.
EUROPEAN COMMISSION - EUR 21350 – BIOMASS - Green energy for Europe, Luxembourg: Office for Official Publications of the European Communities, 2005, http://publications.eu.int.
A. Demirbas, Combustion characteristics of different biomass fuels, Progress in Energy and Combustion Science 30, 2004, 219–230.
S.V. Vassilev, D. Baxter, L.K. Andersen, C.G. Vassileva, An overview of the chemical composition of biomass, Fuel 2010, 89, pp. 913–33.
R. Saidur, E.A. Abdelaziz, A. Demirbas, M.S. Hossain, S. Mekhilef, A review on biomass as a fuel for boilers, Renewable and Sustainable Energy Reviews 15, 2011, ppp. 2262–2289.
Biomass Energy Data Book – 2011, http://cta.ornl.gov/bedb
Phyllis, database for biomass and waste, http://www.ecn.nl/phyllis
K.Reisinger, C.Haslinger, M.Herger, H. Hofbauer, BIOBIB - A Database for Biofuels, University of Technology Vienna, Institute of Chemical Engineering, Fuel and Environmental Technology, http://cdmaster2.vt.tuwien.ac.at/biobib/
A. Demirbas, Potential applications of renewable energy sources, biomass combustion problems in boiler power systems and combustion related environmental issues, Progress in Energy and Combustion Science 31, 2005, pp. 171–192.
A. Friedl, E. Padouvas, H. Rotter, K. Varmuza, Prediction of heating value of biomass fuel and ash melting behaviour using elemental compositions of fuel and ash, CAC 2004, 9th International Conference on Chemometrics in Analytical Chemistry, 20-23 Sept. 2004, Lisbon, Portugal.
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B.V. Babu, Biomass pyrolysis: a state-of-the-art review, Biofuels, Bioproducts & Biorefining 2, 2008, pp. 393–414.
M. Balat, M. Balat, E. Kırtay, H. Balat, Main routes for the thermo-conversion of biomass into fuels and chemicals, Part 1: Pyrolysis systems, Energy Conversion and Management 50, 2009, pp. 3147–3157.
P. Basu, Combustion and Gasification in Fluidized Beds, CRC Press, 2006.
Ion V. Ion, associate professor, mechanical engineering: “Dunarea de Jos” University of Galati, Faculty of Mechanical Engineering, Thermal Systems and Environmental Engineering Department, 111, Domneasca St., off. G102, Galati, 800201, Romania, tel. +40 740566214, e-mail: ion.ion@ugal.ro
