- •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
5.1.3.Supercapacitor energy storage systems
The supercapacitor ESS is typically connected to the DC link of the most popular consumer AC drive power stage (Fig. 2). As an example of very perspective supercapacitor application the supercapacitor ESS for traction purposes will be reviewed. The power stage consists of two main parts – a traction consumer AC drive connected through the overhead network to a traction substation and a supercapacitor ESS. The single direction substation equipment without regenerative braking and any type of energy storage is common for urban transport and includes an uncontrollable diode rectifier. The same ESS connection scheme is used for industrial consumer appliances, e.g. for elevators, lifting devices and other drives with regenerative braking [13]. Due to the short charge-discharge cycle lifetime accumulator battery must be used as primary energy source in the case of unavailable network voltage and never used in parallel to networ for peak shaving operation, therefore the battery is connected instead of network substation rectifier. Similarly the supercapacitor ESS is connected to DC link of small and unpredictable renewable and alternative energy sources such as wind, solar, internal combustion engine and fuell cell. All these sources are connected instead of substation rectifier.
The traction vehicle power scheme layout with simplified generalized substitution scheme of typical traction and industrial consumer power circuit is shown in Fig. 3. Independently from drive type – DC or AC, motor converter is replaced by current source I1. The positive direction of the source current corresponds to the braking mode; in the traction mode the current direction is opposite.
Fig. 2. The power stage of vehicle AC traction drive with supercapacitor ESS
Fig. 3. A tramcar traction drive with hybrid energy storage system (a) and its simplified power circuit substitution scheme (b)
In the braking mode the current flows to the DC power line, for example overhead line in the case of traction application. If it is impossible for some reason or the overhead current is not large enough, the braking IGBT VTbr, which is controlled by a pulse width modulator with 1000 Hz frequency, begins to operate. The control system works as voltage VCf stabilizer with a 780 V setting for 600 V catenary voltage. The energy is dissipated in a brake rheostat Rbr. The pulse currents are closed through capacitor Cf, whereas the overhead line current is smoothed by choke Lf. Between capacitor Cf and choke Lf a radio-frequency filter Lrf, Crf is also connected.
While connecting such a supercapacitor to the existing vehicle power scheme it is necessary to take into account that a current controller must provide:
two-way voltage boost/buck energy interchange between the traction power circuit and the supercapacitor;
smoothed charge/discharge current of the supercapacitor;
controllable initial charge of the supercapacitor;
protection of the supercapacitor against overcurrents caused by overhead short circuits.
If the supercapacitor current controller is connected to point A, the above requirements could be satisfied by the full controller scheme only [7,12]. Fig. 4 shows its connection to the consumer power circuit.
Fig. 4. Connection of the full scheme of supercapacitor’s C current controller to point A of consumer power circuit
The connection in Fig. 4 satisfies all the imposed requirements, being however too complicated. Moreover, a couple of weakly damped oscillation circuits are met in this scheme, e.g. Cf, Lf, L1, C1 when IGBT VT1 is switched on, which causes parasitic oscillations in a power circuit and complicates considerably the development of the control system.
The scheme could be significantly simplified by the following measures:
Connection of the supercapacitor’s current controller to point B. Then the controller-induced pulse currents could be filtered in the overhead line by elements Lrf, Crf, Lf already installed in the tramcar.
Choice of the supercapacitor’s operating voltage, which should be higher than the highest overhead voltage or lower than the lowest overhead voltage. Then a boost converter will be needed in one direction and a buck converter in the other, which could be achieved with two switching elements.
Since the overhead voltage may be varied between 450 V and 780 V, it would be economically justified to select the supercapacitor voltage up to 450 V. Then the scheme can be simplified as shown in Fig. 3. For the basic operation of the scheme it is enough to use the IGBT switches VT1 and VT3. Switch VT1 and diode D3 work as a voltage buck converter in the charging mode of supercapacitor C, whereas VT3 and D1 (at VT2 switched on) - as a voltage boost converter in the discharging mode. The IGBT VT2 is needed for protection of supercapacitor C in the cases when a short circuit or an undervoltage occurs in the overhead or traction converter scheme. When supercapacitor C is discharging the VT2 switch is continuously on, but it is being switched off in the case of supercapacitor overcurrent. For dissipating the energy stored by choke L1 it is necessary to install additional snubber circuits. Capacitor Cf is used as the basic element for the buck/boost converter. Capacitor C1 only compensates the connecting cable’s inductances and must be placed as close as possible to elements VT1, VT2, VT3 and C; its capacity is considerably lower than that of Cf.
If the supercapacitor’s voltage is selected higher than 780 V, then, in the same manner, three IGBT switches are needed to provide that the initial charging of capacitor C is controlled, but in this case one choke and one capacitor are additionally required. Therefore the scheme shown in Fig. 3 could be considered the optimal in view of the required number of elements.
At charging the capacitor from the initial voltage VCmin to voltage VCmax, the energy stored by the capacitor is
. (5)
It is obvious from Eq. (5) that the energy capability of the capacitor strongly depends on the minimum voltage VCmin to which it is discharged. The lower VCmin is the more energy could be stored in the capacitor. The manufacturers of the capacitors recommend that VCmin ≥ 0.5VCmax, which allows up to 75% of the energy stored by capacitor to be utilized. However, the lower VCmin is, the higher the necessary capacitor current at the same braking power Pbr. At the beginning of the process the braking power is maximal but the voltage of the capacitor is minimal, therefore
. (6)
As the semiconductor elements must be chosen corresponding to current ICmax which must not exceed the level allowable for the capacitor, both the aspects should be taken into account for a proper choice of the capacity C and the voltage range. If the total braking energy Wbr is stored, from expressions (5) and (6) at WC = Wbr we can find that
(7)
and
. (8)
In general terms, the braking mode of the vehicle could be characterized by the initial braking power Pbrmax = 300 kW which linearly decreases to zero during braking [7]. The calculated braking energy is Wbr = 900 kJ. Substituting these values into expressions (8) we obtain VCmin and ICmax curves in dependence on capacity C at VCmax = 450 V (Fig. 5).
The supercapacitor contains a great number of series-connected single capacitors. Currently, the capacitors with the allowable voltage of 2.7 V manufactured by the Maxwell
1
2
2
Capacity C, F
Fig. 5. Voltage VCmin (curve 1) and current ICmax (curve 2) vs. capacity C at Pbrmax = 300 kW, Wbr = 900 kJ and VCmax = 450 V
Technologies, Inc. have the largest available capacity of 3000 F (of these capacitors 16 V, 48 V and 125 V modules are made). They also have the optimal ratio between energy density and price. Taking into account a possible voltage disbalance between series-connected capacitors it is desirable that the maximum voltage on a capacitor is not exceeding 2.5 V. This means that at least 180 series-connected single capacitors are needed to achieve the 450V level, with the total capacity of the module equal to 16.66 F. It is clear that the capacity choice is not free; this could be doubled or multiplied by parallel connection of two and more such modules. From Fig. 5, at C = 17 F we have VCmin = 310.8 V, which is permissible, but ICmax = 965 A, which is too high from the viewpoint of the choice of capacitors and IGBT switches. As the optimal value C=33F could be considered, which corresponds to the parallel connection of two 180-element capacitor modules. At C = 33 F voltage VCmin = 384.6 V and current ICmax = 780 A. This is the total current at the parallel connection of supercapacitor modules, while for each supercapacitor branch it is twice smaller, i.e., 390 A, which is allowable.
