- •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
2.1.2.Constraints
Equality constraints (2) represent typical power balance and power flow equations. The power balance equation in distribution network with DG units with renewable and non-renewable energy sources can be expressed as follows:
,
(11)
where NR is the number of DG units with renewable energy sources.
The backward/forward sweep power flow equations are given in [12,13].
Constraints (3) define feasibility region of the problem control variables such as: DG unit active power output limits, root node voltage limits, PV bus voltage limits, transformer tap setting limits and shunt VAR compensation limits:
(12)
(13)
(14)
(15)
(16)
Inequality constraints (4) are functional operating constraints consisted of: load bus voltage magnitude limits, DG units reactive power capabilities and branch flow limits:
(17)
(18)
,
(19)
Inequality constraints of dependent variables contain load bus voltage magnitude, DG units reactive power output and branch loading is added to the objective function as quadratic penalty terms [6]. The new expanded objective function to be minimized becomes
, (20)
where λV, λQDG and λS are defined as penalty factors. xlim is limit value of the dependent variable x and given as [11]:
(21)
Dg units modeling for optimal power flow
3.1 Diesel generator
Usually, diesel fuel consumption data in (L/h) at 25%, 50%, 70% and 100% of the diesel generator power (kW) rating are given by the manufacturer. Based on these data, fuel consumption characteristic of the diesel generator can be estimated as a quadratic function of its active power output:
,
(22)
where Fueldg is diesel generator fuel consumption in (L/h), Pdg is diesel generator output power in (kW), a, b and c are coefficients of the fuel consumption characteristic.
Accordingly, the total ($/h) diesel generator fuel cost fdg can be calculated as:
,
(23)
where cdg is the diesel fuel price to supply the diesel generator in ($/L).
We assume that MDJW 410 T6, 369 kW diesel generator is used in this
paper. Diesel generator fuel consumption data is available in [14].
Based on these data and adopted fuel price
($/L), we obtain the fuel costs characteristic shown in Fig. 1.
Fig. 1. Diesel generator MDJW 410 T6 fuel cost curve for cdg=0.6 ($/L).
3.2 Fuel cell
Fuel cost of the fuel cell depends on the active power output and the fuel cell efficiency [5,15]:
(24)
where
is fuel cost for the fuel cell ($/h),
is fuel cell output (electrical) power (kW),
is fuel cell efficiency,
is fuel (natural gas) price to supply the fuel cell ($/kWh).
The fuel cell efficiency can be expressed as the ratio of the actual operating voltage V and 1.482 V [16]:
(25)
In this paper the Proton Exchange membrane (PEM) fuel cell has been considered. The actual operating voltage of the fuel cell is the function of power level, and can be calculated using the following formula [16]:
(26)
where:
-
theoretical or thermodynamic fuel cell potential (0.9 V);
- selected cell potential at nominal power (0.45 – 0.75 V);
- power level;
- nominal power of the fuel cell.
We assume the PEM fuel cell efficiency characteristic for
and
.
Fig. 2 shows the fuel cost curve estimated for
and
($/kWh).
Fig. 2. PEM fuel cost curve for V0=0.9 V, VPnom=0.6 V, Pnom=300 kW and cfc=0.05 ($/kWh).
3.3 Microturbine
Microturbine fuel costs fmt in ($/h) can be calculated as the following [5]:
(27)
where
is microturbine output electrical power (kW),
is microturbine electric efficiency,
is price of the fuel to supply the microturbine ($/kWh).
The efficiency of the microturbine increases with the increase of the output power [17]. The electric efficiency characteristic of the microturbine can be estimated as a quadratic function of its output power:
(28)
From a typical electrical efficiency curve of a 300 kW CGT301-302
microturbine [17] we obtain the microturbine fuel costs curve given
in Fig. 3. It is assumed that the price of the fuel to supply the
microturbine is
($/kWh)
Fig. 3. Microturbine 300 kW CGT301-302 fuel cost curve for cmt=0.05 ($/kWh).
3.4 Wind turbine
To calculate an output power of the wind turbine, two main factors have been known:
wind speed on certain location and
power curve of the wind turbine
According to [18, 19], the power curve of the wind turbine can be modeled by means of the function split into four different parts:
(29)
where
,
,
and
are nominal power, nominal wind speed, cut-in wind speed, and cut-out
wind speed of the wind turbine, respectively.
and
denoted output power of the wind turbine and the wind speed.
In this paper, we took into consideration Vestas V44/600 kW wind turbine model [20]. Parameters used to model the power curve obtained from the owner’s manual are as follows: Pnom=600 kW, vci=4 m/s, vnom=16 m/s and vco=20 m/s.
Fig. 4 shows wind speed data used to calculate the output power generated by the wind turbine generator in the OPF algorithm.
Fig. 4. Wind speed data.
3.5 Photovoltaic
Output power of the photovoltaic module is dependent on the solar
irradiance and ambient temperature of the site as well as on the
characteristics of the module itself [19]. The following equation can
be used to calculate the output power of the photovoltaic module
[21]:
(30)
where
is photovoltaic module maximum power at Standard Test Condition
(STC) (W),
is solar irradiance on the photovoltaic module surface (W/m2),
is photovoltaic module temperature coefficient for power (˚C-1),
is photovoltaic cell (module) temperature (˚C).
The photovoltaic module temperature can be calculated as a function of the solar irradiance and ambient temperature based on the module’s nominal operating cell temperature (NOCT). The NOCT model equation is given below [22, 23]:
(31)
where Ta is ambient temperature (˚C), TNOCT is nominal operating cell temperature (°C) of the module.
In this paper, we have considered Sunmodule, SW 250 mono modules.
Their performance characteristics are:
,
,
.
Figs. 5 and 6 show the ambient temperature and solar irradiance data [5] used to calculate the output power generated by the photovoltaic modules in the OPF algorithm.
Fig. 5. Ambient temperature data.
Fig. 6. Solar irradiance data.
3.6 Electric grid
Market energy costs
in ($/h) can be represented by means of square function
as:
(32)
where is electrical power in (kW) from the electric grid, and a, b, c are cost coefficients.
In this paper we adopted:
,
and
.
