- •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
Opf Solution Using Gravitational Search Algorithm
In this section, a novel GSA-based approach is proposed to solve the OPF problem in distribution network. The following objective functions are considered: (Case 1) fuel cost minimization, (Case 2) power loss minimization and (Case 3) simultaneous minimization of the fuel cost and power loss. The proposed approach is tested on 11-node distribution network in which three DG units are integrated.
Gravitational search algorithm (GSA) is a newly stochastic search algorithm developed by Rashedi et al. [30]. This algorithm has a great potential to become a break-though optimization method [31]. GSA has been proved as high quality performance method in solving different optimization problems in literature [31], [32-36].
In GSA, the search agents are collection of mutually interacting masses based on the Newtonian gravity and the laws of motion. In this algorithm, agents are considered as objects and their performances are measured by their masses. All these objects attract each other by the gravity force, and this force causes a global movement of all objects towards the objects with heavier masses [30]. The position of the mass corresponds to the solution of the problem, and its gravitational and inertial masses are determined using a fitness function. In other words, each mass presents a solution. The algorithm is navigated by properly adjusting the gravitational and inertial masses. By lapse of time, the masses will be attracted by the heaviest mass representштп an optimum solution in the search space.
The GSA could be considered as an isolated system of masses. It is like a small artificial world of masses obeying the Newtonian laws of gravitation and motion. In a system with N agents (masses), the position of the ith agent is defined by:
for
(35)
where
n
is the search space dimension and
defines the position of the ith
agent in the dth
dimension.
After evaluating the current population fitness, the mass of each agent is calculated as follows [30,36]:
(36)
where:
(37)
where fiti(t) represents the fitness value of the agent i at time t. best(t) and worst(t) are the best and worst fitness of all agents, respectively and defined as follows (for a minimization problem):
(38)
(39)
According to Newton gravitation theory, the total force acting on the ith agent in the dth dimension at t time is specified as follows:
(40)
where randj is a random number in the interval [0, 1]. G(t) is gravitational constant at time t, Mi(t) and Mj(t) are masses of agents i and j, ɛ is a small constant and Rij(t) is the Euclidian distance between the two agents i and j given by the following equation:
(41)
Kbest is the set of first K agents with the best fitness value and biggest mass, which is a function of time, initialized to K0 at the beginning and decreased with time. In such a way, at the beginning, all agents apply the force, and as time passes, Kbest is decreased linearly and at the end there will be just one agent applying force to the others.
By the law of motion, the acceleration of the ith agent, at t time in the dth dimension is given by following equation:
(42)
Searching strategy on this notion can be defined to find the next velocity and next position of an agent. Next velocity of an agent is defined as a function of its current velocity added to its current acceleration. Hence, the next position and next velocity of an agent can be computed as follows:
(43)
(44)
where randi
is a uniform random variable in the
interval [0, 1]. This random number is utilized to give a randomized
characteristic to the search.
represents the position of
agent i
in dimension d,
is
the velocity and
is
the acceleration.
It must be pointed out that the gravitational constant G(t) is important in determining the performance of GSA. It is initialized at the beginning and will be reduced with time to control the search accuracy. In other words, the gravitational constant is a function of the initial value G0 and time t:
(45)
where α is a user specified constant, t the current iteration and T is the maximum iteration number. Parameters of maximum iteration T, population size N, initial gravitational constant G0 and constant α control the performance of GSA.
GSA implementation
Proposed GSA has been applied to solve the OPF problem for distribution network. The steps of the GSA are listed in Table 6.
Table 6. Steps of GSA.
Step 1 Step 2 |
Search space identification. Initialization: generate random population between minimum and maximum values of the control variables of the OPF problem. |
Step 3 |
Fitness evaluation of each agent for the OPF problem. |
Step 4 |
Update the G(t), best(t) and worst(t) and Mi(t) for i=1,2,...,N. |
Step 5 Step 6 Step 7 |
Calculation of the total force in different directions. Calculation of acceleration. Updating agents' velocity and position. |
Step 8 Step 9 |
Repeat Steps 3-7 until the stop criteria is reached. Stop. |
Program was developed in MATLAB 2008b computing environment and run on a 2.20 Ghz, PC with 3.0 GB RAM. The control parameters of GSA are shown in Table 7.
Table 7. GSA control parameters.
Population size N |
50 |
Maximum iteration number T |
100 |
Initial gravitational constant G0 |
100 |
Constant α |
20 |
Simulation results
Proposed GSA-based approach has been implemented to solve the optimal distribution power flow on real MV distribution network consisting of three feeders shown in Fig. 12 [37]. Line data and load data of the distribution network are listed in Table 8. It is supposed that three DG units are integrated in the distribution network. DG units at node 8 consist of several fuel cell stacks and DG units at nodes 9 and 10 consist of microturbine units with characteristics given in [4]. We assume that DG8 and DG10 operate in PQ mode with 0.9 power factors (produce reactive power) in all operating conditions, and DG9 is capable to control active power and voltage magnitude independently, and therefore operates in PV mode. DG units data, including cost coefficients, are given in Table 9. Limits for control variables are given in Table 10. Maximum and minimum values for voltages at load buses, including DG units which are modeled as PQ nodes, are 1.05 and 0.95 p.u., respectively.
Fig. 12. Single line diagram of MV distribution network.
Table 8. Line data and Load data.
Send. node |
Rec. node |
|
Line parameters |
|
Load at Rec. node |
|||
|
R (Ω) |
X (Ω) |
B (S) |
PL (kW) |
QL (kW) |
|||
0 |
1 |
|
0.20900 |
0.11700 |
0.000116 |
|
1262.4 |
256.2 |
0 |
2 |
|
0.20900 |
0.11700 |
0.000116 |
|
2416.6 |
490.5 |
0 |
3 |
|
0.20900 |
0.11700 |
0.000116 |
|
612.7 |
124.4 |
1 |
4 |
|
0.41800 |
0.23400 |
0.000232 |
|
435.1 |
88.3 |
2 |
5 |
|
0.52250 |
0.29250 |
0.000290 |
|
1148.0 |
233.0 |
3 |
6 |
|
0.41800 |
0.23400 |
0.000232 |
|
0 |
0 |
3 |
7 |
|
0.41800 |
0.23400 |
0.000232 |
|
575.4 |
116.8 |
4 |
8 |
|
0.83600 |
0.46800 |
0.000464 |
|
0 |
0 |
5 |
9 |
|
0.41800 |
0.23400 |
0.000232 |
|
1188.2 |
241.2 |
7 |
10 |
|
0.41800 |
0.23400 |
0.000232 |
|
0 |
0 |
Table 9. DG units data.
DG unit |
Type |
Mode |
PDGnom (kW) |
QDG (kVAr) |
|
Cost coefficients |
||
|
a ($/h) |
b ($/kWh) |
c ($/kW2h) |
|||||
DG8 |
MT |
PQ |
1000 |
cosφ=0.9 |
|
1 |
15·10-3 |
14·10-6 |
DG9 |
FC |
PV |
1800 |
-1350 ÷ 1350 |
|
3 |
11·10-3 |
7.9·10-6 |
DG10 |
FC |
PQ |
600 |
cosφ=0.9 |
|
3 |
1.2·10-3 |
35·10-6 |
Market |
HV network |
Slack node |
- |
- |
|
0 |
25·10-3 |
0 |
Table 10. Limits of control variables.
Control variables |
|
Min |
|
Max |
PDG8 (kW) |
|
0 |
|
1000 |
PDG9 (kW) |
|
0 |
|
1800 |
PDG10 (kW) |
|
0 |
|
600 |
V0 (p.u.) |
|
0.97 |
|
1.03 |
VDG9 (p.u.) |
|
0.98 |
|
1.03 |
QC1 (kVAr) |
|
0 |
|
500 |
QC2 (kVAr) |
|
0 |
|
500 |
QC3 (kVAr) |
|
0 |
|
500 |
Proposed GSA approach has been applied to solve OPF problem for three different objective functions. Table 11 shows optimal settings of control variables and objective function values for base case (control variables are set to nominal values) and optimization cases.
Table 11. Optimal settings of control variables.
Control variable and obj. fun. values |
Base case |
Case 1: Fuel cost minimization |
Case 2: Loss minimization |
Case 3: Fuel cost and loss minimization |
PDG8 (kW) |
1000 |
342.7 |
381.9 |
346.5 |
PDG9 (kW) |
1800 |
892.2 |
1800.0 |
1795.6 |
PDG10 (kW) |
600 |
317.9 |
476.3 |
372.2 |
V0 (p.u.) |
1 |
1.0039 |
1.0016 |
1.0015 |
VDG9 (p.u.) |
1 |
0.9991 |
1.0005 |
1.0009 |
QC1 (kVAr) |
500 |
287.8 |
72.1 |
209.9 |
QC2 (kVAr) |
500 |
250.0 |
2.8 |
10.0 |
QC3 (kVAr) |
500 |
369.0 |
42.5 |
35.7 |
Fuel cost ($/h) |
201.0167 |
186.2800 |
193.3815 |
192.7196 |
Ploss (kW) |
13.63 |
13.36 |
7.94 |
8.84 |
In order to verify and compare results, the same OPF problem is solved using a genetic algorithm, which is the most popular and most widely used heuristic optimization method. MATLAB realization of the GA is applied, where population size is set to 50, maximum number of generation is set to 100, and other parameters as the default parameters are used. In each case, 10 consecutive test runs were performed for solving the OPF problem using the proposed GSA approach as well as the reference GA approach.
Case 1: Fuel cost minimization. As could be seen in Table 11, the total fuel cost obtained by the proposed GSA is reduced to 186.28 $/h compared to the base case fuel cost of 201.02 $/h. It is clear that control variables settings corresponding to fuel cost based OPF results in reduction of 7.33 % in fuel cost, but insignificant reduction in power losses.
Comparison results are shown in Table 12. In Table 12 it could be seen that results obtained from the GSA are better than those obtained from the reference GA based approach. Fig. 13 shows comparative convergence profiles of GSA and GA for Case 1. It may be observed from this figure that the GSA tends to find the optimal solution faster than the GA.
Table 12. Comparison of simulation results for Case 1.
Methods |
Fuel cost ($/h) |
The average value of simulation time (s) |
||
Min |
Average |
Max |
||
GSA |
186.2800 |
186.2901 |
186.3489 |
13.5958 |
GA |
186.2823 |
186.3289 |
186.3601 |
17.8755 |
Fig. 13. Comparative convergence profiles of GSA and GA for Case 1.
Case 2: Power loss minimization. Minimization of power loss as objective in OPF results in reduction of 41.75% in losses, and 3.8% in fuel cost over the base case. Compared with Case 1, the power loss is reduced by 40.56% but the fuel cost increased by 3.8%.
Comparison results are shown in Table 13. Results presented in Table 13 clearly show that in GSA approach, Ploss is 7.94 kW, representing reduction of 12.46 % in comparison to GA algorithm. Also, comparative convergence profiles of GSA and GA for Case 2 are shown in Fig. 14. According to this figure, GSA tends to find the optimal solution faster than GA and hence has a higher convergence rate.
Fig. 14. Comparative convergence profiles of GSA and GA for Case 2.
Table 13. Comparison of simulation results for Case 2.
Methods |
Power loss (kW) |
The average value of simulation time (s) |
||
Min |
Average |
Max |
||
GSA |
7.940 |
8.915 |
9.620 |
11.3548 |
GA |
9.070 |
10.00 |
12.17 |
17.5018 |
Case 3: Fuel cost and power loss minimization. Simultaneous minimization of the fuel cost and power loss is a multi-objective OPF problem. The best compromise solution obtained by the proposed GSA is 192.7196 $/h and 8.84 kW, which shows 4.13% reduction in fuel cost and 35.14% reduction in power losses of base case values. Results obtained from the proposed GSA technique are compared with results obtained from the reference GA method. Table 14 shows comparison results. On the basis of these results it is clear that the GSA has better performance in comparison with the GA approach.
Table 14. Comparison of simulation results for Case 3.
Methods |
Fuel cost ($/h) |
|
Power loss (kW) |
The average value of simulation time (s) |
Average |
|
Average |
||
GSA |
192.8601 |
|
10.0370 |
11.6222 |
GA |
192.8844 |
|
10.1910 |
18.2849 |
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Chapter 2: Energy Saving Technologies in transmission, distribution of electrical energy
