Volume 2013, Issue 1 120849
Research Article
Open Access

Combined Heat and Power Dynamic Economic Dispatch with Emission Limitations Using Hybrid DE-SQP Method

A. M. Elaiw

Corresponding Author

A. M. Elaiw

Department of Mathematics, Faculty of Science, King Abdulaziz University, P.O. Box 80203, Jeddah 21589, Saudi Arabia kau.edu.sa

Department of Mathematics, Faculty of Science, Al-Azhar University, Assiut 71511, Egypt azhar.edu.eg

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X. Xia

X. Xia

Centre of New Energy Systems, Department of Electrical, Electronic and Computer Engineering, University of Pretoria, Pretoria 0002, South Africa up.ac.za

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A. M. Shehata

A. M. Shehata

Department of Mathematics, Faculty of Science, Al-Azhar University, Assiut 71511, Egypt azhar.edu.eg

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First published: 13 November 2013
Citations: 15
Academic Editor: Jinde Cao

Abstract

Combined heat and power dynamic economic emission dispatch (CHPDEED) problem is a complicated nonlinear constrained multiobjective optimization problem with nonconvex characteristics. CHPDEED determines the optimal heat and power schedule of committed generating units by minimizing both fuel cost and emission simultaneously under ramp rate constraints and other constraints. This paper proposes hybrid differential evolution (DE) and sequential quadratic programming (SQP) to solve the CHPDEED problem with nonsmooth and nonconvex cost function due to valve point effects. DE is used as a global optimizer, and SQP is used as a fine tuning to determine the optimal solution at the final. The proposed hybrid DE-SQP method has been tested and compared to demonstrate its effectiveness.

1. Introduction

Recently, combined heat and power (CHP) units, known as cogeneration or distributed generation, have played an increasingly important role in the utility industry. CHP units can provide not only electrical power but also heat to the customers. While the efficiency of the normal power generation is between 50% and 60%, the power and heat cogeneration increases the efficiency to around 90% [1]. Besides thier high efficiency, CHP units reduce the emission of gaseous pollutants (SO2, NOx, CO, and) by about 13–18% [2].

In order to utilize the integrated CHP system more CO2 economically, combined heat and power economic dispatch (CHPED) problem is applied. The objective of the CHPED problem is to determine both power generation and heat production from units by minimizing the fuel cost such that both heat and power demands are met, while the combined heat and power units are operated in a bounded heat versus power plane. For most CHP units the heat production capacities depend on the power generation. This mutual dependency of the CHP units introduces a complication to the problem [3]. In addition, considering valve point effects in the CHPED problem makes the problem nonsmooth with multiple local optimal point which makes finding the global optimal challenging.

In the literature, several optimization techniques have been used to solve the CHPED problem with complex objective functions or constraints such as Lagrangian relaxation (LR) [4, 5], semidefinite programming (SDP) [6], augmented Lagrange combined with Hopfield neural network [7], harmony search (HS) algorithm [1, 8], genetic algorithm (GA) [9], ant colony search algorithm (ACSA) [10], mesh adaptive direct search (MADS) algorithm [11], self adaptive real-coded genetic algorithm (SARGA) [3], particle swarm optimization (PSO) [2, 12], artificial immune system (AIS) [13], bee colony optimization (BCO) [14], differential evolution [15], and evolutionary programming (EP) [16]. In [2, 1315], the valve point effects and the transmission line losses are incorporated into the CHPED problem.

In the CHPED formulation the ramp rate limits of the units are neglected. Plant operators, to avoid life-shortening of the turbines and boilers, try to keep thermal stress on the equipments within the safe limits. This mechanical constraint is usually transformed into a limit on the rate of change of the electrical output of generators. Such ramp rate constraints link the generator operation in two consecutive time intervals. Combined heat and power dynamic economic dispatch (CHPDED) problem is an extension of CHPED problem where the ramp rate constraint is considered. The primary objective of the CHPDED problem is to determine the heat and power schedule of the committed units so as to meet the predicted heat and electricity load demands over a time horizon at minimum operating cost under ramp rate constraints and other constraints [17]. Since the ramp rate constraints couple the time intervals, the CHPDED problem is a difficult optimization problem. If the ramp rate constraints are not included in the optimization problem, the CHPDED problem is reduced to a set of uncoupled CHPED problems that can easily be solved. In the literature an overwhelming number of reported works deal with CHPED problem; however, the CHPDED problem has only been considered in [17].

The traditional dynamic economic dispatch (DED) problem which considers only thermal units that provide only electric power has been studied by several authors (see the review paper [18]). The emission has been taken into the traditional (DED) formulation in three main approaches. The first approach is to minimize the fuel cost and treat the emission as a constraint with a permissible limit (see, e.g., [1921]). This formulation, however, has a severe difficulty in getting the trade-off relations between cost and emission [22]. The second approach handles both fuel cost and emission simultaneously as competing objectives [2325]. The third approach treats the emission as another objective in addition to fuel cost objective. However, the multiobjective optimization problem is converted to a single-objective optimization problem by linear combination of both objectives [19, 2630]. In the second and third approaches, the dynamic dispatch problem is referred to as dynamic economic emission dispatch (DEED) which is a multiobjective optimization problem, which minimizes both fuel cost and emission simultaneously under ramp rate constraint and other constraints [19, 24]. In this paper, we incoroporate the CHP units into the DEED problem. Combined heat and power dynamic economic emission dispatch (CHPDEED) is formulated with the objective to determine the unit power and heat production so that the system’s production cost and emission are simultaneously minimized, while the power and heat demands and other constraints are met [17]. The emission has been taken into consideration in the CHPED and CHPDED in [17, 31], respectively. In [17], both fuel cost and emission are simultaneously handled as competing objectives and the multiobjective problem is solved using an enhanced firefly algorithm (FA). In the present paper, the multiobjective optimization problem is converted into a single-objective optimization using the weighting method. This approach yields meaningful result to the decision maker when solved many times for different values of the weighting factor. In [17], the simulation results for test system are shown, but the data of the heat demand is not explicitly tabulated; instead it is expressed graphically (see Figure 12 in [17]). In this case a comparison of our proposed method and FA cannot be performed. In our paper, all the data and the solutions of the test system are available for comparison.

Differential evolution algorithm (DE), which was proposed by Storn and Price [32] is a population based stochastic parallel search technique. DE uses a rather greedy and less stochastic approach to problem solving compared to other evolutionary algorithms. DE has the ability to handle optimization problems with nonsmooth/nonconvex objective functions [32]. Moreover, it has a simple structure and a good convergence property, and it requires a few robust control parameters [32]. DE has been applied to the CHPED and CHPDED problems with non-smooth and non-convex cost functions in [15, 33], respectively.

The DE shares many similarities with evolutionary computation techniques such as genetic algorithms (GA) techniques. The system is initialized with a population of random solutions and searches for optima by updating generations. DE has evolution operators such as crossover and mutation. Although DE seem to be good methods to solve the CHPDEED problem with non-smooth and non-convex cost functions, solutions obtained are just near global optimum with long computation time. Therefore, hybrid methods such as DE-SQP can be effective in solving the CHPDEED problems with valve point effects.

The main contributions of the paper are as follows. (1) A multi-objective optimization problem is formulated using CHPDEED approach. The multi-objective optimization problem is converted into a single-objective optimization using the weighting method. (2) Hybrid DE-SQP method is proposed and validated for solving the CHPDEED problem with nonsmooth and nonconvex objective function. DE is used as a base level search for global exploration and SQP is used as a local search to fine-tune the solution obtained from DE. (3) The effectiveness of the proposed method is shown for test systems.

2. Problem Formulation

In this section we formulate the CHPDEED problem. The system under consideration has three types of generating units, conventional thermal units (TU), CHP units, and heat-only units (H). The power is generated by conventional thermal units and CHP units, while the heat is generated by CHP units and heat-only units. The objective of the CHPDEED problem is to simultaneously minimize the system’s production cost and emission so as to meet the predicted heat and power load demands over a time horizon under ramp rate and other constraints. The following objectives and constraints are taken into account in the formulation of the CHPDEED problem.

2.1. Objective Functions

In this section, we introduce the cost and emission functions of three types of generating units, conventional thermal units which produce power only, CHP units which produce both heat and power, and heat-only units which produce heat only.

2.1.1. Conventional Thermal Units

Cost. The cost function curve of a conventional thermal unit can be approximated by a quadratic function [35]. Power plants commonly have multiple valves which are used to control the power output of the unit. When steam admission valves in conventional thermal units are first open, a sudden increase in losses is registered which results in ripples in the cost function [18, 36]. This phenomenon is called as valve-point effects. The generator with valve-point effects has very different input-output curve compared with smooth cost function. Taking the valve-point effects into consideration, the fuel cost is expressed as the sum of a quadratic and sinusoidal functions [17, 24, 25, 37]. Therefore, the fuel cost function of the conventional thermal units is given by
()
where ai,  bi, and ci are positive constants, ei and fi are the coefficients of conventional thermal unit i reflecting valve-point effects, is the power generation of conventional thermal unit i during the tth time interval [t − 1, t), is the minimum capacity of conventional thermal unit i, and is the fuel cost of conventional thermal unit i to produce .
Emission. The amount of emission of gaseous pollutants from conventional thermal units can be expressed as a combination of quadratic function and exponential function of the unit’s active power output [21]. The emission function is given by
()
where is the amount of emission from unit i from producing power . Constants αi, βi, γi, ηi, and δi are the coefficients of the ith unit emission characteristics [24].

2.1.2. CHP Units

Cost. A CHP unit has a convex cost function in both power and heat. The form of the fuel cost function of CHP units can be given by [6, 17] the following:
()
where is the generation fuel cost of CHP unit i to produce power and heat . Constants , and are the fuel cost coefficients of CHP unit j.
Emission. The emission of gaseous pollutants from CHP units is proportional to their active power output [17, 31]:
()
where and are the emission coefficients of CHP unit j.

2.1.3. Heat-Only Units

Cost. The cost function of heat-only units can take the following form [6, 17]:
()
where , and are the fuel cost coefficients of heat-only unit k and they are constants.
Emission. The emission of gaseous pollutants from CHP units is proportional to their heat output [17, 31]:
()
where and are the emission coefficients of heat-only unit k.
Let N be the number of dispatch intervals and Np + Nc + Nh the number of committed units, where Np is the number of conventional thermal units, Nc is the number of the CHP units, and Nh is the number of the heat-only units. Then the total fuel cost and amount of emission over the dispatch period [0, N] are given, respectively, by
()
where , , , , , and .

2.2. Constraints

There are three kinds of constraints considered in the CHPDEED problem, that is, the equilibrium constraints of power and heat production, the capacity limits of each unit, and the ramp rate limits.

(i) Power Production and Demand Balance
()
where PD,t and Losst are the system power demand and transmission line losses at time t (i.e., the tth time interval), respectively. The B-coefficient method is one of the most commonly used by power utility industry to calculate the network losses. In this method the network losses are expressed as a quadratic function of the unit’s power outputs that can be approximated in the following:
()
where
()
and Bij is the ijth element of the loss coefficient square matrix of size Np + Nc.
(ii) Heat Production and Demand Balance
()
where HD,t is the system heat demand at time t.
(iii) Capacity Limits of Conventional Thermal Units
()
where and are the minimum and maximum power capacity of conventional thermal unit i, respectively.
(iv) Capacity Limits of CHP Units
()
where and are the minimum and maximum power limit of CHP unit j, respectively, and they are functions of generated heat (. and are the heat generation limits of CHP unit j which are functions of generated power .
(v) Capacity Limits of Heat-Only Units
()
where and are the minimum and maximum heat capacity of heat-only unit k, respectively.
(vi) Upper/Down Ramp Rate Limits of Conventional Thermal Units
()
where and are the maximum ramp up/down rates for conventional thermal unit i [18].
(vii) Upper/Down Ramp Rate Limits of CHP Units
()
where and are the maximum ramp up/down rates for CHP unit j [17].

2.3. The Optimization Problem

Aggregating the objectives and constraints, the CHPDEED problem can be mathematically formulated as a nonlinear constrained multi-objective optimization problem which can be converted into a single-objective optimization using the weighting method as
()
where w ∈ [0,1] is a weighting factor. It will be noted that, when w = 1, problem (17) determines the optimal amount of the generated heat and power by minimizing the fuel cost regardless of emission and the problem will be referred to as combined heat and power dynamic economic dispatch (CHPDED) problem. If w = 0, then problem (17) determines the optimal amount of the generated power by minimizing the emission regardless of cost and the problem will be referred to as combined heat and power pure dynamic emission dispatch (CHPPDED).

3. Differential Evolution Method

DE is a simple yet powerful heuristic method for solving nonlinear, nonconvex, and nonsmooth optimization problems. DE algorithm is a population based algorithm using three operators; mutation, crossover, and selection to evolve from randomly generated initial population to final individual solution [32]. In the initialization a population of NP target vectors (parents) Xi = {x1i, x2i, …, xDi}, i = 1,2, …, NP, is randomly generated within user-defined bounds, where D  is the dimension of the optimization problem. Let be the individual i at the current generation G. A mutant vector is generated according to
()
with randomly chosen integer indexes r1, r2, r3 ∈ {1,2, …, NP}. Here is the mutation factor.
According to the target vector and the mutant vector , a new trial vector (offspring) is created with
()
where j = 1,2, …, D, i = 1,2, …, NP and rand(j) is the jth evaluation of a uniform random number between [0,1]. CR ∈ [0,1] is the crossover constant which has to be determined by the user. rnb(i) is a randomly chosen index from 1,2, …, D which ensures that gets at least one parameter from [32].
The selection process determines which of the vectors will be chosen for the next generation by implementing one-to-one competition between the offsprings and their corresponding parents. If f denotes the function to be minimized, then
()
where i = 1,2, …, NP. The value of f of each trial vector is compared with that of its parent target vector . The above iteration process of reproduction and selection will continue until a user-specified stopping criteria is met.
In this paper, we define the evaluation function for evaluating the fitness of each individual in the population in DE algorithm as follows:
()
where λ1 and λ2 are penalty values. Then the objective is to find fmin , the minimum evaluation value of all the individuals in all iterations. The penalty term reflects the violation of the equality constraints. Once the minimum of f is reached, the equality constraints are satisfied.

4. Sequential Quadratic Programming Method

SQP method can be considered as one of the best nonlinear programming methods for constrained optimization problems [38]. It outperforms every other nonlinear programming method in terms of efficiency, accuracy, and percentage of successful solutions over a large number of test problems. The method closely resembles Newton’s method for constrained optimization, just as is done for unconstrained optimization. At each iteration, an approximation is made of the Hessian of the Lagrangian function using Broyden-Fletcher-Goldfarb-Shanno (BFGS) quasi-Newton updating method. The result of the approximation is then used to generate a quadratic programming (QP) subproblem whose solution is used to form a search direction for a line search procedure. Since the objective function of the CHPDEED problem is non-convex and non-smooth, SQP ensures a local minimum for an initial solution. In this paper, DE is used as a global search and finally the best solution obtained from DE is given as initial condition for SQP method as a local search to fine-tune the solution. SQP simulations can be computed by the fmincon code of the MATLAB Optimization Toolbox.

5. Simulation Results

In this section we present two examples. The first example shows the efficiency of the proposed DE-SQP method for the DED problem. In the second example, the hybrid DE-SQP method is applied to the CHPDEED problem. In DE-SQP method, the control parameters are chosen as NP = 80, = 0.423 and CR = 0.885. The maximum number of iterations are selected as 20,000. The results represent the average of 30 runs of the proposed method. All computations are carried out by MATLAB program.

Example 1. This example consists of ten conventional thermal units to investigate the effectiveness of the proposed DE-SQP technique in solving the DED problem with valve point effects and transmission line losses. The technical data of the units as well as the demand for the 10-unit system are taken from [24]. The best solution of the DED problem is given in Table 1. Comparison between our proposed method (DE-SQP) and other methods is given in Table 2. It is observed that the proposed method reduces the total generation cost better than the other methods reported in the literature.

Table 1. Hourly generation (MW) schedule obtained from DED using DE-SQP for 10-unit system.
H Loss
  1 150.0000 135.0000 73.0000 70.3333 222.9974 155.1682 99.2918 120.0000 20.0000 10.0000 19.7912
2 150.0000 135.0000 101.9485 120.3333 222.6154 123.7029 129.2918 90.0000 48.7980 10.7150 22.4058
3 150.0000 135.0000 181.9485 170.3333 174.2621 130.9190 129.6896 120.0000 53.5785 40.7150 28.4468
4 150.0000 135.0000 183.1516 218.2899 223.5485 160.0000 129.3947 120.0000 80.0000 42.0564 35.4415
5 150.0000 135.0000 258.8414 249.7412 224.0147 160.0000 128.5373 120.0000 80.0000 13.2136 39.3484
6 150.0000 135.0000 315.1962 299.7412 243.0000 160.0000 129.8624 120.0000 80.0000 43.2136 48.0136
7 150.0000 176.9470 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 52.9470
8 178.2448 228.3049 340.0000 300.0000 243.0000 160.0000 129.9436 120.0000 80.0000 54.9118 58.4054
9 258.2448 308.3049 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 70.5500
10 289.0490 384.5331 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 79.5821
11 368.7363 397.1230 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 87.8595
12 374.8564 439.5807 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 92.4378
13 342.1737 386.2429 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 84.4166
14 262.1737 306.2429 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 53.1527 70.5693
15 182.1737 226.2429 340.0000 299.9639 243.0000 160.0000 130.0000 120.0000 80.0000 53.0342 58.4148
16 150.0000 146.2429 294.7660 249.9639 223.6700 160.0000 129.6353 120.0000 80.0000 43.3613 43.6398
17 150.0000 135.0000 258.1720 249.5279 223.9121 160.0000 128.8682 120.0000 80.0000 13.8650 39.3459
18 150.0000 151.6366 298.4749 299.5279 243.0000 160.0000 129.7933 120.0000 80.0000 43.6183 48.0511
19 227.2425 231.6366 299.3393 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 43.5728 58.7914
20 307.2425 311.6366 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 74.8793
21 265.4293 301.1183 340.0000 300.0000 243.0000 160.0000 130.0000 120.0000 80.0000 55.0000 70.5476
22 185.4293 221.1183 263.3759 250.0000 225.8767 160.0000 129.8685 120.0000 80.0000 41.1109 48.7801
23 150.0000 141.1183 183.3759 200.0000 223.4887 155.9437 128.7427 120.0000 50.0000 11.1109 31.7806
24 150.0000 135.0000 173.1056 180.5739 173.7249 118.1382 128.6826 120.0000 20.0000 10.0000 25.2260
Table 2. Comparison results of 10-thermal-unit system (cost × 106 $) for the DED problem.
Method EP [34] PSO [34] AIS [34] NSGA-II [24] IBFA [30] DE-SQP
cost ($) 2.5854 2.5722 2.5197 2.5168 2.4817 2.4659

Example 2. This example is 11-unit system (eight conventional thermal units, two CHP units, and one heat-only unit) for solving the CHPDED, CHPDEED, and CHPPDED problems using DE-SQP method. We shall solve the CHPDEED problem when w = 0.5, in addition to the CHPDED and CHPPDED problems which correspond to w = 1 and w = 0, respectively. The technical data of conventional thermal units, the matrix B, and the demand are taken from the 10-unit system presented in [24]. The 5th and 8th conventional units in [24] were replaced by two CHP units. The technical data of the two CHP units and the heat-only unit are taken from [17] and are given in Table 3. The heat demand for 24 hours is given in Table 4. The feasible operating regions of the two CHP units are given in Figures 1 and 2 (see [4, 14]).

Table 3. Data of the CHP units and heat-only unit system.
CHP units
j = 1 2650 14.5 0.0345 4.2 0.030 0.031 0.00015 0.0015 70
j = 2 1250 36 0.0435 0.6 0.027 0.011 0.00015 0.0015 50
  
Heat-only units
  
k = 1 2695.2 0 950 2.0109 0.038 0.0008 0.0010
Table 4. Heat load demand of the three-unit system for 24 hours.
Time (h) Demand (MWth)
1 390
2 400
3 410
4 420
5 440
6 450
7 450
8 455
9 460
10 460
11 470
12 480
13 470
14 460
15 450
16 450
17 420
18 435
19 445
20 450
21 445
22 435
23 400
24 400
Details are in the caption following the image
Heat-power feasible operating region for CHP unit 1.
Details are in the caption following the image
Heat-power feasible operating region for CHP unit 2.

The best solutions of the CHPDED, CHPDEED, and CHPPDED problems for DE-SQP algorithm are given in Tables 5, 6, and 7, respectively. The best cost, the amount of emission, and the transmission line losses are also given in Tables 57. It is seen that the cost is 2.5257 × 106 $ under CHPDED, but it increases to 2.6945 × 106 $ under CHPPDED. The emission obtained from CHPDED is 2.8287 × 105 lb, but it decreases to 2.4195 × 105 lb under CHPPDED. Under the CHPDEED problem, the cost is 2.5295 × 106 $ which is more than 2.5257 × 106 $ and less than 2.6945 × 106 $. Moreover, the emission is 2.7209 × 105 lb which is less than 2.8287 × 105 lb and more than 2.4195 × 105 lb.

Table 5. Hourly heat and power schedule obtained from CHPDED.
H Loss
1 150.0000 135.0000 74.5372 72.0784 124.5129 124.4302 20.0000 10.0000 236.8041 110.1974 21.5630 57.3450 135.5994 197.0556
2 150.0000 135.0000 98.1135 122.0784 122.2113 101.6179 48.2025 10.0000 236.8011 110.1974 24.2248 57.3614 135.5994 207.0392
3 150.0000 135.0000 178.1135 172.0784 120.7640 98.7468 78.2025 10.0000 235.3275 110.1974 30.4319 65.6496 135.5994 208.7509
4 150.0000 135.0000 188.0106 218.5077 160.0000 126.3142 80.0000 40.0000 235.2182 110.1974 37.2496 66.2643 135.5994 218.1363
5 150.0000 135.0000 268.0106 244.7145 128.0292 129.9179 80.0000 42.2707 233.2313 110.1974 41.3736 77.4390 135.5994 226.9616
6 150.0000 135.0000 334.4706 294.7145 160.0000 130.0000 80.0000 48.0931 235.6609 110.1974 50.1383 63.7746 135.5994 250.6260
7 150.0000 199.1593 340.0000 300.0000 160.0000 130.0000 80.0000 49.7990 238.0991 110.1974 55.2549 50.0614 135.5994 264.3392
8 189.7336 229.5497 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 242.2569 110.1974 60.7377 26.6766 135.5994 292.7240
9 265.3596 309.5497 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.1974 73.1068 0.0 135.5994 324.4006
10 303.6024 378.5162 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 246.9410 110.1974 82.2580 0.3317 135.5994 324.0689
11 368.8317 405.6648 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.1974 90.6945 0.0 135.5994 334.4006
12 367.7179 455.4472 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.1974 95.3624 0.0 135.5994 344.4006
13 352.0071 385.0034 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.1974 87.2079 0.0 135.5994 334.4006
14 272.0071 305.0034 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 244.9090 110.1974 73.1169 11.7604 135.5994 312.6402
15 193.6233 225.0034 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 242.9121 110.1974 60.7362 22.9917 135.5994 291.4089
16 150.0000 145.0034 296.8330 250.8703 160.0000 129.9573 80.0000 43.4626 233.2660 110.1974 45.5900 77.2439 135.5994 237.1567
17 150.0000 135.0000 260.0109 250.0000 160.0000 100.0000 80.0000 40.9143 235.3888 110.1974 41.5121 65.3046 135.5994 219.0959
18 150.0000 151.0646 319.4485 300.0000 160.0000 130.0000 80.0000 40.0577 237.4722 110.1974 50.2419 53.5869 135.5994 245.8137
19 229.4141 231.0646 313.3779 300.0000 160.0000 130.0000 80.0000 46.0360 237.0065 110.1974 61.0988 56.2062 135.5994 253.1943
20 309.4141 311.0646 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 116.9757 77.4552 0.0 90.7694 359.2306
21 272.4577 300.8037 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 111.8344 73.0959 0.0 124.7723 320.2277
22 192.4577 220.8037 260.6669 250.0000 160.0000 124.1397 80.0000 45.9763 234.6724 110.1974 50.9154 69.3338 135.5994 230.0668
23 150.0000 140.8037 180.6669 200.0000 127.6584 130.0000 50.0000 40.0000 236.4213 110.1974 33.7482 59.4980 135.5994 204.9026
24 150.0000 135.0000 100.6669 177.0362 123.2649 128.6636 42.3316 10.0000 234.6572 109.5624 27.1834 69.4196 135.0513 195.5291
  • Cost ($) = 2.5257 × 106. Emission (lb) = 2.8287 × 105. Total loss (MW) = 1.3443 × 103.
Table 6. Hourly heat and power schedule obtained from CHPDEED (w = 0.5).
t Loss
1 150.0000 135.0000 77.5875 65.0188 122.5177 129.0996 20.0000 10.0000 238.1722 110.1974 21.5935 49.6499 135.5994 204.7506
2 150.0000 135.0000 73.0000 115.0188 123.4971 126.6027 50.0000 13.3209 237.5744 110.1974 24.2115 53.0122 135.5994 211.3884
3 150.0000 135.0000 135.6390 143.2389 123.5028 130.0000 80.0000 43.3209 237.2689 110.1974 30.1680 54.7308 135.5994 219.6698
4 150.0000 135.0000 197.2495 193.2389 160.0000 130.0000 80.0000 46.3828 241.1942 110.1974 37.2630 32.6533 135.5994 251.7473
5 150.0000 135.0000 227.7945 243.2389 160.0000 130.0000 80.0000 46.9362 238.0276 110.1974 41.1946 50.4634 135.5994 253.9371
6 150.0000 148.0006 307.4622 293.2389 160.0000 130.0000 80.0000 55.0000 244.2131 110.1974 50.1122 15.6745 135.5994 298.7261
7 153.7715 216.0682 309.3974 300.0000 160.0000 130.0000 80.0000 55.0000 242.8740 110.1974 55.3090 23.2061 135.5994 291.1945
8 204.6091 224.9723 327.2185 300.0000 160.0000 130.0000 80.0000 55.0000 244.8130 110.1974 60.8102 12.3003 135.5994 307.1003
9 269.9376 304.9723 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.1974 73.1072 0.0 135.5994 324.4006
10 302.8816 379.1708 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 110.2066 82.2590 0.0 135.5384 324.4616
11 374.8455 398.1777 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 111.6628 90.6861 0.0 125.9076 344.0924
12 396.3649 416.9874 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 119.8750 95.2273 0.0 71.5941 408.4059
13 353.1036 382.7187 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 111.3732 87.1956 0.0 127.8228 342.1772
14 273.1036 302.7187 339.8378 300.0000 160.0000 130.0000 80.0000 55.0000 246.2562 110.1974 73.1138 4.1831 135.5994 320.2175
15 213.0095 222.7187 321.3321 300.0000 160.0000 130.0000 80.0000 55.0000 244.5974 110.1974 60.8552 13.5127 135.5994 300.8879
16 150.0000 142.7187 291.8181 250.0000 160.0000 130.0000 80.0000 46.1485 238.7061 110.1974 45.5889 46.6476 135.5994 267.7530
17 150.0000 135.0000 228.5656 240.9760 160.0000 130.0000 80.0000 45.7659 240.7225 110.1974 41.2275 35.3065 135.5994 249.0941
18 150.0000 207.5152 294.3486 250.0000 160.0000 130.0000 80.0000 55.0000 241.3976 110.1974 50.4588 31.5093 135.5994 267.8913
19 227.0251 235.5649 297.1019 300.0000 160.0000 130.0000 80.0000 55.0000 242.1587 110.1974 61.0481 27.2289 135.5994 282.1716
20 307.0251 315.5649 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 114.8749 77.4649 0.00 104.6636 345.3364
21 270.9950 301.2766 340.0000 300.0000 160.0000 130.0000 80.0000 55.0000 247.0000 112.8155 73.0871 0.00 118.2834 326.7166
22 190.9950 221.2766 260.0000 250.0000 157.3134 126.2505 80.0000 43.7439 239.1773 110.1974 50.9541 43.9973 135.5994 255.4033
23 150.0000 141.2766 180.0000 200.0000 154.2635 126.4607 51.1156 13.7439 238.8386 110.1974 33.8966 45.9019 135.5994 218.4987
24 150.0000 135.0000 100.0000 150.0000 118.3525 129.7054 78.8178 10.0000 235.4040 103.7586 27.0385 65.2191 130.0411 204.7398
  • Cost ($) = 2.5295 × 106. Emission (lb) = 2.7209 × 105. Total loss (MW) = 1.3439 × 103.
Table 7. Hourly heat and power schedule obtained from CHPPDED.
H Loss
1 150.0000 135.0000 73.0000 60.0000 84.3406 63.6438 64.0384 55 247 125.8 21.8228 0.0 31.4722 358.5278
2 150.0000 135.0000 75.2831 75.5559 107.4058 83.4606 80.0000 55 247 125.8 24.5054 0.0 32.4074 367.5926
3 150.0000 146.7217 108.1787 108.2058 154.2362 113.4606 80.0000 55 247 125.8 30.6030 0.0 18.2661 391.7339
4 187.3290 187.7229 135.7677 135.7127 160.0000 130.0000 80.0000 55 247 125.8 38.3323 0.0 32.4074 387.5926
5 209.9448 210.5929 152.0706 152.2866 160.0000 130.0000 80.0000 55 247 125.8 42.6949 0.0 32.4074 407.5926
6 252.6588 252.9491 188.3610 188.4287 160.0000 130.0000 80.0000 55 247 125.8 52.1977 0.0 25.5244 424.4756
7 272.2261 272.7171 208.2382 208.3486 160.0000 130.0000 80.0000 55 247 125.8 57.3300 0.0 26.7637 423.2363
8 290.5854 291.0583 229.5277 229.7367 160.0000 130.0000 80.0000 55 247 125.8 62.7082 0.0 32.4074 422.5926
9 323.8400 324.1415 276.1324 276.3023 160.0000 130.0000 80.0000 55 247 125.8 74.2162 0.0 25.5487 434.4513
10 346.7105 346.8973 313.1106 300.0000 160.0000 130.0000 80.0000 55 247 125.8 82.5184 0.0 32.4074 427.5926
11 379.2210 379.5185 340.0000 300.0000 160.0000 130.0000 80.0000 55 247 125.8 90.5395 0.0 29.4012 440.5988
12 403.5504 403.8291 340.0000 300.0000 160.0000 130.0000 80.0000 55 247 125.8 95.1796 0.0 31.9845 448.0155
13 361.7512 362.0812 337.4700 300.0000 160.0000 130.0000 80.0000 55 247 125.8 87.1023 0.0 32.0189 437.9811
14 323.7805 324.1252 276.7607 275.7492 160.0000 130.0000 80.0000 55 247 125.8 74.2157 0.0 25.5863 434.4137
15 291.7264 292.3796 231.0966 225.7492 160.0000 130.0000 80.0000 55 247 125.8 62.7519 0.0 31.8710 418.1290
16 229.7976 230.1379 167.7688 175.7492 160.0000 130.0000 80.0000 55 247 125.8 47.2535 0.0 31.3306 418.6694
17 210.0699 210.4074 152.1822 152.2351 160.0000 130.0000 80.0000 55 247 125.8 42.6946 0.0 32.3578 387.6422
18 252.7542 253.2318 188.2091 188.2081 160.0000 130.0000 80.0000 55 247 125.8 52.2031 0.0 29.7791 405.2209
19 288.2429 288.7410 226.6332 237.2113 160.0000 130.0000 80.0000 55 247 125.8 62.6285 0.0 27.4724 417.5276
20 335.1319 335.4397 294.6392 287.2113 160.0000 130.0000 80.0000 55 247 125.8 78.2222 0.0 31.3390 418.6610
21 332.6192 333.0535 282.3523 252.7233 160.0000 130.0000 80.0000 55 247 125.8 74.5483 0.0 32.3100 412.6900
22 252.6192 253.0535 202.3523 202.7233 149.4115 112.3565 80.0000 55 247 125.8 52.3163 0.0 27.3503 407.6497
23 172.6192 173.0535 122.3523 152.7233 135.8629 102.0552 80.0000 55 247 125.8 34.4664 0.0 25.1547 374.8453
24 150.0000 135.0000 90.3380 102.7233 128.7354 96.7805 80.0000 55 247 125.8 27.3771 0..0 31.5331 368.4669
  • Cost ($) = 2.6945 × 106. Emission (lb) = 2.4195 × 105. Total loss (MW) =  1.3684 × 103.

6. Conclusion

This paper presents a hybrid method combining differential evolution (DE) and sequential quadratic programming (SQP) for solving dynamic dispatch (CHPDED, CHPDEED, and CHPPDED) problems with valve-point effects including generator ramp rate limits. In this paper, DE is first applied to find the best solution. This best solution is given to SQP as an initial condition that fine tunes the optimal solution at the final. The feasibility and efficiency of the DE-SQP were illustrated by conducting case studies with system consisting of eight conventional thermal units, two CHP units, and one heat-only unit.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

    Acknowledgment

    This work was funded by the Deanship of Scientific Research (DSR), King Abdulaziz University, Jeddah, under Grant no. (130-107-D1434). The authors, therefore, acknowledge with thanks DSR technical and financial support.

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