The frequent start–stop scheme in the operation management of large pumping stations causes several problems, e.g., energy consumption and a potential safety hazard. We therefore established a mathematical model for the optimal operation of a large-scale pumping station considering the start-stop loss of machine. The objectives of the optimization model included electricity charges for a pumping station operation and the start-stop loss of a pumping station. The blade angle and start-stop scheme were taken into account as the double-decision variables, while the target water extraction (equality constraint), start-stop scheme, and power were the constraint conditions. A combination of an orthogonal experiment and a 0-1 integer programming algorithm was proposed to explore the optimal solution of the model. A real case of a single-unit pump station in China was applied to prove the effectiveness of the algorithm. The results showed that the optimization efficiency of the proposed algorithm was 4%–10% higher than that of the genetic algorithm. Additionally, the maximum optimization benefit was obtained when there were fewer than three start-stops during the operation process. The proposed algorithm provided a reference for similar complex nonlinear models.

  • The start-stop loss of a pumping station was introduced to develop the optimization model.

  • A combination of an orthogonal experiment and a 0-1 integer programming algorithm was proposed.

  • The proposed algorithm could deal with the model with equality constraints.

Graphical Abstract

Graphical Abstract
c

Start-stop consumption parameter of pumping station

C

Investment expenses for pumping station, including construction engineering expenses, mechanical and electrical equipment and installation expenses, metal structure equipment and installation expenses, temporary works expenses, independent expenses and reserve expenses (RMB, which is the legal tender of the People's Republic of China)

f

Total water-lifting expense during operation process (RMB)

F

Fitness function

Hi

Head for period i (m)

ki

Start-stop state of pumping station in period i, set the value to 1 when it is on and 0 when it is off

KT

The number of pumping station's start-stop during operation process

N

Divided time periods during operation process

N

Investment years of pumping station to date

Actual power of period i

Pi

Electricity price of period i (RMB/(kW·h))

Unit water-lifting expense (RMB/104 m3)

Flow of pumping station in period i (m3/s)

t

Reduced service life of pumping station caused by frequent start-stop (h)

T

Actual life of pumping station (h)

Time increment of period i (h)

We

Target water extraction of pumping station issued by the administrative department (m3)

Z

Barrier function

Discount rate (%)

Unit efficiency of pumping station (%)

Motor efficiency (%). When the load is greater than 60%, the motor efficiency can be considered basically unchanged and calculated as 94%

Transmission efficiency (%), which refers to the ratio between the power transmitted to the pump and the output power of the motor. The transmission efficiency of direct connection is 100%.

Blade angle of pumping station in period i (°)

Penalty factor

Recently with the construction of the South-to-North Water Transfer Project, a number of studies have investigated optimal schemes for the operation of pumping stations, including single unit stations (Negharchi et al. 2016; Gong et al. 2021) and pumping station groups (Hashemi et al. 2014; Gong & Cheng 2018). In the process of model construction, objective function included minimum energy consumption (Fernández García et al. 2014; Negharchi et al. 2016; Olszewski 2016), maximum benefit (Cheng et al. 2013), or highest efficiency (Lamaddalena & Khila. 2013). The frequent start-stops of a pumping station is common and unavoidable in such optimization schemes. All transient events induced changes in most operating parameters (e.g., discharge, head, rotational speed, and voltage) in pumping stations. The impacts of these changes on the pumping station should be assessed at an early stage of any hydroelectric project. Arce (2001) emphasized the effect of generator unit start-stops on efficiency. Gagnon et al. (2010) indicated that runners were subject to complex dynamic forces which might lead to eventual blade cracking and generate unexpected down time and high repair cost. Trivedi et al. (2013) proposed that transients created both steady and unsteady pressure loading on the runner blade, resulting in cyclic stresses and fatigue development in the runner. In addition, pump stoppage could instantaneously increase the pressure within a pipeline, which was an extreme condition and poses a severe threat to the safety of long-distance water transmission projects. Zhang et al. (2019) provided information for the design of protection devices to alleviate the water hammer effect caused by sudden pump shutdown, and effectively prevented extreme pressure waves caused by rapid valve closure. Stoenescu et al. (2019) proposed that maintenance costs could double the energy production variable cost if wrong operational decisions are applied. These papers have laid a solid foundation for this study, from different fields and views; however, they only considered the effect on the unit caused by frequent start-stops and neglected the optimization scheme from the management perspective.

In the process of model solving, it mainly included dynamic programming methods (Arce 2001; Cheng et al. 2010; Zheng et al. 2016), genetic algorithms (Abkenara et al. 2015), and ant colony optimizations (Ostfeld & Tubaltzev 2008; Mehzad et al. 2019). When the models were solved using modern intelligent algorithms, it was not always possible to satisfy the constraints in a short time. Most intelligent algorithms adopted random sampling, which also had difficulty in solving the equality constraint (Birhanu et al. 2014; SaberChenari et al. 2016). However, the water demand constraint was an equality constraint that was used to minimize waste.

The improved model construction and algorithm were proposed to solve these problems. The blade angle and start-stop scheme were available parameters that could be controlled by end users. Therefore, they were taken into account as the double–decision variables. Meanwhile, a combination of an orthogonal experiment and a 0-1 integer programming algorithm was proposed to explore the optimal solution of the model with equality constraint.

Modeling

Objective functions

The objective of the optimization model was developed in two parts: electricity charges for a pumping station operation and the start-stop consumption of a pumping station. The blade angle (θi) and start-stop scheme (ki= 0 for shut down, ki = 1 for start up) were taken into account as the double decision variables. The objective function is calculated by Equation (1):
(1)

Physical constraints

  • (1)
    Water demand constraint:
    (2)
  • (2)
    Start-stop scheme constraint:
    (3)
  • (3)
    Power constraint:
    (4)

Start-stop consumption parameter (c) of pumping station

The adverse effects on start-stops of a large plant have been studied by many scientists (Barán et al. 2005; Pulido et al. 2006). Yang et al. (2016) studied the wear and tear on hydro power turbines due to primary frequency control. Meniconi et al. (2014) derived an expression for the head envelope damping for turbulent flows in smooth and rough pipes, and indicated that the energy dissipation in unsteady-state pressurized pipe flow was quantified through a key parameter governing the dominance of unsteady friction in transient flows. Bi et al. (2010) proposed that it might induce a serious water hammer event in the pipes as the pump rapidly shut off. Thus, the transients in the pipes could be effectively alleviated by prolonging the valve closing time and reducing the valve opening. Nilsson & Sjelvgren (1997) pointed out that the factors affecting the start-stop consumption of a pumping station included wear of mechanical equipment and failure of control equipment during start-up. The largest cost was maintenance and personnel cost due to wear caused by equipment failure. The reviewed literature showed that frequent start-stops lead to load change, wear, and even fatigue damage, which affected the service life of the unit. However, the start-stop of the plant is inevitable and adjusting the scheme to minimize losses and prolong the service life of the plant is necessary. Therefore, quantification of the start-stop consumption is crucial.

To the best of the authors' knowledge, there is no unified standard for the start-stop consumption of pumping stations. Theoretically, the longer the service period, the greater the start-stop consumption of unit. Nilsson's theory, which was adopted in this paper, states that the service life should be reduced by 15 h for each start-stop. The expenses of pumping stations included construction engineering, mechanical and electrical equipment, and installation costs. This statistical method did not only avoid the detailed mechanism research of flow pattern change, but it also expressed the influence of flow pattern change on pump loss in the optimization model. The consumption of each start-stop in the pumping station is shown as:
(5)

Combination of orthogonal experiment and 0-1 integer programming algorithm

Equations (1)–(4) were complex nonlinear models with double-decision variables: blade angle (θi) and start-stop state (ki). If the blade angle (θi) of each stage was known, Equations (1)–(4) could be transformed into a 0-1 integer programming model with the start-stop state (ki) of each stage as the decision variable. Therefore, the optimization method of the orthogonal experiment was employed by the decision variable of blade angle, and the optimization method of the 0-1 integer programming was employed by the decision variable of start-stop state. As a consequence, this proposed algorithm was a combination of an orthogonal experiment and a 0-1 integer programming algorithm. The algorithm steps are shown in Figure 1.
Figure 1

Flow chart of the combination algorithm.

Figure 1

Flow chart of the combination algorithm.

Close modal
Jiangdu No. 4 Station of the South-to-North Water Transfer Project was rebuilt in 2004 and reopened in 2005. Jiangdu No. 4 Station installed seven sets of vertical axial flow pump. The rated speed is 150 rpm, single-unit flow is 31.2 m3/s, pump specific speed is 700, impeller diameter is 2,900 mm and rated blade angle θ = 0°. The blade of the pumping station is fully adjustable by hydraulic pressure, with adjustment range of (−4°, + 4°). A cross-sectional drawing of the pumping station is shown in Figure 2.
Figure 2

A cross-sectional drawing of the pumping station.

Figure 2

A cross-sectional drawing of the pumping station.

Close modal

Related parameters

Start-stop consumption of a single unit in Jiangdu No. 4 Station

According to Equation (5) the start-stop consumption of a single unit is shown in Equation (6). The investment expenses of Jiangdu No. 4 Station are shown in Table 1.

Time period

Each day was divided into nine periods and considered the operation management of the pumping station, the peak-valley electricity price, and the impact of model accuracy. The flow rate, unit efficiency, electricity price and average head of different blade angles in each period are shown in Table 2.

Optimization results

Experimental factor, experimental level, and orthogonal table selection

The target water extraction (We) was 2.00 × 106 m3 and the number of start-stop (KT) was limited to three. Taking periods as the experimental factor, the blade angle of each period was the experimental level. Each factor was separated into five experimental levels within the corresponding range (−4, −2, 0, +2, +4).

An orthogonal experiment method was adopted to construct the L64(59) orthogonal table, and the experimental combination scheme selected by the orthogonal table obtained the theoretical optimal blade angle corresponding to all combinations. The experimental combination of the L64 (59) orthogonal table are shown in Table 3.

The 0-1 integer programming method

In Equations (1)–(4), the blade angle (θi) was known, so the optimization model was transformed as follows:
(6)

Physical constraints:

  • (1)
    Water demand constraint:
    (7)
  • (2)
    Start-stop scheme constraint:
    (8)

Equations (7)–(9) were 0-1 integer programming models, which could be solved with a branch-and-bound method. The target water extraction (We) was 2.00 × 106 m3 and the number of start-stops (KT) was limited to three. Sixty-four combination schemes selected according to the L64 (59) orthogonal table were successively substituted into equations (7)–(9) to obtain 64 target values of corresponding schemes– expenses, as shown in Table 3.

Orthogonal analysis

Through orthogonal analysis, as shown in Table 3, the theoretical optimal solution was obtained (period 1–9, 0°, −4°, 2°, 0°, 4°, −4°, −2°, −2°, −2°). Based on the theoretical optimal solution of blade angle, the 0-1 integer programming model was used to obtain the optimal combination of start-stop state for each period (period 1–9, which is 0, 0, 1, 1, 1, 0, 0, 1, 1). The optimization operation processes are shown in Table 4.

Table 1

Calculation table of the loss

NumberNameUnitAmount
The total investment/C 104 RMB 6,903.38 
(1) Construction engineering expenses 104 RMB 253.1 
(2) Mechanical and electrical equipment and installation expenses 104 RMB 4,942.46 
(3) Metal structure equipment expenses and installation expenses 104 RMB 275.09 
(4) Temporary works expenses 104 RMB 83.46 
(5) Independent expenses 104 RMB 782.35 
(6) Reserve expenses 104 RMB 506.92 
(7) Other expenses 104 RMB 60 
Reduced use time for each start-up and shutdown/t 15 
Total running time/T year 30 
Discount rate/ 
Year of investment to date/n year 16 
NumberNameUnitAmount
The total investment/C 104 RMB 6,903.38 
(1) Construction engineering expenses 104 RMB 253.1 
(2) Mechanical and electrical equipment and installation expenses 104 RMB 4,942.46 
(3) Metal structure equipment expenses and installation expenses 104 RMB 275.09 
(4) Temporary works expenses 104 RMB 83.46 
(5) Independent expenses 104 RMB 782.35 
(6) Reserve expenses 104 RMB 506.92 
(7) Other expenses 104 RMB 60 
Reduced use time for each start-up and shutdown/t 15 
Total running time/T year 30 
Discount rate/ 
Year of investment to date/n year 16 
Table 2

Flow rate, installation efficiency, and electricity price

TimeAverage head (m)Blade Angle (°)Flow (m3/s)Efficiency (%)Electricity prices (RMB/(kW·h))TimeAverage head (m)Blade Angle (°)Flow (m3/s)Efficiency (%)Electricity prices (RMB/(kW·h))
7.90 −4 28.5 74.3 1.0724 7.24 −4 30.5 76.9 1.0724 
−2 31.1 75.5 −2 33.3 77.8 
33.6 77.0 36.1 78.7 
36.5 78.6 38.4 78.9 
39.0 78.6 40.9 78.5 
7.26 −4 30.4 76.8 1.0724 7.38 −4 30.0 76.4 1.0724 
−2 33.2 77.8 −2 32.8 77.5 
36.0 78.7 35.6 78.6 
38.4 78.9 38.0 79.0 
40.9 78.5 40.5 78.8 
7.43 −4 29.9 76.2 0.6414 7.72 −4 29.0 75.1 0.6414 
−2 32.7 77.3 −2 31.7 76.3 
35.4 78.5 34.4 77.8 
37.9 79.0 37.0 78.9 
40.4 78.9 39.5 78.9 
7.98 −4 28.2 74.0 0.2904 8.12 −4 27.8 73.4 0.6414 
−2 30.8 75.1 −2 30.2 74.3 
33.3 76.6 32.7 75.7 
36.2 78.5 35.7 78.0 
38.7 78.3 38.2 77.6 
8.08 −4 28.0 73.6 0.2904       
−2 30.4 74.5       
32.9 76.0       
35.8 78.2       
38.3 77.8       
TimeAverage head (m)Blade Angle (°)Flow (m3/s)Efficiency (%)Electricity prices (RMB/(kW·h))TimeAverage head (m)Blade Angle (°)Flow (m3/s)Efficiency (%)Electricity prices (RMB/(kW·h))
7.90 −4 28.5 74.3 1.0724 7.24 −4 30.5 76.9 1.0724 
−2 31.1 75.5 −2 33.3 77.8 
33.6 77.0 36.1 78.7 
36.5 78.6 38.4 78.9 
39.0 78.6 40.9 78.5 
7.26 −4 30.4 76.8 1.0724 7.38 −4 30.0 76.4 1.0724 
−2 33.2 77.8 −2 32.8 77.5 
36.0 78.7 35.6 78.6 
38.4 78.9 38.0 79.0 
40.9 78.5 40.5 78.8 
7.43 −4 29.9 76.2 0.6414 7.72 −4 29.0 75.1 0.6414 
−2 32.7 77.3 −2 31.7 76.3 
35.4 78.5 34.4 77.8 
37.9 79.0 37.0 78.9 
40.4 78.9 39.5 78.9 
7.98 −4 28.2 74.0 0.2904 8.12 −4 27.8 73.4 0.6414 
−2 30.8 75.1 −2 30.2 74.3 
33.3 76.6 32.7 75.7 
36.2 78.5 35.7 78.0 
38.7 78.3 38.2 77.6 
8.08 −4 28.0 73.6 0.2904       
−2 30.4 74.5       
32.9 76.0       
35.8 78.2       
38.3 77.8       

Note: The peak-valley electricity price in the table is extracted from the timeshare-of-sale electricity price of Jiangsu Power Grid in 2020–2022 published by Jiangsu Provincial Development and Reform Commission.

Table 3

The experimental combination of L64 (59)

Testing programBlade angle at each period (test level)
Expenses (104 RMB)
IIIIIIIVVVIVIIVIIIIX
−2 −4 −4 −2 4.33 
−2 −4 −2 −2 −4 3.56 
−4 −4 −2 −4 −2 3.81 
−4 −2 −4 −2 −2 3.32 
−4 −2 −2 −4 3.79 
−2 −4 −4 −2 4.05 
−2 −4 −4 −2 −2 4.04 
−4 3.52 
… … … … … … … … … … … 
52 −4 −4 −2 −2 −2 3.29 
… … … … … … … … … … … 
64 −4 −4 −4 −4 −4 −4 −4 −4 −4 4.06 
Index average k−4 4.02 3.89 3.93 4.2 4.36 3.98 3.89 3.98 4.18  
k−2 4.00 4.16 3.95 4.01 3.95 4.09 3.86 4.00 4.08  
k0 4.02 4.08 4.01 3.96 3.98 3.99 4.20 4.02 4.03  
k2 4.10 4.00 4.41 4.03 3.99 4.05 4.40 4.44 3.90  
k4 4.14 4.07 4.14 3.96 3.76 4.18 4.11 3.89 3.87  
Range 0.14 0.27 0.48 0.24 0.60 0.19 0.54 0.55 0.31  
Testing programBlade angle at each period (test level)
Expenses (104 RMB)
IIIIIIIVVVIVIIVIIIIX
−2 −4 −4 −2 4.33 
−2 −4 −2 −2 −4 3.56 
−4 −4 −2 −4 −2 3.81 
−4 −2 −4 −2 −2 3.32 
−4 −2 −2 −4 3.79 
−2 −4 −4 −2 4.05 
−2 −4 −4 −2 −2 4.04 
−4 3.52 
… … … … … … … … … … … 
52 −4 −4 −2 −2 −2 3.29 
… … … … … … … … … … … 
64 −4 −4 −4 −4 −4 −4 −4 −4 −4 4.06 
Index average k−4 4.02 3.89 3.93 4.2 4.36 3.98 3.89 3.98 4.18  
k−2 4.00 4.16 3.95 4.01 3.95 4.09 3.86 4.00 4.08  
k0 4.02 4.08 4.01 3.96 3.98 3.99 4.20 4.02 4.03  
k2 4.10 4.00 4.41 4.03 3.99 4.05 4.40 4.44 3.90  
k4 4.14 4.07 4.14 3.96 3.76 4.18 4.11 3.89 3.87  
Range 0.14 0.27 0.48 0.24 0.60 0.19 0.54 0.55 0.31  
Table 4

Optimization operation processes

TimeAverage head (m)Angle (°)FlowEfficiency (%)Amount of water (104 m3)Expense (104 RMB)Water-lifting expense (RMB/104 m3)
7.9 off     
7.26 off     
7.43 37.9 79.0 40.9 0.91 222.32 
7.98 33.3 76.6 48 0.42 87.59 
8.08 38.3 77.8 55.2 0.68 123.3 
7.24 off     
7.38 off     
7.72 −2 31.7 76.3 34.2 0.84 245.36 
8.12 −2 30.2 74.3 21.7 0.44 202.35 
Subtotal     200 3.29 164.49 
TimeAverage head (m)Angle (°)FlowEfficiency (%)Amount of water (104 m3)Expense (104 RMB)Water-lifting expense (RMB/104 m3)
7.9 off     
7.26 off     
7.43 37.9 79.0 40.9 0.91 222.32 
7.98 33.3 76.6 48 0.42 87.59 
8.08 38.3 77.8 55.2 0.68 123.3 
7.24 off     
7.38 off     
7.72 −2 31.7 76.3 34.2 0.84 245.36 
8.12 −2 30.2 74.3 21.7 0.44 202.35 
Subtotal     200 3.29 164.49 

Table 4 indicates that the cost of water lifting was 3.29 × 104 RMB, and water-lifting cost was 164.49 RMB/104 m3 when the target water extraction was 2.00 × 106 m3/d. The consumption of the machine's start-stop was considered, which was missing in previous papers (Cheng et al. 2010; Gong et al. 2021). Meanwhile, the start-stops were limited to fewer than three within the operation process. The consumption caused by the machine's start-stop was reduced artificially through management, including economic and security aspects, which was consistent with our expectations (Trivedi et al. 2013; Stoenescu et al. 2019).

Comparative analysis

Algorithm characteristics and comparison

With the development of computer technology, genetic algorithms, ant colony algorithms, and other modern optimization algorithms emerge one after another. The characteristics of these algorithms are to find the optimal solution by various random sampling and search approximation methods after the decision variables were discretized in the feasible domain. A genetic algorithm was selected for comparative analysis in this paper and a penalty function method was adopted to process it. The solution steps of the penalty function method are as follows: after selecting the target water extraction We, head Hi, electricity price Pi, flow rate Qi, and efficiency , the start-stop state ki and blade angle θi of each period were generated randomly within the feasible region. The problem was transformed into an unconstrained problem by using the penalty function method to deal with constraints.

If the constraint on target water extraction was not satisfied, the constructed barrier function was used, as shown in Equation (10):
(9)
If the constraint on times of start-stop was not satisfied, the constructed barrier function was used, as shown in Equation (11):
(10)
Fitness function:
(11)

The algorithm terminated after satisfying the condition. The running time and results of the two algorithms were compared, as shown in Table 5.

Table 5

Comparison of optimization results between the two algorithms

Combination algorithm of orthogonal test and 0-1 integer programming
Genetic algorithm
Running time (s)Running results
Running time (s)Running results
Amount of water (104 m3)Expense (104 RMB)Amount of water (104 m3)Expense (104 RMB)
200.0 3.29 200.3 3.64 
19 200.4 3.64 
46 200.4 3.64 
Combination algorithm of orthogonal test and 0-1 integer programming
Genetic algorithm
Running time (s)Running results
Running time (s)Running results
Amount of water (104 m3)Expense (104 RMB)Amount of water (104 m3)Expense (104 RMB)
200.0 3.29 200.3 3.64 
19 200.4 3.64 
46 200.4 3.64 

Analysis of optimization results

Table 5 showed that the running time of the proposed algorithm was within 10 seconds while the running time of the genetic algorithm was more than 40 seconds. In addition, the results calculated by the genetic algorithm failed to meet the constraints after several iterations. The optimization efficiency of the proposed algorithm was 4%–10% higher than that of genetic algorithm. The results obtained in a short time did not fully meet the constraints because there was equality constraint in the model and it was difficult to converge through the genetic algorithm. The comparison showed that the results calculated by the proposed algorithm was more rapid and effective than the genetic algorithm.

The influence of different constraints

Results under different constraints were compared in this paper, including the number of start-stops in the pumping station (KT) and target water extraction (We), as shown in Figure 3.
Figure 3

1.5 × 106 m3, 2.0 × 106 m3, and 2.5 × 106 m3 were the different target water extractions. The minimum expenses of water extraction under different number of pumping station’ s start-stop (1, 2, 3, 4, 5 time(s)/day) in Figure 3.

Figure 3

1.5 × 106 m3, 2.0 × 106 m3, and 2.5 × 106 m3 were the different target water extractions. The minimum expenses of water extraction under different number of pumping station’ s start-stop (1, 2, 3, 4, 5 time(s)/day) in Figure 3.

Close modal

The results showed that: (1) when KT reached three times or more, the unit water-lifting expense was related to the target water extraction. The larger the target water extraction, the larger the water extraction cost and the smaller the optimization benefit. Therefore, when the target water extraction is large, it is recommended to give instructions and arrange the water-lifting task in advance, which is beneficial to reduce energy consumption. (2) when the target water extraction was 2.5 × 104 m3, the optimization benefit was at a maximum when there were two start-stops; when the target water extractions were 2.0 × 104 m3 and 1.5 × 104 m3, the optimization benefit was at a maximum when there were three start-stops. Therefore, the maximum optimization benefit was obtained when there were fewer than three stop-starts during the operation process at the pumping station.

In view of the large pumping stations, a novel mathematical model was constructed to minimize the water-lifting expenses of pumping stations, and the consumption of start-stops was considered in the model. This complex nonlinear model with double-decision variables could be solved by a proposed combination of an orthogonal experiment and a 0-1 integer programming algorithm. The optimization results of the actual case (Jiangdu No. 4 Station) showed that the proposed algorithm improved the operation efficiency and optimization benefit compared with the modern intelligent algorithm, and solved the complex nonlinear model with equality constraint. This paper researched a single pumping station, but the optimal operation of multi-unit pumping stations will be studied in depth in future research.

This work was supported by the National Natural Science Foundation of China (NSFC) [grant number 52079119].

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

Abkenara
S. M. S.
,
Stanley
S. D.
&
Millera
C. J.
2015
Evaluation of genetic algorithms using discrete and continuous methods for pump optimization of water distribution systems
.
Sustainable Computing-Informatics & Systems
8
,
18
23
.
Barán
B.
,
VonLücken
C.
&
Sotelo
A.
2005
Multi-objective pump scheduling optimisation using evolutionary strategies
.
Advances in Engineering Software
36
(
1
),
39
47
.
Bi
H. L.
,
Liu
Z. Q.
,
Hong
Y. P.
,
Wang
F. J.
&
Bai
M. M.
2010
Analysis on hydraulic transients of a long-pipeline pumping station system
.
Journal of Engineering Thermophysics
31
,
149
152
.
Birhanu
K.
,
Alamirew
T.
,
Dinka
M. O.
,
Ayalew
S.
&
Aklog
D.
2014
Optimizing reservoir operation policy using chance constraint nonlinear programming for Koga Irrigation Dam, Ethiopia
.
Water Resources Management
28
(
14
),
4957
4970
.
Cheng
J. L.
,
Zhang
L. H.
,
Zhang
R. T.
&
Gong
Y.
2010
Study on optimal daily operation of single adjustable-blade pump unit in pumping station
.
Journal of Hydraulic Engineering
41
(
4
),
499
504
.
Cheng
X.
,
Li
G.
,
Cheng
C. T.
&
Guo
X. H.
2013
Modeling method of operation rules on cascade hydroelectric plants with hybrid pumped storage power station
.
Journal of Hydraulic Engineering
44
(
4
),
388
397
.
Fernández García
I.
,
Moreno
M.
&
Rodríguez Díaz
J. A.
2014
Optimum pumping station management for irrigation networks sectoring: case of Bembezar MI
.
Agricultural Water Management
144
,
150
158
.
Gagnon
M.
,
Tahan
S. A.
,
Bocher
P.
&
Thibault
D.
2010
Impact of startup scheme on Francis runner life expectancy
.
IOP Conference Series: Earth and Environmental Science
12
(
1
),
012107
.
Gong
Y.
,
Cheng
J. L.
,
Che
L.
&
Wang
L.
2021
Optimal operation of a single unit with an adjustable blade in an interbasin water transfer pumping station based on successive approximation discretization for blade angle
.
Shock and Vibration
2021
,
1
10
.
Lamaddalena
N.
&
Khila
S.
2013
Efficiency-driven pumping station regulation in on-demand irrigation systems
.
Irrigation Science
31
(
3
),
395
410
.
Mehzad
N.
,
Tabesh
M.
,
Ataeekia
B.
&
Hashemi
S.
2019
Optimum reliable operation of water distribution network considering pumping station and tank
.
Iranian Journal of Science and Technology – Transactions of Civil Engineering
43
,
413
427
.
Meniconi
S.
,
Duan
H. F.
,
Brunone
B.
,
Ghidaoui
M. S.
,
Lee
P. J.
&
Ferrante
M.
2014
Further developments in rapidly decelerating turbulent pipe flow modeling
.
Journal of Hydraulic Engineering
140
(
7
),
1
.
Negharchi
S. M.
,
Shafaghat
R.
,
Najafi
A.
&
Babazade
D.
2016
Evaluation of methods for reducing the total cost in rural water pumping stations in Iran: a case study
.
Journal of Water Supply: Research & Technology-AQUA
65
(
3
),
277
293
.
Ostfeld
A.
&
Tubaltzev
A.
2008
Ant colony optimization for least-cost design and operation of pumping water distribution systems
.
Journal of Water Resources Planning and Management
134
(
2
),
107
118
.
Pulido
C. I.
,
Gutiérrez
E. J. C.
&
Asensio-Fernández
R.
2006
Optimal design of pumping stations of inland intensive fishfarms
.
Aquacultural Engineering
35
(
3
),
283
291
.
SaberChenari
K.
,
Abghari
H.
&
Tabari
H.
2016
Application of PSO algorithm in short-term optimization of reservoir operation
.
Environmental Monitoring and Assessment
188
(
12
),
667
.
Stoenescu
B.
,
Costinas
S.
&
Deaconu
G. M.
2019
Assessment of hydropower plants energy production cost influenced by operational decisions and control strategy
. In
22nd International Conference on Control Systems and Computer Science (CSCS) 2019
. pp.
347
352
.
Trivedi
C.
,
Gandhi
B.
&
Michel
C. J.
2013
Effect of transients on Francis turbine runner life: a review(Review)
.
Journal of Hydraulic Research
51
(
2
),
121
132
.
Yang
W. J.
,
Norrlund
P.
,
Saarinen
L.
,
Yang
J. D.
,
Guo
W. C.
&
Zeng
W.
2016
Wear and tear on hydro power turbines – influence from primary frequency control
.
Renewable Energy
87
(
1
),
88
95
.
Zhang
Y. P.
,
Liu
M. Q.
,
Liu
Z. Y.
,
Wu
Y. W.
,
Mei
J.
,
Lin
P.
&
Xue
F.
2019
Pump-stoppage-induced water hammer in a long-distance pipe: a case from the Yellow River in China
.
Water Supply
19
(
No.1–2
),
216
221
.
Zheng
H. Z.
,
Zhang
Z.
,
Wu
H. M.
&
Lei
X. H.
2016
Study on the daily optimized dispatching and economic operation of cascade pumping stations in water conveyance system
.
Journal of Hydraulic Engineering
47
(
12
),
1558
1565
.
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