Abstract
1. Introduction
Hydropower is a well-known renewable energy source generating clean, secure, and predictable electric power. It has zero carbon emission, low operational cost, and virtually zero greenhouse gas emission. With the technology of over one hundred years, hydropower is considered as the most established technology to provide energy in a small or large scale. By far, hydropower is the largest renewable energy produced accounting for 90% of the total renewable energy worldwide [1]. In 2010, hydropower has been utilized in 150 countries with installed capacity of 860 GW and Europe having the highest installed capacity followed by East Asia and Oceania [2].
While large hydropower plants feed the national grid, typical off-grid microhydro is the most popular solution for electrification among rural communities which supplies power in the range of 5–100 kW which usually use a run-of-the-river to divert some of the water from the river before dropping into a pressurized penstock. The water potential energy from the gravitational force over height difference is converted to rotational mechanical energy. A hydro turbine is used to transform energy from the flowing water to mechanical rotational energy and then a generator transforms the rotational mechanical energy to electrical energy regulated by electric control system. Microhydro configurations vary depending on the topography and hydrological site conditions [3].
The main components that comprise typical microhydro schemes are electromechanical equipments, civil structures, and energy distribution systems [4]. An optimum operational design, smart selection of equipment, and reduced professional consultation input can lower the overall cost [5–7]. It is important to pay attention to actions to reduce the whole microhydro cost because it is always the main concern for small communities especially in rural areas. In order to minimize the overall cost, microhydro system must be in the optimal operation and component selection. Furthermore, the microhydro must be reliable, robust, and manageable with minimum technical knowledge by local communities.
2. Pump as Turbine (PAT)
The electromechanical unit is one of the most expensive components in microhydro system. Generally, microhydro manufacturers offer high efficiency turbine performance; however, they are expensive and unaffordable particularly for rural communities. The use of PAT for microhydro offers low cost solution as a substitution for commercial microhydro turbine. Domestic and industrial end suction centrifugal pumps cover a wide range of flow and head are readily available and mass produced in many countries. The advantages of PAT compared to commercial turbines are simple constructions, know-how knowledge which is readily available, and low operating and initial cost thus making the technology more affordable, and these advantages are the reasons why there are a large number of PATs installed in rural areas [8, 9].
Pump as turbine (PAT) as an unconventional type of turbine does not have a flow regulating mechanism; therefore, each pump running in the turbine mode has single best efficient point (BEP), in which the flow rate and head are fixed for a particular point. The application of PAT is suitable for radial and mixed flow serving low specific speed turbine which is normally covered by a single jet Pelton wheel, multijet Pelton wheel, and crossflow turbine in the range of 13 to 100 m of head [10–12] as shown in Figure 1. Axial flow pumps which are not covered in this paper are prone to cavitation and are more expensive; thus they reduce the cost-benefit factors.

3. Research Review
3.1. Experimental Analysis of PAT
Pump manufacturers only supply pump mode performance curve and this makes it difficult to predict the turbine mode performance. Many attempts have been made to predict turbine mode performance by using analytical model but the percentage of deviation is relatively large compared to the actual performance [13–16]. To attain a definite characteristic pump in turbine mode, the pump is required to be tested over a range of heads and flows shown in Figure 2. A feed pump producing greater head and flow is used to supply inverse flow to the studied pump. The characteristic can be obtained at constant rotational speed controlled by electrical control equipment. The review on present PAT experimental works is presented in the following.

Laboratory schematic test rig for PAT.
Derakhshan and Nourbakhsh (2008) had tested four industrial centrifugal pumps with specific speed between 14 and 60 (m,m3/s) to derive a prediction model for the best efficient point based on pump hydraulic characteristic [16]. The test showed that centrifugal pump can operate in turbine mode without mechanical problem. Based on the experimental data, all centrifugal pumps give lower BEP running in turbine mode compared to pump mode. The efficiency in turbine mode was reported to be between 60 and 80%. The authors suggested that bigger pump impeller performs better in turbine mode.
Raman et al. (2013) had carried out experimental investigation of a centrifugal pump with specific speed of 15.36 working in turbine mode [17]. Calgon (HES 40–200) end suction centrifugal pump with head and flow of 22 m and 8.31 l/s was used for the test. 5 kW, 230 V synchronous AC generator was directly coupled to the pump. Control panel measured the rotational speed, generator voltage, current, and frequency of the system. The experiment shows that the best efficient point (BEP) was found at higher head and flow than in the pump mode. The efficiency was recorded at 39%, head and flow of 30 m and 13.52 l/s, respectively. The efficiency in pump mode was reported at 59% and the lower efficiency suggests higher hydraulic loss in the turbine mode.
Fernández et al. (2004) presented a performance study of a centrifugal pump in order to justify the feasibility of using pump in turbine mode by determining pump and turbine performance and radial thrust and prediction of pump-turbine characteristic curves [18]. The pump used for the study had a single axial suction and spiral volute casing with an impeller of 200 mm. The pump was tested using hydraulic setup standard ISO3555:1977. The best efficiency point in turbine mode was reported at 58% corresponding to flow coefficient and head coefficient of 0.015 and 0.011, respectively.
Nautiyal et al. (2011) studied the performance characteristics of a centrifugal pump running in pump and turbine mode. A Kirloskar (KC100-65-315) pump with specific speed of 18 was selected for the test [19]. The pump ratings for head, flow, and power are 32.8 meter, 14.8 l/s, and 8.18 kW, respectively. A synchronous generator of 12.5 kVA was coupled to the pump to measure power output running at 1500 rpm. The efficiency of pump operating in turbine mode was found to be 8.53% lower than the best efficiency in pump mode.
3.2. Numerical Analysis on PAT
The computer fluid dynamic (CFD) analysis provides great tools in the designing and performance analysis of fluid dynamics in turbo machinery. This tool allows researchers, engineers, and plant managers to test hydraulic performance in virtual condition. With the advancement in numerical algorithms and computing power, CFD plays a significantly large role in the discipline of fluid dynamics and turbo machinery. CFD allows various parameters investigation such as flow visualization, hydraulic optimization, off-design operation, and cavitation analysis which are impossible to perform by experimental work. Moreover, CFD can provide a pinpoint insight for local flow phenomenon and allow for the alteration on corresponding parameters for optimization purpose. An example of PAT computer design model is shown in Figure 3.

PAT computer aided design model.
Natanasabapathi and Kshirsagar (2004) had conducted a simulation study on PAT using ANSYS CFX (V5.6) on newly developed unstructured mesh geometry replacing complex blocked mesh [20]. Unstructured mesh was used to match the pump complex geometry. The flow domain was divided into three individual parts as casing, runner, and draft tube. Total pressure boundary condition and average static pressure were set at the inlet and outlet, respectively. Comparison between experimental data and simulation shows good agreement for head drop across the turbine; however, there was a deviation in the efficiency for discharge. Further enhancement by additional interface ring between the casing and runner leads to considerably reduced error.
Yang et al. (2012) presented a computational fluid dynamics analysis on reverse mode performance prediction using commercial flow solver, ANSYS-CFX software [21]. The control volumes domains were divided into five component parts: inlet pipe, front, back chambers, impeller, and volutes. Each part used different types of mesh, tailored to suit flow pattern and requirements. Structured hexahedral grid was used to generate meshes for each individual component. Comparison of experimental and simulation results shows that both performance curves are in good agreement. The relative error between both results at BEP for efficiency, head, and power is −3.02%, −0.78%, and −0.78%, respectively. The study highlighted the importance to establish performance prediction model using theoretical analysis, empirical correlation, and simulation results.
Fernández et al. (2004) investigated three-dimensional flow simulation for end suction centrifugal pump installed with an impeller size of 200 mm operating in turbine mode by using commercial Fluent software [18]. Specially refined mesh was used at critical flow domain in the pump such as leading and trailing edges of the impeller and volute tongue. Uniform velocity distribution was set at the inlet and constant static pressure at the outlet. Turbulence effect of standard k-epsilon was used together with standard wall function. Good agreement and trend between numerical computation prediction and experimental analysis were observed. However, the numerical analysis yielded higher performance as predicted. The reason can be explained by leakage loss that was excluded in the simulation work. Once validated, the simulation model was later used to investigate hydraulic flow and radial force.
Rawal and Kshirsagar (2007) conducted numerical simulation on a single stage, mixed flow pump having an impeller size of 236 mm operating in turbine mode [22]. The flow domains considered for the simulation consist of casing, impeller, and draft tube. Unstructured tetrahedral mesh was used for all flow domains taking advantage of adjusting mesh density at critical flow zone. The boundary condition at the inlet was specified as known uniform pressure exerted by fluid flow from the penstock. The wall interface was set to no-slip boundary condition over wetted surface. K-epsilon turbulence model was used in this simulation. The simulation results match well with the experimental results for low flow range but perform poorly beyond the best efficiency flow range. The disparities between the simulation and the experiments were from frictional losses in mechanical system and leakage loss which was excluded in the simulation.
Derakhshan and Nourbakhsh (2008) conducted a simulation in pumping and turbine for an industrial centrifugal pump with specific speed of 23.5 using 3D full Navier-Stokes equation and FineTurbo V.7 flow solver [23]. Two different types of mesh grid were used for two flow domains developed by IGG5.5 for the volute and Autogrid5 for the impeller. The simulation model excluded flow domain between impeller hub and casing which excludes leakage loss, disc friction, and mechanical loss. However, these losses were estimated using Thorne and Stephanoff method and then added to the simulation power input. The simulation shows that BEP of the pumping mode gives good match but the turbine operation was not in good coincidence with the experimental data.
3.3. PAT Performance Improvement
Pump has low efficiency in turbine mode and geometric modification of the impeller can lead to an increase in efficiency. Modifications works on PAT were reported through rounding impeller blade and shrouds, installing splitter blades, enlargement of suction eye, and using fixed guide vane. To further understand the internal hydraulic characteristic, Singh and Nestmann (2011) had divided pump control volume into five different flow zones so it can be treated and optimized individually [24]. The control volume domain was enclosed between the inlet and outlet of the pump. By treating the zone as individual section, the alteration can be performed based on local losses. The aim of the experiment is to minimize modification in order to maintain cost-benefit of PAT. Among all geometrical modifications, rounding centrifugal tip is the most beneficial, reducing shock loss at the turbine inlet and increasing efficiency up to 2.4% as shown in Figure 4 [25]. In many cases, average modification work may potentially improve turbine mode efficiency between 2 and 3%. Conversely, the effect must be validated through experimental analysis because there are a large variety and number of pumps operating at various ranges of head and flow.

Singh (2005) had conducted an experimental investigation on the effect of impeller rounding for radial flow and mixed flow pump in turbine mode [26]. The modification gives a positive impact on the overall best efficient performance with a raise between 1 and 3%. The reason for the efficiency increase is from the reduction of loss coefficient due to rounding effect.
Suarda et al. (2006) had carried out experimental analysis on the effect of rounding off the impeller tips [27]. The modification was performed by grinding the pump impeller tips to rounded shape, eliminating excessive turbulence at the inlet. A centrifugal pump with specific speed of
Derakhshan et al. (2009) had performed a modification by rounding the blades leading edges and shroud [25]. The modification involves rounding up the impeller tips and shrouds by half of the blade thickness eliminating the sharp edges at pump inlet in turbine mode. An industrial pump with a specific speed of
Sun-Sheng et al. (2012) had studied the effect of splitter blades to a centrifugal pump in turbine mode [28]. A complete microhydro test rig with an electric eddy current dynamometer to regulate and measure the studied pump was constructed to test centrifugal pump with specific speed of 37.5. By introducing splitter blades to the impeller, the fluid flow inside the pump changed. The authors had proposed that by adding splitter blades there is a substantial decrease in pressure fluctuation between impeller blades and pressure gradually decreases along the outlet pipe. The splitter blades reduce the original pressure head and flow rate but increase the turbine mode performance by additional 6.66% from its original condition.
Patel et al. (2013) examine the effect of fixed guide vanes with NACA-4418 profile to part load operating conditions [29]. A smaller impeller size was used to make additional space by replacing 250 mm diameter impeller with 200 mm impeller. The installation of guide vanes at an angle of 75° helps guide the flow tangential with the impeller and thus reduces the loss of kinetic energy. The variation flow velocity inside the casing decreases, which leads to improvement of part load operating condition.
Many researchers have reported that the efficiency of pump in turbine mode can be improved by simple modification such as rounding impeller tips, installation of splitter blades, and reducing impeller size. Other pump modifications such as trimming the impeller diameter can alter the pump characteristic to match the operation condition. In some cases, minor modification to the pump impeller contributes to huge hydraulic improvement leading to increased efficiency.
3.4. Induction Generator
The use of induction motor as generator is usually employed for installed powers below 30 kW. It has been known that an induction motor which is normally coupled directly with PAT can be modified as AC generator and largely used in microhydro applications. Converting induction motor to induction generator is viable by carefully adding capacitor and wiring modification on the motor winding. The application of induction motor as generator is well proven in many microhydro sites [30]. Selection of appropriate capacitance for operating voltage and frequencies can be achieved in many ways. Listed are some of the methods to determine capacitance to initiate self-excitation.
Generally, minimum and maximum capacitance value can be derived from fundamental equations derived from equivalent circuit [31–33]. Brennen and Abbondanti (1977) had proposed an exciter scheme based on static reactive power generator with fixed capacitor and thyristor control inductors [34]. Harrington and Bassiouny (1998) had proposed using complex impedance matrix analysis loaded with an inductive load which involves algebraic equation solved by iterative approach [35]. The value of capacitor excitation at no load and the desired rate of operation can be determined iteratively.
Different from synchronous generator, induction generator does not have a voltage regulator. The generated frequency and voltage depend mainly on the power factor of the load, rotational speed from the turbine, excitation from the capacitor, and the load current applied to the terminal [30]. Induction Generator Controller (IGC) as power electronic device is used to regulate voltage and frequency output maintaining good power quality [36, 37]. The most popular IGC for microhydro application is Electric Load Controller (ELC). This type of IGC uses solid state electronic controller regulating voltage and frequency, maintaining constant applied load at generator terminal by dummy load. The function of ELC is to eliminate hydraulic control mechanism and let the turbine and generator run at their optimum operating speed.
The philosophy of ELC for rural electrification is to generate stable voltage and frequency using unsophisticated solid state electrical circuit maintaining a constant load at generator terminal. Since the possibility of sensitive electronic equipment is low and common loads are from resistive loads such as fan and lighting [38], the complexity of the control system is kept at a minimum level. This approach can be achieved by generating moderate power quality. With emphasis on optimum solution for remote microhydro, uncontrolled rectifier with a chopper controller dump load is the most favourable induction generator [30, 39]. This control system uses unsophisticated electric circuit with only one dump load and requires no batteries or inverters, which is deemed as simple, cheap, rugged, and reliable, as shown in Figure 5. This system offers satisfactory performance under transient and steady state, for balanced and unbalanced resistive load. An uncontrolled rectifier converts AC voltage to DC voltage and then it is filtered by filtering capacitor producing a variable unity power factor load. An insulated-gate bipolar transistor (IGBT) based chopper operates as load diverter, dumping excessive current to the dummy load maintaining constant applied load at the generator terminal.

Induction generators which are coupled with pump were found to be the best electric generators with PAT. With wiring modification and ELC, the system exhibit reliable, simple, and excellent for microhydro application.
3.5. Cost Analysis on PAT
One of the major cost analysis evaluations is to rationalise installation investment of PAT [40]. This will help users to assess the cost-benefit factor of PAT compared to commercial hydro turbine in a range of the operating period. For economic justification, PAT offers low initial cost at low efficiency but commercial hydro turbine has high efficiency at higher cost. The main function of economic benefit analysis is to justify the financial investment benefit to the project. The main economic evaluation aspect is price of unit energy cost ($/kWh) which is a financial indicator for the hydro scheme. In a microhydro scheme, the initial and operation cost vary and are site specific. Typical microhydro system costs include but are not limited to mechanical components, control system, electric distribution system, and civil structures. However, reviewed cost analysis in this study is focussed on electromechanical components supposing that other expenses are identical for any microhydro system. Case studies comparing commercial turbines with PAT have been reported in academic literature but in very small numbers.
Motwani et al. (2013) had carried out a cost analysis for commercial justification of centrifugal pump in turbine mode for hydropower application [41]. The performance characteristic of 3 kW PAT was determined through experimental analysis. It was found that the highest efficiency in turbine mode is around 60%. A conventional hydro turbine, Francis turbine, having an efficiency of 80% was chosen for the economic comparison analysis. The parameters considered in this cost analysis were initial cost of the project, capital recovery factor, annual expenses, discount rate, annual life cycle cost, annual energy generated, and cost of electricity generated per unit. Based on the study, the ratio of Annual Life Cycle cost and the cost of electricity generated per unit between Francis turbine and centrifugal pump in turbine mode were found to be 6.8 and 5.07, respectively. The study had also signified that the cost of electricity generation ($/kWh) for centrifugal pump in turbine mode is 5 times cheaper compared to Francis turbine.
Chuenchooklin (2006) explained the implementation of centrifugal pump in turbine mode to generate power for electrification of Thailand conservation area [42]. A centrifugal pump, model Mono flo MF 65–16 with 3 horse power (hp), was used for the project. PE pipe with inner diameter of 100 mm was used as the system penstock. An electric controller system was installed to regulate the voltage output to 220 V by using parallel system together with series of running capacitors. The cost of the project was approximately USD 4000. It was found that 45% of the expense is for penstock, 37% for electric control, and 18% for PAT and induction generator. The electricity energy production was reported to be 8760 kWh per year and, with energy price of 0.75 cent per kWh, the payback period will be in 6 years.
Arriaga (2010) presented a pico hydro development status in Lao PDR and proposed the use of PAT as a cost-effective solution for electrification for isolated communities [43]. Three power generation options were considered including PAT, commercial Vietnamese crossflow, and PV panels. Cost estimation model divided the expenditure into three categories including energy generation equipment, civil works, and energy distribution system. The analysis shows that a 2 kW PAT system offers a 53% cost reduction for energy generation equipment compared to Vietnamese crossflow turbine. PAT offers the lowest installation cost per kW compared to commercial crossflow turbine and PV panel.
4. Conclusion
This paper reviews previous research works on radial flow and end suction centrifugal pump operating as turbine for standalone microhydro application. Experimental and simulation works show that, by inversing the fluid flow, end suction centrifugal pump can work well in turbine mode. However, BEP for turbine mode is slightly lower than the pump mode. Efficiency improvement is viable by modification of the pump impeller and it was found that rounding impeller tips contribute the highest efficiency improvement. Induction motors which usually come with pump can be modified into induction generator by adding capacitor. ELC can be used to regulate voltage and frequency producing satisfactory power quality by maintaining shaft rotational speed. The use of induction generator further reduces the overall cost and justifies the economic feasibility of PAT as practical options. With low initial cost, energy generation cost is 5 times lower and the payback period is shorter than commercial hydro turbines. Moreover, the know-how maintenance knowledge is readily available in local areas. This further reduces maintenance and operational cost of the system.
Conflict of Interests
The authors declare that there is no conflict of interests regarding the publication of this paper.
