Evolutions of flow patterns and pressure fluctuations in a prototype pump-turbine during the runaway transient process after pump-trip

Evolutions of flow patterns and pressure fluctuations in a prototype pump-turbine during the runaway transient process after pump-trip

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Journal Pre-proof Evolutions of flow patterns and pressure fluctuations in a prototype pump-turbine during the runaway transient process after pump-trip Zhiyan Yang, Yongguang Cheng, Linsheng Xia, Wanwan Meng, Ke Liu, Xiaoxi Zhang PII:

S0960-1481(20)30098-7

DOI:

https://doi.org/10.1016/j.renene.2020.01.079

Reference:

RENE 12942

To appear in:

Renewable Energy

Received Date: 26 January 2019 Revised Date:

10 January 2020

Accepted Date: 18 January 2020

Please cite this article as: Yang Z, Cheng Y, Xia L, Meng W, Liu K, Zhang X, Evolutions of flow patterns and pressure fluctuations in a prototype pump-turbine during the runaway transient process after pumptrip, Renewable Energy (2020), doi: https://doi.org/10.1016/j.renene.2020.01.079. This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing this version to give early visibility of the article. Please note that, during the production process, errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain. © 2020 Published by Elsevier Ltd.

Zhiyan Yang:Conceptualization, Writing - Original Draft, Writing- Reviewing and Editing. Yongguang Cheng: Supervision, Resources, Writing - Original Draft, Writing- Reviewing and Editing. Linsheng Xia: Writing Original Draft, Investigation. Wanwan Meng: Writing - Original Draft, Validation. Ke Liu: Methodology, Validation. Xiaoxi Zhang: Investigation, Validation, Methodology.

1

Evolutions of flow patterns and pressure fluctuations in a prototype pump-turbine

2

during the runaway transient process after pump-trip

3 4

Zhiyan Yanga, Yongguang Chenga*, Linsheng Xiab, Wanwan Menga, Ke Liua and

5

Xiaoxi Zhangc

6 7

a. State Key Laboratory of Water Resources and Hydropower Engineering Science,

8

Wuhan University, Wuhan 430072, China

9

b. China Ship Development and Design Center, Wuhan 430064, China

10

c. School of Environmental Science and Engineering, Xiamen University of

11

Technology, Xiamen 361024, China

12 13

Corresponding author: Yongguang Cheng; E-mail: [email protected]

14 15

Abstract: The runaway after pump-trip is a fast transient process, during which unit

16

vibrations, water-hammer fluctuations, pressure pulsation changes and flow pattern

17

transitions happen violently, endangering pump-turbine units of pumped-storage

18

power stations. In this paper, based on validated CFD data from 1D-3D coupled

19

simulation, we describe the evolutions of flow patterns and pressure fluctuations in a

20

prototype pump-turbine during this working point fast sliding process, and try to

21

reveal the influence mechanism of flow pattern transitions on pressure fluctuation

22

changes. The results show that the general evolutions of flow patterns are dominated

23

by the changes of the runner velocity triangles, which are controlled by the changes of

24

the discharge and rotational speed. Inhomogeneous local flow also contributes to

25

abundant local vortex structures, such as rotating-stall vortices in the vane and runner

26

regions, skirt and helical vortices in the draft-tube, separation vortices in the blade

27

channels, and the impinging jets on the blade surfaces. These unstable vortices appear,

28

change, and vanish in a fast transitional and uneven manner, leading to great

29

differences in pressure and runner force fluctuations in different working regions.

30 1

31

Key words: pump-turbine, runaway transient process, 1D-3D coupled simulation,

32

flow patterns, pressure fluctuations, runner forces

33 34

1. Introduction

35

Pumped-storage power is the largest and best regulator in the power grid for its

36

irreplaceable capacities of peak fitting, valley filling, frequency regulating, phase

37

modulating, and spinning reserving. With the development of intermittent renewable

38

energies, the complementary functions of pumped-storage become more and more

39

important. Because a pumped-storage plant has many operating conditions and

40

transformations between different operations, violent pressure fluctuations and

41

machine vibrations in pump-turbines can be encountered in many pumped-storage

42

plants. During transient processes, such problems will become more severe, because

43

the working point passes through various working modes, which may include the

44

hump and S-shaped characteristic regions where unstable flow structures develop and

45

change abruptly [1-2]. The pump-trip runaway, an accident process when the

46

motor-generator is rejected from the power grid but the guide vane servomotor fails to

47

close, is the most violent one because both the hump- and S-shaped regions are

48

experienced [3]. During this process, the runner will be decelerated and accelerated by

49

dynamic working head, and complex flow pattern transitions and severe pressure

50

fluctuations will happen, which could endanger the safety of units. Therefore, despite

51

the probability of the pump-trip runaway is small, it is one of the must studied

52

transient processes in the design stage of pumped-storage plants. To analyze this fast

53

changing phenomenon, considering the superposition of water-hammer in water

54

conveyance system and pressure pulsations in pump-turbine, and understanding the

55

relationship of flow patterns, pressure pulsations and runner forces, are important,

56

because their interactions, correlations and evolutions are the main cause of a series of

57

unit vibration problems [4].

58

Many studies on flow patterns and pressure pulsations in pump-turbines have

59

been conducted based on computational fluid dynamics (CFD) simulations or model

60

tests, and some correlations between them have been clarified [5-7]. However, the 2

61

attentions of the existing investigations were mainly focused on the flow

62

characteristics of a certain steady working condition. Xia [8] and Pacot [9] analyzed

63

the rotating-stall instabilities of a pump-turbine in the pump mode and concluded that

64

the rotating-stall could cause periodical high pressure. Liu [10] found that the

65

cavitation on the suction side of runner inlet could lead to great changes of pressure

66

distributions on blade surface, when the pump-turbine worked in the hump-shaped

67

region. Foroutan [11] reported that the pressure fluctuations in a simplified draft-tube

68

due to the vortex rope could have a large amplitude, as high as twice the local mean

69

pressure value. Hasmatuchi [12] presented the experimental evidence of the

70

rotating-stall in a model pump-turbine working in the S-shaped region, and found that

71

the pressure pulsating amplitude increased when the discharge decreased. Recently,

72

Xia [19] found the backflow patterns at the runner inlet in the pump-turbines working

73

in the S-shaped region, and discussed the correlation between the working points

74

located along the guide vane opening curves and their corresponding flow patterns.

75

As for transient processes, studying the flow characteristics by model tests is

76

very difficult and CFD simulation becomes the basic tool. A few studies on this topic

77

have already been reported [13] and the evolutions of pressure fluctuations

78

corresponding to the flow transitions have been discussed [14-16]. However, they

79

were limited by only considering some specific working conditions, and most

80

questionably ignoring water-hammer pressure effects [17], without which the dynamic

81

characteristics of pump-turbine cannot be fully considered. In addition, the generation

82

mechanism of special flow patterns has not been discussed in depth, and the

83

coexistence of multiple vertex structures has been neglected. Li [18] investigated the

84

transient process in pump mode, in which the guide vanes were closing and the

85

rotational speed was constant, and found that the obvious flow separations in the

86

runner and vanes could result in significant pressure fluctuations. Staubli [19]

87

predicted the unstable flow fields during turbine starting-up process in the turbine

88

mode, and found time-varying inflow and outflow from the runner into the vaneless

89

space could be the cause of instability. Liu [20] simulated a load rejection transient

90

process of a prototype pump-turbine, and found that the vortex ropes in the draft-tube 3

91

had large deviations from the results in steady working conditions. Li [21] simulated

92

the normal shutdown process of a prototype pump-turbine in turbine mode, and

93

investigated the global characteristics and pressure fluctuations under the emergence

94

of flow separation and vortex formation. Xia [22] studied the runaway transient

95

process from a turbine working point, and concluded that the locally distributed

96

backflow vortices at the runner inlet could enhance the local rotor-stator interaction,

97

and the evolving rotating-stall could induce asymmetrical pressure distribution on

98

runner blades.

99

From the above works, we know that the flow patterns in pump-turbines working

100

in different modes show quite different features, contributing to great differences in

101

pressure fluctuations. This is an obvious conclusion for both steady conditions and

102

transient processes. But how the flow patterns change during the transient processes

103

that experience different working regions, and how they influence the alterations of

104

pressure pulsations and runner forces, need to be clearly stated.

105

In this study, the runaway transient process after pump-trip in a prototype

106

pumped-storage power station was simulated, and the evolutions and correlations of

107

pressure fluctuations, runner forces and flow structures were analyzed. The paper will

108

describe the basic simulation model and parameters; the resulting histories of macro

109

parameters; the evolutions of flow structures, pressure pulsations, and runner forces.

110

The results are discussed according to the trajectory curve in the characteristic plane,

111

and related by the short term Fourier transformation.

112 113

2. Numerical Methods

114

2.1 The pumped-storage station and its simulation model

115

A low-head pumped-storage power station with two 150MW units in one water

116

conveyance system was considered. As shown in Fig.1, the system includes an

117

upstream reservoir (water level 397.67m), a diversion tunnel, two penstocks, two

118

pump-turbine units (rated head 126.7m in the pump mode), two downstream conduits,

119

and a downstream reservoir (water level 291.28m). The setting elevation of the units

120

is 264.00m. The pumping condition with one unit in operation was simulated in this 4

121

study. The 1D-3D coupling method [23] was adopted, in which the diversion tunnel,

122

penstock and downstream conduit were simulated by the one-dimensional (1D)

123

method of characteristics (MOC), while the pump-turbine was simulated by

124

three-dimensional (3D) CFD. The profile and parameters of computational domain are

125

shown in Fig. 1, while the 3D model of pump-turbine and the layout of several

126

monitoring points are shown in Fig. 2. The basic parameters of the pump-turbine are

127

given in Table 1, in which D1 denotes the runner outlet diameter (pump mode), D2 the

128

runner inlet diameter (pump mode), nr the rated rotational speed, Zb the number of

129

runner blades, ngv the number of guide vanes, nsv the number of stay vanes, ns the

130

specific-speed (pump mode), and Hr the rated head (pump mode).

131

Fig. 1. Profile of the computational domain

132

Fig. 2. 3D model of pump-turbine and schematic of monitoring points and sections

133 134

Table 1. Main parameters of the prototype pump-turbine Parameter

Value

Parameter

Value

D1 (m)

5.2265

Zb

7

D2 (m)

4.132

ngv

20

nr (rpm)

200

nsv

20

ns (m,m3/s)

59.9

Hr (m)

126.7

135 5

136

2.2 Numerical schemes

137

Commercial software ANSYS FLUENT 15.0 was used in the 1D-3D simulations.

138

The 3D geometry in Fig. 2 was discretized into structured meshes with multiple

139

blocks by ANSYS ICEM 15.0. A grid refinement evaluation was performed and we

140

found that the relative differences in macro parameters from 6.9 million to 8.0 million

141

grid elements are negligible. Therefore, the mesh with 6.9 million grid elements was

142

finally chosen (Table 2), in which fine boundary layers are set up in the regions of

143

stay vanes, guide vanes, and runner.

144 145

Table 2. Number of grid elements (million) Draft-tube with

Spiral casing with Runner

Stay vanes Guide vanes 1.2

Total extended tube

extended tube 1.0

1.1

2.3

1.3

6.9

146 147

We selected the SAS-SST turbulence model, and specified the transient

148

simulation timestep as 0.00125s, which corresponds to 1.5 degrees of runner rotation

149

at the rated speed. For both steady and unsteady working conditions, the SIMPLEC

150

algorithm was chosen to achieve the coupling solution of the velocity and pressure

151

equations. The second order discretization in time and in space was used.

152

Boundary conditions were defined as follows. The outlet and inlet of pipes in 3D

153

model were set as static pressure and total pressure boundary conditions by 1D MOC,

154

respectively. At the 1D-3D interfaces, the partly overlapping coupling method in

155

reference [23] was used and the compressibility of water was simulated by defining

156

the pressure depended density, as shown in Eq. 1. The friction and local head losses in

157

each pipe were considered in the 1D model. ρ = ρ0 e(p-p0 )/ρ0 a

158

2

(1)

159

where ρ and p are the density and pressure of water, respectively; ρ0 and p0 are the

160

initial values of ρ and p, respectively; e (-) is the base of natural logarithms; a is the

161

acoustic speed in water. 6

162

2.3 Computation of the varying speed of turbine unit

163

The rotation of the runner was simulated by the sliding mesh model during

164

runaway process. The angular speed ω of the runner varies with time in accordance to

165

angular momentum equation, as shown in Eq. 2, and a User-Defined-Function (UDF)

166

program in ANSYS FLUENT 15.0 was used to realize the variation of rotational

167

speed.

168

T

ωt = ∆t + ωt-∆t J

(2)

169

where J is the total rotational inertia of runner and motor-generator; T is the hydraulic

170

torque acting on the runner; ωt and ωt-Δt are the rotational speed at the current and

171

previous timesteps, respectively; ∆t is the timestep.

172 173

2.4 Validation of the simulation model

174

Before simulating the runaway transient process, the 1D-3D coupling model

175

should be validated. Because the data of a field test for the pump-trip transient process

176

with a designed closing law of guide vanes from the original opening (GVO) 23.6

177

degrees was available, we simulated the same condition for comparison. Fig. 3 shows

178

the resulting macro parameters, in which the field test curves provided by the test

179

engineer are filtered. Compared to the field test values, the simulated pressure history

180

has stronger fluctuations, which should be the signals of water-hammer in pipelines

181

and complex flow structures in the pump-turbine. The water-hammer cycle in the

182

upstream pipeline is around 1.25s, corresponding to the pressure fluctuating cycle at

183

P1 after guide vanes have closed. The relatively high frequency fluctuations at P4

184

should be caused by vortices in draft-tube and runner passages. Generally speaking,

185

the simulation results are in good agreement with the field test results, and the

186

reliability of the 1D-3D coupled approach is validated. Then, the runaway process

187

without guide vane closing after the pump-trip from the same steady working point

188

was simulated, which will be explained in later sections.

7

189

Fig. 3 Validation of the 1D-3D coupled CFD model by field test results

190 191

3 Results of the runaway transient process after pump-trip

192

3.1 Macro parameters during the runaway process

193

During the runaway process, the working point passes through the pump,

194

pump-braking, turbine, and turbine-braking modes, and its dynamic trajectory travels

195

across these regions and finally revolves around a zero-torque point with fluctuations,

196

as shown by the red curve in the n11-Q11 plane of Fig. 4, in which the unit speed

197

n11 = -nD1 / √H and unit discharge Q11 = -Q / (D21 √H) are defined. The dynamic

198

curve has a good agreement with the static characteristic curve (black curve, obtained

199

by model tests) in the pump, pump-braking and turbine modes, excepting near the

200

static zero-torque point. Not following the static characteristic curve, the dynamic

201

trajectory fluctuates and gradually converges to a speed-no-load region, which is on

202

the left of the static zero-torque point. If the errors in model tests and simulation are

203

considered, the remaining deviations of the dynamic and static curves should be

204

owing to the unstable vortex structures developed in the whole runaway process,

205

which are marked in Fig. 4.

206

The histories of the key macro parameters during the runaway are shown in Fig.

207

5, in which the process has been divided into six modes: pump (P), pump-braking

208

(PB), turbine (T1), turbine-braking (TB), turbine (T2), and no-load runaway (NL). The

209

transition from the P mode to PB mode is defined by the sign of discharge Q changing

210

from positive to negative, namely the flowing direction changes from pump direction

211

to turbine direction but the runner rotates still in pump direction. The transition from 8

212

the PB mode to T1 mode is defined by the sign of rotational speed n changing from

213

positive to negative, namely the rotating direction changes from pump direction to

214

turbine direction and the runner works in normal turbine condition. The transition of

215

T1 mode and TB mode is defined by the sign of torque T changing from negative to

216

positive, namely the water driving power is surpassed by the water dissipating power.

217

The NL mode defined by the small and fluctuating turbine output power when the

218

working point revolves around the zero-torque point. These definitions are

219

corresponding to the characteristic regions in Fig. 4(b).

220

Due to the specific-speed of this pump-turbine is relative large, there is no larger

221

fluctuations in rotational speed and discharge during the last no-load runaway mode,

222

which is obviously different from the unstable fluctuations in the S-shaped region for

223

many low specific-speed pump-turbines [24]. The torque T varies with normal laws in

224

the P, PB and T1 modes, and becomes unstable in the TB, T2 and NL modes. The

225

axial force of runner (Fz) in the P and PB modes is mainly affected by the

226

water-hammer and increases quickly at the beginning of the P mode. However, in the

227

T1 mode, Fz decreases sharply before the working point is approaching to the rated

228

turbine point. Once entering the last three modes, Fz becomes unstable and fluctuates

229

with high frequencies and large amplitudes. For the radial force (Fx and Fy) of runner,

230

the variation range is not large and the fluctuations in the last TB, T2 and NL modes

231

are also severe. Obviously, all the severe fluctuations in torque and runner forces

232

begin after the working point enters the so-called S region, although the S-shaped

233

shape is not obvious for this low-head pump-turbine.

(a) Original data

9

(b) Low-pass filtered data in S-shaped region Fig. 4. Dynamic trajectory curve in the n11 – Q11 plane

234

(a) Histories of torque, discharge and speed

(b) Histories of runner forces

235

Fig. 5. Histories of macro parameters during the pump-trip runaway process. (P:

236

pump; PB: pump-braking; T1 and T2: turbine; TB: turbine-braking; NL: no-load

237

runaway)

238 239

3.2 Pressure fluctuations during the runaway process

240

The pressure fluctuations at points P1, P2, P3 and P4 during the runaway

241

transient process are shown in Fig. 6. On the whole, regional variation features are

242

obvious as the working point passes through the six modes successively. In the P

243

mode, the rapidly decreasing discharge after the sudden power loss causes a negative

244

water-hammer wave upstream the runner and a positive water-hammer wave

245

downstream the runner (Fig. 6(b)). Accordingly, the pressure histories at monitoring

246

points P1, P2 and P3 show rapid decrease and the pressure at point P4 shows rapid

247

increase (Fig. 6). When the working point enters the PB mode, the flow direction

248

reverses and the torque turns to increase again (Fig. 5(a)), leading to the gradual

249

restorations of pressure values at the monitoring points (Fig. 6). The pressures recover

250

roughly to their initial values when the working point gets into the T1 mode. In the 10

251

TB mode, the torque value becomes positive, meaning energy dissipation (Fig. 5(a)),

252

accordingly the pressures at P1, P2 and P3 begin to decrease and that at P4 begins to

253

increase (Fig. 6). These pressure decreases and increases during the first four modes

254

are mainly related to the water-hammer in water conveyance system and the

255

pump-turbine characteristics transferring between the operating modes. After the T2

256

mode, the discharge and speed are approaching to a steady level, therefore the pipe

257

water-hammer effect becomes weak and turbine pressure pulsation effect becomes

258

dominant (Fig. 6). It can be seen that the pressure fluctuation amplitudes increase

259

rapidly once the working point leaves the turbine best efficiency point (t = 21.5 s), and

260

they approach to the maximum values after entering the TB mode. The violent

261

fluctuations continue in the T2 and NL modes, showing no damping tendency. The

262

fluctuation frequencies and amplitudes at P3 are much higher than at other points,

263

because the pressure pulsations by the rotor-stator interaction are superimposed.

(a) Original pressure data 264 265

(b) Low-pass filtered data

Fig. 6. Histories of pressure fluctuations at different monitoring points 3.3 Evolutions of flow patterns during the runaway process

266

To investigate the mechnism of large pressure fluctuation amplitudes, the

267

evolutions of flow patterns in the vane, runner and draft-tube regions were analyzed.

268

Three stream surfaces with spanwise ratios 0.1, 0.5, and 0.9 across the vane and

269

runner (Fig. 2) were selected to show the flow patterns. At the same time, the velocity

270

triangles at the inlet (adjacent to the guide vanes) and outlet (connected to the

271

draft-tube) of runner were borrowed to interpret the general development trends of

272

flow patterns, even though it cannot describe local vertex structures accurately. 11

273

When the unit is in a steady pumping operation, the flow fields in the

274

pump-turbine are smooth, and there are no obvious vortex structures and flow

275

blockages (Fig. 7, t = 0.0 s). Accordingly, the pressure pulsations are stable and have

276

no high amplitude signals. However, during the runaway process, the pressure

277

fluctuations vary quickly and the flow patterns evolve with various vortex structures.

278

(1) Pump mode (t < 6.5 s)

279

When the pump is suddenly powered off, the rotational speed, discharge and

280

head begin to decrease simultaneously, because the runner is decelerated by the

281

resisting torque of water. In addition, because the water pumping force is proportional

282

to the square of rotational speed, the decrease of discharge is faster than that of

283

rotational speed (Fig. 5(a)), leading to the reduction of outflow angle α1, which is

284

defined by the angle between the absolute flow velocity V1 and the peripheral velocity

285

U1, as shown Fig. 7. Because U1 in the vaneless region is still high and the water in

286

the vane region is slowed down, the enhanced shearing action and the large attack

287

angle to the vanes generate several rotating-stall vortices. The existing studies [5,8]

288

showed that when the rotating stalls occur, the disturbed flow and blockage can only

289

be observed in part of blade and vane channels (Fig. 7, t = 5.5, 6.0 s), which result in

290

uneven circumferential outflow and pressure distributions.

291

As for the inflow triangle, the absolute flow velocity V2 near the pressure surface

292

of runner blades decreases sharply, resulting in the increase of the inflow attack angle

293

β2, which is defined by the exterior angle between the relative velocity W2 and the

294

peripheral velocity U2. When the inflow water impacts with runner blades, it separates

295

from blades and contributes to large-scale separation vortices in the blade passages

296

(Fig. 8(a)). Overall, the main axes of vortices in the vane and runner regions are

297

approximately perpendicular to the stream surfaces. For the flow in the draft-tube,

298

previous studies showed that when water flows into the runner region, it is disturbed

299

by the runner and has circumferential components [25]. And the decrease of runner

300

discharge will result in the increase of the circumferential components of draft-tube

301

water. Here, to identify the vortex structures accurately, a newly proposed omega

302

method was used [26], which considers vortex as a region where vorticity overtakes 12

303

deformation and are superior to other methods (e.g., vorticity tube, Q-criterion and

304

Lambda-2 method) [27,28]. In this case, once the pump is tripped, due to the decrease

305

of runner flow capacity and the inertia of water in the draft-tube, the inflow water will

306

impinge on the pressure surfaces of runner blades, forming backflows on the shroud

307

side (Fig. 8(b)). The upward main flow in the draft-tube center moves shearing with

308

these backflows, generating backflow vortex structures near the draft-tube wall.

309

Under the disturbance of the runner, these vortices further separate into several skirt

310

shaped vortices (Fig. 7, t = 5.5, 6.0 s).

311

Generally speaking, the smaller the discharge, the more complex the flow

312

patterns. Also, the velocity triangles can only show the developing trend of flowing

313

state, but the local backflows and vortices cannot be accurately described, which

314

reflects the complexity and inhomogeneity of the flow patterns.

315

Fig. 7. Velocity triangles and flow patterns in the pump mode

(a)

(b) 13

316 317

Fig. 8. Separations in runner passages (a) and backflows in the draft-tube (b) (t = 6.0 s)

(2) Pump-braking mode (6.5 s < t < 13.7 s)

318

Due to the recovering pressure head on the turbine (Fig. 6(b)), the flowing

319

direction begins to reverse to the turbine direction, but the rotating direction remains

320

in the pump direction, even though the rotational speed continues to decrease (Fig.

321

5(a)). In the initial stage of pump-braking mode, because the rotational speed, inflow

322

angle β1 (defined by the exterior angle between the relative velocity W1 and the

323

peripheral velocity U1) and centrifugal force at the runner inlet are still large, flowing

324

into the runner passages is not smooth. The inflow strongly impacts the pressure

325

surfaces of the blades. The impact makes some water turning left and returning to the

326

vaneless space, some water jumping over and impacting the next blade, and some

327

water turning right and entering the blade passages, which form large separation

328

vortices around the suction surfaces of the blades (Fig. 9, t = 9.0 s).

329

At the runner outlet, the increasing outflow angle α2 (defined by the angle

330

between the absolute flow velocity V2 and the peripheral velocity U2) pushes the main

331

flow near the draft-tube wall to develop stronger, with the reverse flow in the center

332

also intensified (Fig. 9, t = 13.0 s). In detail, a part of the outflow goes into the

333

draft-tube directly, and the rest goes round to suction surfaces, which intensifies the

334

shearing actions with the upward flow in draft-tube center and produces separation

335

vortices near suction surfaces (Fig. 10).

336

In the later period of the pump-braking mode, with the increase of discharge, the

337

main flow in the vane region gradually becomes strong and steady, depressing the

338

local small vortex structures between vanes. Also, the large separation vortices in

339

runner passages are decreasing in scale but not in intensity.

340

According to the above two working regions, the different flow patterns have

341

different influences on pressure fluctuations. Generally speaking, the formation of

342

vortex structures can produce higher amplitude pressure fluctuations, which should be

343

weakened if the vortex structures disappear. However, the pressure fluctuating

344

amplitudes increase obviously in pump-braking mode, far larger than in the pump

345

mode (Fig. 6(a)). The reason is that the vortex structures in the pump mode are 14

346

generated by shearing action. Due to low energy dissipation, these vortices are

347

difficult to produce higher amplitude signals. But in pump-braking mode, the strong

348

impacts on the runner blade pressure surfaces and the large separating vortices on

349

suction surfaces are high energy dissipated, which can produce high amplitude signals.

350

Therefore, it is not the number and size of vortices that determines the amplitudes of

351

pressure fluctuations, but the strengths of impacting on the solid walls and interacting

352

between vortices.

353

Fig. 9. Velocity triangles and flow patterns in pump-braking mode

354

(a) 355 356

(b)

Fig. 10. Flow patterns in runner passages and draft-tube in pump-braking mode (t = 9.0 s)

(3) Turbine mode T1 (13.7 s < t < 28 s)

357

Affected by the increasing resisting torque, the runner begins to rotate in the

358

direction of turbine mode, companied by increase of discharge. In the initial stage,

359

because of the relatively small peripheral velocity U1 and the small inflow attack

360

angle β1, the impacting of inflow on blade pressure surfaces accelerates the rotational

361

speed of runner, and the separation vortices on the suction surfaces still exist (Fig. 11,

362

t = 16.0 s). With the increase of rotational speed, namely the increase of peripheral 15

363

velocity U1, β1 becomes larger gradually and fits to the blade inlet angle, contributing

364

to scale and intensity decreases of the separation vortices. At the optimal working

365

point (about t = 21.5 s), the inflow enters the runner passages without any hindrance,

366

and the outflow at the runner outlet flows vertically and smoothly down to the

367

draft-tube (Fig. 11, t = 21.5 s). However, after t = 21.5 s, when the working point

368

passes through the optimal, the rotational speed and the inflow attack angle β1 at the

369

runner inlet continues to increase, and separation vortices occur again on the blade

370

suction surfaces (Fig. 11, t = 27 s). Fig. 12 shows the flow patterns in a single runner

371

passage. Once the working point leaves the optimal, obvious backflows occur on the

372

shroud side due to the centrifugal force and the increasing impact on the runner blade.

373

A part of the backflows jumps into the nearby runner channel, and a part goes back to

374

the vaneless space. On the hub side, the water flows into the blade passage easily.

375

As for the draft-tube, in the turbine mode with different discharges, flow patterns

376

have a developing manner, which are corresponding to the findings in references

377

[11,29]. Fig. 13 shows vortex structure evolutions in the draft-tube at different times.

378

As flow rate increases, backflows in the draft-tube center weakens, resulting in the

379

shrinking of skirt vortex structures near the wall and the developing of a single thick

380

eccentric vortex belt in the center. When the working point is before the optimal, the

381

larger the discharge, the finer the vortex shape, which is approaching a conical

382

cucumber shape from a helical rope shape. Once the working point leaves the optimal

383

the optimal, skirt vortices are re-generated and overspread the whole wall.

384

It is evident from the pressure fluctuation diagram (Fig. 6(a)) that when the unit

385

enters the turbine mode, especially before t = 21.5 s, the pressure fluctuations

386

gradually decrease at P2 and P3 due to the disappearance of the unstable vortex

387

structures. However, high amplitude pressure fluctuations at P4 and runner radial

388

forces (Fig. 5(b)) still keep exist during this time, it should be due to the existence of

389

the vortices in the runner passages and draft-tube (Fig. 11, t = 16 s). After t = 21.5s,

390

the pressure amplitudes begin to increase again because of the backflows at the runner

391

inlet [30]. Due to backflows in the vaneless space, the recirculation inside the blade

392

passages, and the impact by the runner blades, the rotor-stator interaction is 16

393

intensified and the pressure fluctuating amplitudes increase greatly (Fig. 6(a)).

394

Fig. 11. Velocity triangles and flow patterns in the pump-braking mode

395

t = 21.5 s 396

t = 27.0 s

Fig. 12 Flow patterns in a single runner passage at different times

397

398

t = 16.0 s

t = 17.0 s

t = 18.0 s

t = 20.0 s

t = 21.0 s

t = 21.5 s

t = 25.0 s

t = 27.0 s

Fig. 13. Evolutions of the vortices in the draft-tube 17

399

(4) Turbine-braking mode TB, turbine mode T2 and no-load mode NL (t > 28 s)

400

From the histories of pressure fluctuations in Fig. 6, it can be seen that the last

401

three working regions are similar because of the constant trends of rotational speed

402

and discharge. In these three stages, the pressure pulsating amplitudes are the largest

403

in the vaneless space. The vaneless space should be the area where energy is

404

dissipated during runaway process, because the increase of amplitudes can be

405

considered as the increase of energy dissipation. Fig. 14 shows flow patterns in a

406

single runner passage and draft-tube, which are similar to those in the turbine mode

407

after the optimal working point.

408

To better investigate the internal flow patterns when the runaway is approaching

409

to the NL point, three stream sections cutting through the runner and vane regions at t

410

= 70 s are shown in Fig. 15. Obviously, on the hub side and middle span, there are

411

only a few separation vortices near the blade suction surfaces. However, on the shroud

412

side, more vortices exist near the blade pressure surfaces, accompanied with

413

backflows at the runner inlet. As a result, the stronger shearing action induced by the

414

high-speed flow in the vaneless space and the low-speed flow in the vane region,

415

contribute to the formation of separation vortices on the abdomen of guide vanes.

(a)

(b)

416

Fig. 14. Flow patterns in a single runner passage (a) and draftt-ube (b) (t = 70.0 s)

417

Fig. 15. Flow patterns on the three stream sections at t = 70.0 s

418 419

3.4 Frequency spectrum A time-frequency analysis of the transient pressure fluctuations at the monitoring 18

420

points is performed by using the Short Time Fourier Transform (STFT) [31], and the

421

results are shown in Fig. 16. At the beginning of the runaway process, the

422

characteristics of pressure fluctuations are mainly influenced by the runner. The

423

dominant frequency in the spectrograms is the blade passing frequency (BPF), and the

424

rest high frequencies are the integer multiples of the BPF. Due to the decreases of the

425

rotational speed and discharge, the vortex structures generated in the vane and runner

426

regions cause the generation of relatively low frequency signals with relatively higher

427

amplitudes (4.0 s < t < 6.5 s). In the transferring process from pump mode to

428

pump-braking mode, it is obvious that, due to the separation vortices and the impact

429

on runner blades, higher frequency signals and low frequency signals mix up and

430

display no clear boundary, and changing trends of the frequencies are in accordance

431

with the change of the rotational speed (6.5 s < t < 13.7 s). When the unit enters the

432

turbine mode, the frequency distinction becomes clear, and the amplitudes decrease

433

greatly near the better operation region (13.7 s < t < 21.5 s). These are because the

434

vortices in the vane region become weak or disappear. Once the working point leave

435

the optimal, the amplitudes increase gradually because of the violent rotor-stator

436

interaction induced by backflows (21.5 s < t < 28 s). After t = 28 s, the unit goes into

437

TB, T2 and NL modes in turn. All the low frequency and high frequency signals joint

438

again, and the amplitudes become very strong. These should be due to the various

439

vortices in the vane region, vaneless space, runner, and draft-tube.

(a) Point P1

(b) Point P2

19

(c) Point P3 440 441

(d) Point P4

Fig. 16. Frequency spectra for pressures at the monitoring points 4. Conclusions

442

The flow patterns, pressure pulsations, and runner force fluctuations during the

443

runaway transient process after pump-trip experience rapid and dynamic evolutions,

444

because the working point slides across the pump, pump-braking, turbine 1,

445

turbine-braking, turbine 2, and no-load runaway modes successively. In this study, we

446

analyzed the evolutional phenomena in this process and found that the changes in

447

pressure pulsations and runner force fluctuations are correlated to the transition of the

448

flow patterns, which have distinct features in different modes. Apart from the

449

rotating-stall vortices in the vane and runner regions in the pump mode, the impact

450

and separation vortices in the blade channels, the skirt and backflow vortices in the

451

draft-tube in the pump-braking and turbine 1 modes, along with the backflow vortices

452

at the runner inlet in the turbine-braking, turbine 2, and no-load runaway modes, are

453

the main causes that make the fluctuating magnitudes of pressure and runner forces

454

larger. The main findings are summarized as follows.

455

(1) When the discharge becomes small in the pump mode, the rotating-stall

456

vortices in the runner and vane regions develop due to the shearing action, and the

457

skirt vortices near the draft-tube wall appear due to the back and rotating flow around

458

the circumference.

459

(2) In the pump-braking mode, the flowing direction changes to the turbine

460

direction but the rotating direction is still in the pump direction. The vortices in the

461

vane region disappear completely as the discharge increases. The distinguish flow

462

structures in this mode are the strong impact jets on the blade pressure surfaces and 20

463

the large separation vortices near the suction surfaces. In the draft-tube, the runner

464

outflow around the tube wall and the backflow in the center are enhanced with the

465

increase of discharge, resulting in larger skirt vortices distributed in the circumference.

466

These flow structures make the pressure and runner force fluctuations intensified.

467

(3) As the rotating direction turns to the turbine direction, the pump-turbine is

468

operating in the turbine mode. Before the working point is approaching to the best

469

efficiency point, the impact jets on the blade pressure surfaces and the separation

470

vortices near the suction surfaces, along with the skirt vortices and backflow in the

471

draft-tube are suppressed as the rotational speed increases. In the best efficiency point

472

all flow patterns become smooth. After the working point leaves this optimal point,

473

the runner and draft-tube vortices appear again. The shroud side backflows at the

474

runner inlet become visible before the working point is approaching to the

475

turbine-braking mode. The runner inlet backflows make the rotor-stator interaction

476

obvious, resulting in the increasing pressure pulsations and runner force fluctuations.

477

(4) In the turbine-braking to no-load runaway modes, the working point comes

478

back to the turbine mode many times. The flow characteristics during this last

479

oscillating and converging process are similar. Apart from the separation vortices in

480

the vane and runner regions, the skirt vortices in the draft-tube, the backflow vortices

481

at the runner inlet are the distinguished phenomenon. It is the backflow vortices that

482

make the pressure and runner force fluctuations more violent.

483

(5) During this runaway transient process, the pressure pulsations in the vaneless

484

space are the largest in the pump-turbine. This phenomenon is caused by the

485

rotor-stator interaction, which are intensified by the impact jets on blades and the

486

backflow vortices at the runner inlet. The skirt and helical vortices in the draft-tube

487

and the rotating-stall vortices in the runner and vane regions are the main source of

488

low frequency pressure fluctuations.

489 490

Funding

491

This work was supported by the National Natural Science Foundation of China

492

(NSFC) (Grant Nos. 51839008 and 51579187), the Natural Science Foundation of 21

493

Hubei Province (Grant No. 2018CFA010), and the Natural Science Foundation of

494

Fujian Province (Grant No. 2018J01525).

495 496

Acknowledgments

497 498

The numerical simulations were conducted on the supercomputing system in the Supercomputing Center of Wuhan University.

499 500

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25

•Evolutions of flow patterns and pressure fluctuations during runaway process were described. •Evolutions of flow patterns are dominated by changes of velocity triangles. •Inhomogeneous local flow contributes to vortex structures. •Different vortices lead to great differences in pressure fluctuations in different working regions.

Conflict of interest statement: Yongguang Cheng and other co-authors have no conflict of interest.