Variateur de fréquence dans pompe de condenseur de générateur de 300MW

Variateur de fréquence dans pompe de condenseur de générateur de 300MW
2009-12-28 16:12:14

Résumé Cet article introduit l’application de réforme avec variateur de fréquence VFD dans la pompe de condenseur d’une centrale de 300MW, expose les effets d’économie d’énergie et le mode d’opération après la réforme.

Mots clésVariateur de fréquence VFD, pompe de condenseur, unité de 300MW, application

 

The total capacity of Zhangjiakou Power Plant is 8 × 300MW. Steam turbine unit is produced by Dongfang factory. The condensing system of 5,6,7,8 are medium pressure system, equipped with 9LDTNA-5UA-type condensing pump made by

Shenyang pump factory. The motor YLST500-4 type is made by Xiangtan Electrical Machinery Factory.

Table 1   condensing pump parameters

Flow

Lift

Power

Voltage

Current

Speed

950m3/h

280m

1000kW

6kV

118.8A

1480r/m



 

 The condensing water mainly keeps the stability of deaerator water level by adjusting inlet gate, supplies mechanical seal cooling water to pump, low pressure axletree of steam turbine and other equipments, also to other low pressure bypass, spray cylinder, the cold water tank inside.

 

1. Introduction

1.1 Purpose

1The condensing water is medium pressure system. The pressure is not lower than 2.6Mpa when load is 300MW. Pressure is higher when opening is small during low load operation, which causes higher pressure. Gate opening control causes low economy. Even at full load, the opening is only about 30%, and much smaller at low-load.

2The high pressure condensing water causes the pipe a big vibration, the minimum flow adjustment gate leakage, meanwhile, makes the cooling water pipe of feed pump a big vibration and noise and adjustment gate damage. In addition, the motor of the pump has a big vibration and the coil temperature reaches to 100 ℃ in summer.

To solve these issues, we decide to adopt variable frequency technology to adjust the speed of condensing pump and change the Q-H curve of the pump. The pressure is reduced at the same flow, so that the inlet gate opens, eliminating damper loss.

1.2 Technology

We choose to use 1000kW/6kV medium voltage VFD produced by Beijing Leader Harvest Technology Co., Ltd. Its model is HARSVERT—A06/130, capacity 1350kVA,  ambience temperature 0 ℃-40 ℃.

                                                          Table 2   Parameters

Rated input voltage

Input frequency

Output frequency

Rated output current

Acceleration/Deceleration time

VFD Efficiency

6000V±10%

45-50Hz

0-50 Hz

130A

0.1-3000S

Rated load

>96%


1.3 Problems and Solutions

In order to reduce the cost of reformwe only change one of the two mutual-spare condensing pumps with variable frequency adjustment. Different adjustment modes makes different parameters between two pumps. So, there are following problems.


1The inlet gate opens when the pump runs in VFD mode. It makes the condensing water pressure lower by changing the pump speed to adjust water level of deaeratoreven not more than 1.6MPa. The water pressure declines with load reducing
can not work, so after canceling this logic we increase water pressure alarmthat is, “condensing water pressure less than 1.0MPa or more than 1.8MPa” alarm “ link start spare pump at low pressure ”.


2For VFD mode pump, condensation water pressure is low because of variable speed adjustment. But the constant speed pump is still adjusted by inlet gate whose water pressure is very high. In case of the variable frequency pump trips off, the pressure and flow increase suddenly when the spare pump starts, which will cause a big influence on the deaerator water level. For this issue, we change the control logic like this: when the VFD pump or its switch trips off &sends command of link start constant speed pumpthe
gram will sends a preset command to the inlet gate, shut down the inlet gate to a certain position immediately and program turns to “auto” to adjust deaerator water level.


3When the spare constant speed pump starts, pressure sudden-increase makes a big influence on other auxiliary equipmentsespecially to the system of mechanical seal cooling wateras its pressure should be less than 1.0Mpa. For this problem, we set a control logic which could prohibit closing adjustment gate when the pressure is too low or high, avoiding mechanical seal cooling water pressure too high caused by condensing water pressure sudden -increase. In normal operation, it adjusts automatically. At the same time, alarm “water pressure more than 0.8MPa or less than 0.5Mpa” is added.


4
, use their average to ensure the safety of automatic adjustment. The logic of water level signal is changed to “select two of three” when the water level is low, in order to prevent from pump mistake. When the VFD mode pump runs in auto mode, the inlet gate could be controlled manually in remotewhich increases the flexibility of the unit in startup, stop and low-load operation. "VFD starts failure" alarm is added. Alarm includes all alarms, for more details in DCS.


2
Condensing system safety test


1In order to confirm the influence of VFD pump trip-off and constant speed pump link-startwe make a load test for condensing pump before starting generator unit.

For VFD mode pump, condensing water pressure is 1.19Mpa, flow is 737t/hthe opening of the deaerator inlet gate is 88.9%. pump transfers to auto operationopening is 78.5% and pressure is 0.56Mpa. Load is set 150MW. Stop VFD pump and constant speed pump link starts. Close opening of the inlet gate to 18.7% and transfer it into“automatic”. Condensation water flow changes to 630t/h. Close the opening of mechanical seal cooling water gate to 22%. The minimum pressure can be down to 0.24Mpa, max can reach to1.2Mpa then settle to 0.4Mpa. The whole variety process is less than 30s. From the above test data we consider it can satisfy the basic operational requirements.


2Operating Parameters

                                          Table 3  Typical operating parameters

Load MW

Current

A

Speed

r/m

Flow

t/h

Condensation

Pressure

MPa

Cooling water

Opening

%

Cooling water pressure

MPa

Adjustment gate opening%

150

15

818

386

0.78

100

0.48

60.2

150

76

1490

397

3.05

49

0.66

32

200

23

926

497

0.98

100

0.60

57.6

200

81

1490

514

2.98

50

0.66

35.8

300

50.5

1188

743

1.53

75.2

0.66

47

300

92

1490

760

2.74

53

0.66

37.4

PSThe water in table is mechanical seal cooling water of feed pump.


Table 4  Vibration values

Measurement site

Upper bracket (µm)

Lower bracket (µm)

Speed(r/m)

Left

Left

Front

Right

Behind

600

54

38

54

38

20

18

20

19

780

136

75

135

70

35

20

30

20

810

56

51

56

51

39

35

39

35

900

64

44

65

54

16

18

19

17

1200

55

15

50

15

<20

<15

<20

<15

Vertical vibration is 15µm

3The economic effects comparison

To ensure the economy of the reformmake the power consumption test both in frequency adjustment and throttle adjustment for the same condensing pump in 300MW, 200MW, 150MW load.

 

                                          Table 5  Typical operating conditions comparison

Load MW

Flow t/h

Speed r/m

Current A

Power kW

Condensation Water Pressure

VS

CS

VS

CS

VS

CS

VS

CS

VS

CS

150

386

395

818

1490

15

75

173

804.5

0.78

3.05

200

497

511

926

1490

23

80

251.8

862.9

0.98

2.98

300

743

737

1188

1490

50.5

92

521

991.7

1.53

2.8

From above data, VFD could greatly reduce power consumptionespecially in low load(in 150MW, 631.5kW can be saved, in 300MW, 470.7kW can be saved). After the reformaccording to average load is 68.09%204.27MWand work time 7047h, 4306.4217MWh can be saved. Electrovalence is 0.32 yuan/kW.hso annual saving is 1378000yuan( USD 202647). Through calculating, single unit power consumption rate could be reduced 0.3%.


4
The operation after reform

The variable frequency pump works and constant speed pump is only for spare. In order to ensure the safety of pumps and other auxiliary equipmentswe make following measures:


1In general, variable frequency pump works and constant speed pump is only for spare. Opening of the inlet gate is between 80%—95%. Adjust the deaerator water level by VFD. Turn down the inlet gate in low load to keep the pressure not less than 1.1 Mpa and speed not lower than 900r/m. Ensurethe other equipments run safely.


2Make periodical test for constant speed pump and the test should not be less than 2h to ensure excellent status. Make switch test for consdensate pumps every month.


3When we switch VFD mode to constant speed modethe deaerator inlet gate transfers to “auto”. Accelerate VFD pump to rated speedand start constant speed pump, then stop the VFD pump after checking normally. When the constant speed pump is runningadjust the VFD pump runs in rated speed. Constant speed pump stops. Then adjust the speed of VFD pump until the inlet gate opens large. Switch off “auto adjustment” of inlet gate. VFD plunges to “auto adjustment”.


4When the unit starts or stops, adjust VFD speed in a certain value and adopt the inlet gate adjustmentwhich not only keeps the water level stable but also could make sure enough pressure cooling water for other auxiliary equipments. The VFD pump has a large vibration in 600—800r/m. It may be the critical speed areatherefore, the VFD pump is strictly prohibited to run in this area.


5
Conclusion

1The reform is safe and reliable. It reduces the vibration of condensing water pipeline and temperature of motor coil.

2The reform cancels throttle adjustment. Energy-saving for the condensing pump is obvious.

3Personnel must take care in checking , for maintenance and check of VFD.

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