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VACUUM PAN MECHANICAL CIRCULATOR SYSTEMS

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Mechanical Pan Stirrers

Mechanical circulators are installed in vacuum pans in order to reduce the boiling time. But published data from Huletts Refinery in Durban has shown a reduction in sugar color and an increase in pan yield as a result of the use of a pan stirrer.

Hugot quotes Webre in stating advantages of pan stirrers as follows

  • Saving in time for the strike.
  • Maximum temperature reached by the massecuite substantially lowers.
  • Crystals better formed, more shapely and more regular.
  • Less color in the sugar and reduced risk of sugar losses by local overheating.
  • Possible ready application of automatic feed controlled by the power consumption of the motor; when power increases, the feed valve is opened; when it decreases the valve is closed
  • Possibility of feeding the pan with syrup and molasses only slightly under saturated without risk of re-melting crystal.
  • Less deposit on the tubes, due to the abrasion effect by friction of the circulating crystals

Design Specification

The stirrer shall be vertical top suspended type. The stirrer shaft shall be supported by bearings mounted inside the gearbox casing. The stirrer gearbox shall be supported on the pan itself. The pan shall be designed to carry the weight and live loads imposed on it by the stirrer.
If a bearing is required at the bottom of the shaft, it shall be lubricated by massecuite. The bearing housing shall be so designed that the bearing can be removed and replaced from the outside of the pan.

The material of construction of shaft and impeller shall be the same as that of the pan in which it is mounted, except that above the pan strike level the shaft may be of carbon steel. A rigid flanged coupling shall be used to join the carbon steel part to the stainless steel part of the shaft.

The shaft shall be coupled to the gearbox by means of a hollow shaft coupling. The gearbox shall have an American Gearbox Manufacturers Association (AGMA) service factor of no less than 1.5.

A gland or seal shall be provided to prevent air from passing between the shaft and the pan shell in to the pan body. This seal may be of the packed gland type.

Depending on the stirrer design baffles may be provided to reduce the circumferential velocity of massecuite in the pan downtake.

The critical speed of the shaft and impeller shall be no less than 120% of the maximum shaft speed. The impeller blade tip clearance shall be no less than 5% of the impeller diameter. The blade tip speed shall not exceed 10 m/s.

The stirrer shall be supplied with either

  • a two speed motor, with the appropriate switch gear to change from high speed to low speed operation, or
  • a single speed motor and AC variable speed direct torque control drive

Two-Speed Motor

If a two speed motor is supplied the motor shall be wound such that the full load torque at the low speed is equal to full load torque at the high speed. Belts and pulleys shall be used to transmit power from the motor to the input of the gearbox.

The motor shall run at the high speed for as long as possible. When the motor current drawn reaches the rated full-load current the switchgear must change the motor from the high-speed windings to the low speed windings. The motor must continue to run at the low speed until the motor current drawn reaches the rated full load current for the low speed windings, at which point the motor must trip, an audible and visible alarm shall be given in the pan floor control room.

Direct Torque Control Variable Speed Drive

If a variable speed direct torque control drive is supplied the motor shall be flange mounted on to the gearbox.

The drive shall be programmed to run at the fastest speed possible while keeping within the motor's allowable power and torque capabilities. If the massecuite viscosity increases, the drive must sense the increase in required torque and slow down the motor to prevent any component from being overloaded. If the massecuite viscosity increases to a point where the drive is running at the lowest speed allowable, for motor cooling, then the drive must trip; an audible and visible alarm shall be given in the pan floor control room.

Stirrer Efficiency

Since

  • the impeller is required to operate over a range of speeds, and
  • it is expected the stirrer will run at the higher speeds for most of the duration of a boil, and
  • the maximum efficiency can only occur at one speed, therefore
  • the impeller shall be designed to have the maximum efficiency at the higher speeds.

Pan Stirrer Power Consumption

As can be seen from the specification above the power absorbed by the stirrer increases as the boil progresses. This is because the viscosity of the massecuite increases as the brix increases. The graph below shows the variation of motor power with boil time for a stirrer fitted with a two-speed motor.


Stirrer Power
An extract from the ABB two-speed motor catalog is given below

 

Current

Torque

Frame Size

Speed [rpm]

Power [kW]

Efficiency [%]

Power Factor

Ifl [amps]

Is/Ifl

Tfl [Nm]

Ts/Tfl

Tmax/Tfl

160M

1465

7.5

85.5

0.83

15.5

7.1

49

2.1

2.7

965

5.5

80.5

0.77

13.0

4.7

54

1.8

1.9

160L

1465

11.5

86.5

0.84

23.0

7.0

75

2.1

2.7

965

8.5

82.5

0.76

19.5

4.9

84

1.8

2.0

180M

1475

13

88.0

0.82

26.0

6.5

84

1.9

2.6

975

8

82.5

0.75

19.0

4.3

78

1.4

1.8

180L

1475

15

88.5

0.83

30.0

7.1

97

2.3

2.7

975

10

84.0

0.74

24.0

4.4

97

1.5

1.9

200MLA

1475

18

88.5

0.91

33.0

7.6

117

2.1

2.5

985

12

86.0

0.86

24.0

7.8

116

2.6

2.6

200MLB

1475

22

89.5

0.89

40.0

8.2

142

2.4

2.8

985

14.7

86.5

0.87

29.0

7.6

143

2.6

2.5

200MLC

1475

25

89.0

0.87

47.0

7.7

162

2.3

2.6

980

16.7

85.5

0.88

32.0

6.7

162

2.3

2.2

225SMB

1480

32

90.0

0.88

58.0

8.6

206

2.3

2.8

985

21

89.5

0.86

40.0

8.0

204

2.4

2.7

225SMC

1480

36

90.5

0.88

69.0

8.4

232

2.2

2.8

985

24

90.0

0.87

45.0

7.4

233

2.2

2.5

250SMB

1475

50

92.5

0.89

89.0

7.5

324

2.3

2.6

985

32

90.5

0.80

65.0

7.1

310

3.1

2.6

280SMB

1485

65

93.0

0.87

117.0

6.5

418

2.0

2.4

988

43

92.0

0.79

86.0

6.7

417

2.9

2.3

280SMC

1486

76

93.7

0.87

136.0

7.2

488

2.3

2.7

989

50

92.6

0.78

101.0

7.4

483

3.4

2.5

315SMB

1485

90

93.6

0.87

160.0

6.0

579

1.6

2.4

990

60

94.0

0.77

119.0

6.7

579

3.3

2.9

315SMC

1485

110

93.8

0.87

195.0

5.6

707

1.6

2.3

89

75

94.0

0.79

146.0

6.1

724

2.9

2.5

315MLA

1488

140

94.5

0.87

250.0

6.6

900

2.0

2.8

989

95

94.2

0.79

185.0

6.5

917

3.1

2.5

355S

1486

135

94.0

0.88

235.0

6.9

868

1.4

3.0

991

90

93.5

0.80

175.0

7.4

867

1.9

3.2

355SMA

1490

200

95.0

0.87

350.0

8.5

1282

1.5

3.7

991

130

94.5

0.79

255.0

7.8

1253

2.0

3.3


 

 

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