-
E-mail
815510555@qq.com
- Phone
-
Address
No. 3566 Jiasong Middle Road, Qingpu District, Shanghai
Shanghai Jiaquan Pump Industry Co., Ltd
815510555@qq.com
No. 3566 Jiasong Middle Road, Qingpu District, Shanghai
IH type chemical pump | stainless steel centrifugal pump-brief introduction
IH type chemical pumpIt is a single-stage single suction cantilever centrifugal pump, with rated performance points and dimensions equivalent to the international standard ISO2858-1975 (E). It is an energy-saving product used to replace F-type corrosion-resistant pumps and is suitable for conveying corrosive media with temperatures ranging from -20 ℃ to 105 ℃ or media with physical and chemical properties similar to water in the chemical, petroleum, metallurgical, power station, food, pharmaceutical, synthetic fiber and other sectors.
Performance range of IH type chemical pump (according to design points)
Flow rate Q: 6.3-400 m ³/h
Head H: 5-125m
The working design pressure of the pump is 1.6MPa
Users can choose different materials for the main components of the pump's overcurrent section based on the corrosiveness level of the conveyed medium. There are five types of materials and their codes for the main components of the overcurrent part of the pump:
IH type chemical pumpThe temperature of the conveying medium ranges from -20 ℃ to 105 ℃. If necessary, a double end sealed cooling device can be used to transport the medium at a temperature of 20 ℃ to+280 ℃. Suitable for industries such as chemical, petroleum, metallurgy, power, papermaking, food, pharmaceuticals, environmental protection, wastewater treatment, and synthetic fibers for transporting various corrosive or non polluting media similar to water.
IH type chemical pump-Performance range: Traffic Q: 6.3-400m3/Head H: 5-132m Speed n: 2900, 1450r/min with power: 0.55~110KW Imported diameter: 50-200mm Working pressure: 1.6Mpa IH type chemical pumpThere are 29 basic types, of which 22 dual speed (2900, 1450r/min) have been modified by cutting the impeller diameter of two types A and B, reaching 112 specifications.
Pump structure:
The structural characteristics of the pump:
Pump shaft seal type: |
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IH type chemical pump | stainless steel centrifugal pump-working conditions
Flow Q: 6.3-400m3/h Rotation N: 2900-1450r/min Caliber DN: 50-200mm
Head H: 5-125m with power: 0.55-90kw Working pressure P: 1.6Mpa
IH type chemical pump | stainless steel centrifugal pump-Model Meaningjustice
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For example: IH50-32-160 |
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IH type chemical pump
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model
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rotational speed
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Traffic (m)3/h)
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Flow rate (L/S)
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lift
(m)
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efficiency
(%)
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shaft power
(Kw)
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Equipped with power
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Cavitation allowance (m)
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weight
(kg)
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Medium density
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1.0
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1.35
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1.85
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IH50-32-125
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2900
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12.5
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3.47
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20
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51
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1.33
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2.2
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6.0
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4.0
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2.0
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45
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1450
|
6.3
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1.74
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5.0
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45
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0.19
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0.55
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0.55
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0.55
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2.0
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45
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IH50-32-160
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2900
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12.5
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3.47
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32
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46
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2.37
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3.0
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4.0
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5.5
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2.0
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49
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1450
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6.3
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1.74
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8.0
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40
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0.34
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0.55
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0.75
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1.1
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2.0
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49
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IH50-32-200
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2900
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12.5
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3.47
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50
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39
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4.36
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5.5
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7.5
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11
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2.0
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59
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1450
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6.3
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1.74
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12.5
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33
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0.65
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1.1
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1.1
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1.5
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2.0
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59
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IH50-32-250
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2900
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12.5
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3.47
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80
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33
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8.25
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11
|
15
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18.5
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2.0
|
93
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1450
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6.3
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1.74
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20
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27
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1.27
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2.2
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2.2
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3.0
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2.0
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93
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IH65-50-125
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2900
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25
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1.53
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2.0
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62
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2.2
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3.0
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4.0
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5.5
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2.0
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47
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1450
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12.5
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6.94
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5.0
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55
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0.31
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0.55
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0.55
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0.75
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2.0
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47
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IH65-50-160
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2900
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25
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2.78
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32
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57
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3.82
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5.5
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7.5
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11
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2.0
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53
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1450
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12.5
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6.94
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8.0
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51
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0.53
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0.75
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1.1
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1.5
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2.0
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53
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IH65-40-200
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2900
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25
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2.92
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50
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52
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6.55
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11
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11
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15
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2.0
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63
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1450
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12.5
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6.94
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12.5
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46
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0.93
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1.5
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2.2
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2.2
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2.0
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63
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IH65-40-250
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2900
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25
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2.92
|
80
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46
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46
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15
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3.0
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30
|
2.0
|
99
|
|
1450
|
12.5
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6.94
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20
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39
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39
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2.2
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37
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4.0
|
2.0
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99
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IH65-40-315
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2900
|
25
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3.06
|
125
|
39
|
39
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30
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5.5
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55
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2.0
|
116
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1450
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12.5
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6.94
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32.0
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33
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33
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5.5
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5.5
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7.5
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2.0
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116
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IH80-65-125
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2900
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50
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13.9
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20
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69
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3.95
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5.5
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7.5
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11
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3.0
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52
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1450
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25
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6.94
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5.0
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64
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0.53
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0.75
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1.1
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1.5
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2.5
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52
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IH80-65-160
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2900
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50
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13.9
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32
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67
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6.5
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11
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11
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15
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2.3
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57
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1450
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25
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6.94
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8.0
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62
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0.88
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1.5 |
1.5
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2.2
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2.3
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57
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IH80-50-200
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2900
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50
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13.9
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50
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63
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10.8
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15
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18.5
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30
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2.5
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65
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1450
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25
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6.94
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12.5
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54
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0.83
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1.1
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1.5
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2.2
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2.0
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65
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IH80-50-250
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2900
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50
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13.9
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80
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58
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18.8
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30
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37
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45
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2.5
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103
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|
1450
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25
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6.94
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20
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52
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2.62
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4.0
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5.5
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7.5
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2.0
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103
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IH80-50-315
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2900
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50
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13.9
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125
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52
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32.73
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45
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55
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75
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2.0
|
121
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1450
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25
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6.94
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32
|
48
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4.54
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7.5
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7.5
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11
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2.0
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121
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IH100-80-125
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2900
|
100
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27.8
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20
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73
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7.47
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11
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15
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18.5
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4.5
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57
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1450
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50
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13.9
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5.0
|
68
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1.0
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1.5
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2.2
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3.0
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3.5
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57
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IH100-80-160
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2900
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100
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27.8
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32
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73
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11.9
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15
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22
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30
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4.3
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87
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1450
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50
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13.9
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8.0
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69
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1.58
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2.2
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3.0
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4.0
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3.4
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87
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IH100-65-200
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2900
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100
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27.8
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50
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72
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18.9
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30
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37
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45
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3.9
|
96
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1450
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50
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13.9
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12.5
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68
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2.5
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3.0
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4.0
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5.5
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2.5
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96
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IH100-65-250
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2900
|
100
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27.8
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80
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68
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32.0
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45
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55
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75
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3.6
|
115
|
|
1450
|
50
|
13.9
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20
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63
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4.3
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5.5
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7.5
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11
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2.5
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115
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IH100-65-315
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2900
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100
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55.6
|
125
|
62
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54.9
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75
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90
|
132
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3.2
|
166
|
|
1450
|
50
|
27.8
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32
|
58
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7.5
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11
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15
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18.5
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2.0
|
166
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|
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IH125-100-200
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2900
|
200
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55.6
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50
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77
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35.4
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45
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55
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90
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5.0
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99
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1450
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100
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27.8
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12.5
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73
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4.66
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7.5
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11
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15
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2.9
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99
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IH125-100-250
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2900
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200
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55.6 |
80
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75
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58.1
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11
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110
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132
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4.5
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151
|
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1450
|
100
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27.8
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20
|
72
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7.56
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132
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15
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18.5
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2.3
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151
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IH125-100-315
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2900
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200
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55.6
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125
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72
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94.56
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18.5
|
160
|
220
|
4.5
|
166
|
|
1450
|
100
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27.8
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32
|
65
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13.41
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18.5
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22
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30
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2.8
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166
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|
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IH125-100-400
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1450
|
100
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27.8
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50
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55
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14.74
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18.5
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30
|
37
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2.5
|
211
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IH50-125-250
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1450
|
200
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55.6
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20
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77
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14.1
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30
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30
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37
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2.5
|
165
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IH50-125-315
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1450
|
200
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55.6
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32
|
75
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23.2
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30
|
37
|
55
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2.8
|
196
|
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IH50-125-400
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1450
|
200
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55.6
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50
|
70
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38.9
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55
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75
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90
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2.8
|
238
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IH200-150-250
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1450
|
400
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111.1
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20
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77
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28.3
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37
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55
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75
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2.5
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195
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IH200-150-315
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1450
|
400
|
111
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32
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79
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44.1
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55
|
75
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110
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4.0
|
269
|
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IH200-150-400
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1450
|
400
|
111
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50
|
78
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39.8
|
90
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132
|
160
|
3.5
|
290
|
model
IH typeStainless steel chemical centrifugal pump(Disassembly and assembly, starting, running, and stopping)
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Disassembly and assembly
disassemble:
Due to the use of an extended coupling, there is no need to disassemble the inlet and outlet pipelines, pump body, and motor when disassembling the pump. Only the middle coupling in the extended coupling needs to be removed to disassemble the rotor components for repair and maintenance.
1. Remove the drain pipe plug on the pump body and the drain pipe plug on the suspension body, and drain the liquid inside the pump and the lubricating oil inside the suspension body. (Note: If there are additional pipelines on the pump, they should also be removed).
2. Disconnect the connection between the pump body and the intermediate bracket, and remove all rotor components such as the intermediate bracket, suspension components, and pump cover from the pump body together.
3. Remove the impeller nut, remove the impeller and key.
4. Remove the pump cover, coaxial sleeve, mechanical seal end cover, and mechanical seal from the shaft together. Be careful not to slide the shaft sleeve relative to the pump cover, and then remove the mechanical seal end cover. Remove the mechanical seal together with the shaft sleeve, and then disassemble the shaft sleeve and mechanical seal.
If the seal uses packing, the shaft sleeve can be directly removed from the pump cover, and then the packing cover, packing, and packing ring can be removed in sequence.
If the seal adopts a special structure, attention should be paid to different disassembly methods.
5. Remove the middle bracket and suspension bracket.
6. Remove the pump coupling and key.
7. Remove the dust discs at both ends of the suspension body and the front and rear covers of the bearings, and then remove the shaft and bearings from the suspension body together.
8. Remove the bearing from the pump shaft.
assemble
Reverse the disassembly procedure.
Start, Run, and Stop
1. Preparation before starting
1) Before starting, clean the pump and the site thoroughly.
2) Check if the lubricating oil level inside the bracket is appropriate (the oil level is about 2mm from the centerline of the oil level gauge) and if the oil level gauge is intact.
3) Before connecting the coupling, check the direction of the prime mover and align it with the pump's direction arrow before connecting the coupling.
4) After installing the mechanical seal or packing and coupling, the pump shaft can be manually rotated without any rubbing, and the protective cover of the coupling should be installed properly.
5) When using the pump with suction, it should be filled or evacuated before starting; When using the pump in reverse flow, fill the pump with the conveyed liquid before starting, remove the air from the pump, and then close the gate valve of the discharge pipe.
6) Before starting, check if the basic screws are loose. Whether the gland is skewed, and the supply of lubricating oil and cooling water.
2. Start up
1) Close the inlet and outlet pressure (or vacuum) gauges and outlet valves (if there is a bypass pipe, it should also be closed at this time). Start the motor (first jog and confirm that the pump direction is correct before starting formal operation), then open the inlet and outlet pressure (or vacuum) gauges. When the pump reaches normal speed and the instrument indicates the corresponding pressure, slowly open the outlet valve and adjust it to the required working condition. When the discharge pipeline is closed, the continuous working time of the pump cannot exceed 3 minutes.
2) During the starting process, attention should be paid to the power reading of the prime mover and the vibration of the pump at all times. The vibration number should not exceed 0.06 millimeters, and the measuring part is the bearing seat.
3) Sealing condition: The mechanical seal should have no leakage or heating phenomenon, and the packing seal should be in a continuous dripping state.
3. Run
1) Regularly check the heating condition of the pump and motor (the temperature rise of the bearings should not exceed 75 ℃) and the oil supply of the oil level gauge. Generally, after every 1500 hours of operation, all lubricating oil should be replaced.
2) Do not use suction valves to regulate flow to avoid cavitation.
3) Pumps should not operate continuously at flow rates below 30%. If continuous operation is necessary under these conditions, a bypass pipe should be installed at the outlet to discharge excess flow.
4) Pay attention to whether there is any noise during the operation of the pump. If any abnormal state is found, it should be eliminated or stopped for inspection in a timely manner.
4. Stop
1) Slowly close the gate valve of the discharge pipeline (if the pump is used in reverse flow, also close the gate valve of the suction pipeline), and turn off the switches of various instruments.
2) Cut off the power supply
3) If external drainage is used for sealing, the external drainage valve should also be closed.
4) If the ambient temperature is below the freezing point of the liquid, the liquid in the pump should be drained to prevent freezing and cracking.
5) If parked for a long time without use, in addition to draining the corrosive liquid inside the pump, all components should be disassembled and cleaned, especially the sealing chamber. The pump should be disassembled, cleaned, and reinstalled. In addition to applying oil and rust prevention treatment and sealing the pump inlet and outlet, regular inspections should also be conducted
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precautions
Malfunctions and troubleshooting
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Possible causes of the malfunction |
The pump cannot output liquid |
Insufficient flow and head |
Excessive power consumption |
Generate vibration and noise |
Excessive leakage at the sealing point |
Heat generation of shaft seal (including packing box) |
The pump heats up excessively and cannot rotate |
Bearing heating and bearing wear |
Elimination methods |
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There is air left inside the pump or suction pipe |
0 |
0 |
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0 |
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Recharge the pump to remove air |
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Excessive suction head or insufficient injection height |
0 |
0 |
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0 |
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Lower the pump position and increase the pressure at the inlet |
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The suction pipe passes through small or debris filled plugs |
0 |
0 |
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0 |
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Increase the suction pipe diameter and remove the # plug |
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Insufficient immersion depth or air leakage of the suction pipe |
0 |
0 |
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Increase immersion depth or inspect pipelines |
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Speed too high or too low |
0 |
0 |
0 |
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Check the speed of the prime mover as required by regulations |
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Pump direction is incorrect |
0 |
0 |
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Adjust steering |
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The total head does not match the pump head |
0 |
0 |
0 |
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Reduce the resistance or height of the vomiting system |
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The density and viscosity of the medium do not meet the requirements of the fruit |
0 |
0 |
0 |
|
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Conversion should be performed |
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Vibration occurs during operation when the flow rate is too low |
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|
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0 |
0 |
|
0 |
0 |
Increase the flow rate or install a bypass circulation pipe |
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Inconsistent axis between pump and motor or bent shaft |
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0 |
0 |
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0 |
0 |
0 |
correct |
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There is friction between the rotating part and the fixed part |
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0 |
0 |
|
|
0 |
0 |
Repair the pump or improve its use working condition |
|
Severe wear or damage to bearings |
|
|
|
0 |
|
0 |
0 |
0 |
Replace it |
|
Excessive wear of the sealing ring |
|
0 |
0 |
|
|
|
|
|
Replace it |
|
Excessive wear of shaft sleeve, packing or dynamic and static plutonium |
|
|
0 |
|
0 |
0 |
0 |
|
Replace it |
|
Improper selection or installation of fillers (or mechanical seals) |
|
|
0 |
|
0 |
0 |
0 |
|
Re select or install according to usage requirements |
|
Unbalanced rotating parts cause vibration |
|
|
|
0 |
0 |
0 |
0 |
0 |
Check the cause and try to eliminate it |
|
Excessive oil volume in the oil chamber (or dirty oil) |
|
|
0 |
0 |
|
|
|
0 |
Add oil according to the oil level requirements or replace with new oil |
|
There is something inside the pipeline or pump Blockage caused by debris |
0 |
0 |
|
0 |
|
|
|
|
Check and eliminate |
|
Improper sealing fluid pressure |
|
|
|
|
0 |
0 |
|
|
The pressure before sealing the chamber should be increased by 0.049~0.147MPa |
|
The packing gland is too tight or too loose |
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|
0 |
|
0 |
0 |
|
|
Adjust appropriately |