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ME444 ENGINEERING PIPING SYSTEM DESIGN

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Presentation on theme: "ME444 ENGINEERING PIPING SYSTEM DESIGN"— Presentation transcript:

1 ME444 ENGINEERING PIPING SYSTEM DESIGN
CHAPTER 6 : PUMPS

2 LAST SESSION PIPING SYSTEM DESIGN PROCEDURE PIPE THICKNESS
PIPE SIZING AND SYSTEM PRESSURE DROP

3 CONTENTS Fundamental of Pumps Operating Point Pump Selection
Pump Installation

4 1. Fundamental of Pumps When source pressure is not enough to provide desired output, pump is utilized. SOURCE PIPING SYSTEM END USERS

5 Pump output Flow rate and Pressure rise. Flow rate

6 Pump

7 Pump input and output Output = Flow rate and Pressure rise. Flow rate
Input energy

8 Specific Speed

9 Pump performance Dynamic pump Positive displacement pump

10 Pump performance range

11 Performance curves = 0.57 (Ns = 1,550) = 3.66 (Ns = 10,000)

12 Steep vs. flat curves Flat curve for closed loop system with variable flow rate Steep curve for high head and constant flow rate

13 Affinity law Impeller Diameter Impeller Speed

14 Example of performance curves

15 Example of performance curves

16 Speed of induction motor
poles Synchronous speed (rpm) Possible Operating Speed (rpm) 2 3000 2850 4 1500 1425 6 1000 950 8 750 712 10 600 570

17 Standard motor size hp kW 1/8 0.09 1/6 0.12 1/4 0.18 1/3 0.25 1/2 0.37
3/4 0.55 1 0.75 1.5 1.1 2 2.5 1.85 3 2.2 hp kW 4 3 5.5 7.5 10 15 11 20 25 18.5 30 22 40 50 37 60 45

18 Effect of Fluid Viscosity

19 Net Positive Suction Head

20 Net Positive Suction Head Required
At low pressure, water can become vapor, causing cavitations. Suction pressure must be maintained above NPSHR to avoid cavitation

21 Net Positive Suction Head Available
MUST Maintain NPSHA > NPSHR z Suction lift Vapor pressure Pressure drop in suction piping

22 Patm vs Elevation

23 Example 6.1

24

25 2. Operating Point Pump performance curve Operating point
System pressure drop curve

26 Filling a tank from bottom
Pump performance curve

27 Filling a tank from bottom vs. from top
Which way fill faster?

28 Throttling the discharge valve
Throttled valve Fully open valve Pump performance curve

29 Variable speed drive vs. valve throttling
Feedback signal Throttled valve Fully open valve Pump performance curve N1 Pump performance curve N2

30 VSD for pressure control
signal Valve 1 and 2 open All valve open Pressure set point Pump performance curve N1 Pump performance curve N2

31 Limitation of VSD Feedback signal System curve Cannot reduce speed

32 Parallel and Serial Connection
Do not exceed Maximum Allowable Working Pressure (MAWP)

33 Response to Parallel Connection

34 Parallel Connection of Pumps with Different Size

35 Utilization of Pressure Tank
Pressure Switch Pressure Tank Air Water Pressure in tank Pump operate Pump stop time

36 Example 6.2

37 Example 6.2

38 Example 6.2

39 Example 6.2

40 Example 6.2

41 3. Pump Selection Best Efficiency
Energy cost is far beyond the pump cost

42 Pump Specification

43 Pump Nameplate

44 IP RATING The IP Code, International Protection Marking, IEC standard 60529, sometimes interpreted as Ingress Protection

45 Example 6.3 Select the suitable pump for Example 5.1
m.WG.

46 Example 6.3 (2) Possible selections: NM12 and NM25/20 50.85 m 200 lpm

47 Example 6.3 (2) Select NM12: Trim Diameter to 198 mm

48 Note: follow standard motor size
Example 6.3 (3) Select NM12: Trim Diameter to 198 mm Pump has efficiency of 49.5% Power consumption 3.2 kW Max power consumption 4kW Select Motor size: 5.5kW Note: follow standard motor size

49 Example 6.3 (4) hp kW 1/8 0.09 1/6 0.12 1/4 0.18 1/3 0.25 1/2 0.37 3/4 0.55 1 0.75 1.5 1.1 2 2.5 1.85 3 2.2 hp kW 4 3 5.5 7.5 10 15 11 20 25 18.5 30 22 40 50 37 60 45

50 Example 6.3 (5) Dimension of NM12

51 Example 6.4 Back to example 5.3, if two identical pump of the following curve is installed, predict the operating point.

52 Example 6.4 (2) 23.1m.WG. = 21.6m.WG  Variable with flow rate
+ 1.5 m. WG. Elevation  Constant

53 Example 6.4 (3) 2 pumps in parallel Single pump

54 3. Pump Installation

55 Typical Installation

56

57 Suction Lift More suction lift = Less NPSHA  Cavitation
5 Meter lift is the maximum possible value Foot Valve Submersible pump

58 Priming

59 Self Priming Pump

60 Pumping from Tank Vent Mak-up Overflow Drain Vortex prevention plate

61 Eccentric Reducer CORRECT INCORRECT

62 Installation photos

63 Installation photos

64 Pump Seal

65 Packing Seal

66 Mechanical Seal

67 Homework Exercise 6.1 and 6.2

68 Case Study


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