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Incompressible Fluid Flow. References Required Principles of Naval Engineering – (pg. 35-59) Optional Introduction to Naval Engineering – (pg. 19-22 &

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Presentation on theme: "Incompressible Fluid Flow. References Required Principles of Naval Engineering – (pg. 35-59) Optional Introduction to Naval Engineering – (pg. 19-22 &"— Presentation transcript:

1 Incompressible Fluid Flow

2 References Required Principles of Naval Engineering – (pg. 35-59) Optional Introduction to Naval Engineering – (pg. 19-22 & 477-501)

3 Objectives – Comprehend the various forms of head to fluid dynamics. – Apply Pascal’s Principle, the principle of Conservation of Mass, and Bernoulli’s Equation to fluid dynamics. – Comprehend the modes of fluid flow including the factors determining the mode, the associated velocity/temperature profiles, the effects on heat transfer rates, and the desirable qualities of each.

4 Objectives – Comprehend the operation and application of various pumps found in the propulsion plant. – Comprehend the operation and application of centrifugal and axial fans. – Comprehend the basic construction and application of valves used in the propulsion plant including methods for operating remotely. – Know the schematic representations for valves and pumps used in the propulsion plant. – Comprehend the principles of operation of various heat exchangers and their classification.

5 Pascal’s Principle The force applied to a column of liquid is transmitted equally and undiminished in all directions through the liquid and to the walls of its container. Find F 2

6 Head (Pressure) Head is a surrogate term for pressure The height of a column of flowing fluid that a given pressure can support Three types – Static Head – Velocity Head – Friction Head

7 Static Head Head – The pressure exerted by a column of fluid

8 Velocity Head

9 Friction Head The pressure necessary to overcome friction Also referred to as Head Loss What are the sources of friction in a piping system?

10 Friction Head

11

12 Fluid Flow Profiles Fluid flow in piping is affected by: – Piping diameter – Fluid viscosity – Fluid velocity – Relative piping roughness Fluid flows in two broad categories – Laminar – Turbulent

13 Flow Regimes Laminar Flow Streamline or viscous flow Layers of fluid flow over one another with virtually no mixing Fluid particles move in definite and observable paths Parabolic flow profile Turbulent Flow Irregular particle movement No observable paths or layers Relatively flat profile

14 Conservation of Mass

15 The nozzle of a fire hose contracts from 2.5” in diameter to 0.5” in diameter. On average, the water traveling in the hose moves at 10 ft/sec. Find the exit velocity of the water. D2D2 D1D1 V1V1 V2V2

16 Bernoulli’s Equation Velocity head static head Pressure head

17 Valves devices which control the amount and direction of fluid flow in piping systems Material is dictated by the system conditions: – High Pressure/Temperature Applications: Steel Alloys – Low Pressure/Temperature Applications: Bronze, Brass

18 Globe Valve Inlet Outlet Hand Wheel Packing Gland Nut Stem Packing Gland Follower Body Disc Seat Bonnet

19 Types of Valves Two basic groups: – Stop valves - used to shut off or partially shut off the flow of fluid ( ex: globe, gate, plug, needle, butterfly) – Check Valves - used to permit flow in only one direction (ex: ball-check, swing-check, lift-check) Special types: – Relief valves – Pressure-reducing valves – Remote-operated valves

20 Globe Valve Inlet Outlet Hand Wheel Packing Gland Nut Stem Packing Gland Follower Body Disc Seat Bonnet

21 Globe Valve http://www.youtube.com/watch? v=yTr4kpkHovg

22 Globe Valves – Most common type of stop valve – Used in steam, air, water, & oil lines – Disc attached to valve stem rests against seat to shut off flow of fluid – Adv: Good throttling (flow control) characteristics – Disadv: high head loss (flow resistance)

23 Gate Valve Inlet Outlet Body Hand Wheel Disc Stem Bonnet Packing Gland Nut Packing Gland Follower

24 Gate Valve – Used when there must be straight-line flow of fluid w/ min. resistance – Gate usually wedge-shaped or a vertical disc – Adv: minimal head loss when open, excellent stop valve – Disadv: poor throttling characteristics, difficult to open against a large differential pressure Two types: – Rising Stem – Non-rising Stem

25 Butterfly Valve Ball Valve

26 Butterfly Valves – Used in water, fuel, and ventilation systems – Adv: light-weight, & quick-acting, low head loss – Disadv: poor throttling, poor seating characteristics

27 Ball Valves – Similar to butterfly valves – Normally found in seawater, sanitary, and hydraulic systems – Adv: excellent seating characteristics – Disavd: zero throttling

28 Check Valves Controls direction of flow Operated by flow of fluid in pipe Types: – Swing check - disc moves through an arc – Lift check - disc moves up and down – Ball check - ball is located at end of stem and lifts to allow flow

29 Swing-check Valve

30 Lift Check Valve

31 Ball Check Valve

32 Relief Valves Used to protect piping system from excessive pressure Opens automatically when fluid pressure becomes too high (pressure acts against spring pressure) Relieving pressure set by an adjusting screw

33 Pressure-reducing Valves Used to automatically provide a steady, lower pressure to a system from a higher pressure source Used in air, lube-oil, seawater, and other systems

34 Remote-operated Valves Valves that allow operation from distant stations Types: – Mechanical - uses reach rods and gears – Hydraulic - uses fluid and piston set up – Motor - uses and electric or pneumatic motor – Solenoid - uses coil and core mechanism to open or close on an electric signal

35 Remote Operators Mechanical

36 Remote Operators Hydraulic

37 Remote Operators Motor

38 Remote Operators Solenoid

39 Heat Exchangers(HX) Definition: and device designed to allow the flow of thermal energy (heat) from one fluid to another Ships (and life in general) are filled with heat exchangers. Examples?? Heat Exchangers are classified by: – Relative direction of fluid flow – Number of passes – Construction (shell and tube) – Type of tube (U-tube)

40 Heat Exchangers(HX) Relative direction of fluid flow Number of passes Construction (shell and tube) Type of tube (U-tube)

41 Heat Exchangers(HX) Relative direction of fluid flow Number of passes Construction (shell and tube) Type of tube (U-tube)

42 Heat Exchangers(HX) Relative direction of fluid flow Number of passes Construction (shell and tube) Type of tube (U-tube)

43 Heat Exchangers(HX) Relative direction of fluid flow Number of passes Construction (shell and tube) Type of tube (U-tube)

44 Heat Transfer Recall: In order to analyze the effects of soot/scale on heat transfer, it is necessary to think about the heat transfer across each layer Every layer has it’s own heat transfer coefficient and thickness.

45 Pumps

46 Device that adds energy to a fluid in order to: – Supply pressure head – Overcome head loss – Provide sufficient flow – Raise the height of the fluid Accomplished by – Pushing – Pulling – Throwing – Combination of the three

47 Components of Pumps Drive mechanism (steam, electric, gear) Pump shaft Impeller or piston Casing

48 Positive Displacement Pump

49 Used in systems that employ a viscous working substance (like oil) or high pressure applications such as lubrication/hydraulic systems Advantage: constant discharge volume, self priming Disadvantage: pulsating discharge, lower flow rates compared to centrifugal pumps

50 Pumps Non-positive Displacement: volume of fluid is dependent on static head/pressure – Centrifugal: impeller inside a case (called volute). Impeller is a disc w/ curved vanes mounted radially (like a paddle wheel) Suction is the Eye -> fluid accelerated as it travels outward & then enters volute – Propeller: uses prop inside casing to move fluid -> not used much in Navy

51 Centrifugal Pump

52

53 Pumps Jet pumps: – Bernoulli’s principle and no moving parts – Velocity Head vs. Pressure head h in + v in 2 /2 = h out + v out 2 /2

54 Pump Characteristic Curves Pump Parameters: – N = pump speed, RPM – V = volumetric flow rate, GPM – H p = pump head (discharge pressure), psig – P = power required, Hp Centrifugal Pump Laws – V  N – H p  N 2 – W  N 3

55 Positive Displacement Pumps HpHp GPM N1N1 N2N2 N 2 = ____

56 Centrifugal Pumps

57 Series pumps (called staging) HpHp GPM V 2 = ____ H p2 = ____ 2 Pumps 1 Pump

58 Net Positive Suction Head Def’n: that pressure required at the suction of a pump to prevent cavitation So what is cavitation? - the formation of bubbles due to low pressure area and the subsequent collapse upon migration to a high pressure area Cavitation causes noise and damage

59 Net Positive Suction Head Need enough pressure on the suction side so that the pump does not reduce pressure @ the eye to cause P < P sat If P < P sat, water flashes to vapor causing damage to the pump What are possible means of providing NPSH to prevent cavitation?

60 Take Aways Describe the two basic groups of valves. Give examples of each and any associated advantages/disadvantages Properly label a drawing of a globe/gate valve indicating the following: - Valve body- Packing - Disc- Packing gland/nut - Seat- Stem - Bonnet- Hand wheel Describe the purpose of a relief valve and pressure reducing valve Describe the various methods of remotely operating valves Describe the purpose of a pump. Describe the types of pumps covered in lecture (positive displacement, centrifugal, jet pump).

61 Take Aways Describe how volumetric flow rate, pump head and power vary with pump speed Describe how the above parameters are affected by various pump combinations (series, parallel operation) List and describe the two types of fans. Apply Pascal’s Principle to specific situations Apply Bernoulli’s Equation to specific situations.

62 Homework 1.10 1.16 1.17 2.1 2.9

63 Questions? Questions?


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