experiment 3 minor losses in pipes

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Experiment 3 Minor Losses in Pipes Lecturer: Laith Hamdan اد اعدسي التدري : ليث حمدانتعليم وزارةاللعالي ا والبحثعلمي اللجامعة ا المستنصريةية الهندسة كل قسم هندسة البيئةMinistry of Higher Education and Scientific Research Al-Mustansiriayah University College of Engineering Environmental Engineering Department

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Experiment 3

Minor Losses in Pipes

Lecturer: Laith Hamdan

: ليث حمدان التدريسياعداد

العلمي والبحث العالي وزارةالتعليم

المستنصرية الجامعة

كلية الهندسة البيئة هندسة قسم

Ministry of Higher Education and

Scientific Research

Al-Mustansiriayah University

College of Engineering

Environmental Engineering

Department

Objectives:

The goal of this laboratory is to study pressure losses due to viscous

(frictional) effects in fluid flows through pipes. These pressure losses are

a function of various geometric and flow parameters including pipe

diameter, length, internal surface roughness and type of fitting. In this

experiment, the influence of some these parameters on pressure losses in

pipe flows will be evaluated by measuring flow rates through different

types of pipes.

Equipments and apparatus:

The following apparatus will be used for this experiment:

1. The pipe flow rig with pipes of different diameters and lengths.

2. A large graduated cylinder used to measure the volume of water

flowing out of the system.

3. A stop watch used to measure the time required to collect the

water.

4. A pump for refilling the water reservoir.

Experimental Procedure

1. Measure and record the heights of the base of the reservoir and the

center of the pipes in the table in the data sheet.

2. Start with the reservoir filled to the highest level indicated in the

data sheet for the pipe you are examining.

3. Record the exact, initial height of water in the reservoir.

4. Ensure that all manual valves to all the pipes are closed.

5. Place a graduated cylinder at the exit of the pipe you are

examining. The graduated cylinder will have to be tilted to avoid

spillage.

6. Open the manual valve only to the pipe under study.

7. One person should operate the stop-watch and the solenoid switch,

which starts the flow.

8. Open the solenoid valve and start the stop-watch simultaneously.

9. Shut off the valve and the stop-watch simultaneously when the

water level drops to the next height on the table in the data sheet

for this pipe. Collect all the water flowing through the piping

system in the graduated cylinder.

10. Measure and record the actual height to which the water level has

dropped.

11. Measure and record the volume of water collected in the graduated

cylinder.

12. Record the time taken to collect the water.

13. Empty the water from the measuring cylinder into the bucket

provided.

14. Repeat steps 7 – 14 for all other reservoir levels indicated in the

Table for this pipe.

15. Close the manual valve for this pipe.

16. Repeat steps 2 –16 for the various pipe systems specified by the lab

instructor.

Theoretical background and Calculation:

Exit Loss :

Case of where pipe enters a tank – a very large enlargement. The

tank water is assumed to be stationery, that is, the velocity is zero.

Therefore all kinetic energy in pipe is dissipated, therefore K =1.0.

𝐡𝐋 = 𝟏. 𝟎 × (𝐯𝟏𝟐

𝟐𝐠)

Gradual Enlargement

If the enlargement is gradual (as opposed to our previous case) –

the energy losses are less. The loss again depends on the ratio of the pipe

diameters and the angle of enlargement.

𝐡𝐋 = 𝐊 × (𝐯𝟏𝟐/𝟐𝐠)

K can be determined from Fig below and table below:

2015

2016

Note :

➢ If angle increases (in pipe enlargement) – minor losses increase.

➢ If angle decreases – minor losses decrease, but you also need a longer

pipe to make the transition – that means more FRICTION losses -

therefore there is a tradeoff!

➢ Minimum loss including minor and friction losses occur for angle

of 7 degrees – OPTIMUM angle!

Sudden Contraction

Decrease in pipe diameter – Loss is given by –

𝐡𝐋 = 𝐊 × (𝐯𝟐𝟐/𝟐𝐠)

Note: that the loss is related to the velocity in the second (smaller) pipe.

The loss is associated with the contraction of flow and turbulence.

The section at which the flow is the narrowest – Vena Contracta. At vena

contracta, the velocity is maximum, K can be computed using Figure

below and table below – Again based on diameter ratio and velocity of

flow.

Energy losses for sudden contraction are less than those for sudden

enlargement.

Gradual Contraction

Again a gradual contraction will lower the energy loss (as opposed to

sudden contraction). θ is called the cone angle

𝐡𝐋 = 𝐊 × (𝐯𝟐

𝟐/𝟐𝐠)

K is given by Figures below

Note that K values increase for very small angles (less than 15 degrees).

Why – the plot values includes both the effect flow separation and

friction.

Entrance Losses

Fluid moves from zero velocity in tank to v2