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The document is a tutorial for CHEMENG 1007/1007UAC focusing on the momentum equation, with specific problems related to fluid flow through a tee connection and a flow device. It includes calculations for flow rates, pressures, and forces exerted by the fluid, assuming steady, uniform, incompressible, and frictionless flow. The tutorial is due on 12 June 2025 and provides detailed answers for the posed questions.
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0% found this document useful (0 votes)
12 views7 pages

New Tutorial 10

The document is a tutorial for CHEMENG 1007/1007UAC focusing on the momentum equation, with specific problems related to fluid flow through a tee connection and a flow device. It includes calculations for flow rates, pressures, and forces exerted by the fluid, assuming steady, uniform, incompressible, and frictionless flow. The tutorial is due on 12 June 2025 and provides detailed answers for the posed questions.
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as PDF, TXT or read online on Scribd
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CHEMENG 1007/1007UAC: INTRODUCTION TO PROCESS ENGINEERING

TUTORIAL 10
MOMENTUM EQUATION
(Due: 12 June 2025)
Attempt all questions and submit your best solutions for assessment.

3.1 An oil (SG = 0.86) flows through the horizontal tee connection as shown in Fig. 3.1. The
discharge flow rate Q3 at section (3) is 2.0 m3/s and each pipe section has an inside diameter
of 0.5 m. Assume the flow is steady, uniform, incompressible and frictionless.
a. Find the flow rate of oil entering the line at section (2).
b. Calculate the pressures at sections (3) and (2).
c. Determine the components, magnitude and direction of the force exerted by the oil on the
tee.
Ans: (a) 0.82 m3/s (b) 171 kPa; 208 kPa (c) Rx = –45.3 kN; Ry = 7.3 kN;–81o from y-axis

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Fig. 3.1 Fig. 3.2

3.2 Calculate the magnitude and direction of the force required to hold the flow device in Fig. 3.2
stationary. The fluid is water at 20oC, and the device and its content weighs approximately
600 kg. Assume that flow is steady, uniform and frictionless, and that pressures at all outlets
are atmospheric. Gravity is perpendicular to the x-y plane (of the paper);
Ans: (a) 7.1 kN; - 14o from x-axis

Page 1 of 1
Area 0.812 0.196
Question 1
z 59 0.86
Q3 2m31s
i I IT
x
V3 10.2m s

10
v 6m s
Q P 2001pA
Q 1.178 a

Assumptions
steady state flow
uniform
Incompressible fluid
No friction loss frictionless

a Find Qz
A a 0.5
4

0.196

Q v A

65 7m
1 178

Qin Qout
Q Q2 Qs
1.178 Q2 2 m S

i Q2 0 8 2 m s

b Find ps and Pa

Find v2
V2 Q2 A

0.82
4 18 mis

Find v3

V3 03 A
2 1 76
10.2m s

Find p
0.86 1000 density water 861

Formula

P Ipv P3 P V22

Pz P p v12 V32
2
P3 200 000 0.5 860 x 6 10.2
171 KPA

P2 P p v v22
0.5 860 62 4.18
200 000
208kpA
C Roc PV Pn A2 PV P A

78 6,2 200000 0.196


45300 N

45.3 KN

Fy paV2A2 vaxson P3V3 As v3 sin

20800064.18 0.196 sino 171000 10.2 0196 10.20518

7300 N
7 3 kW

Angle aratan
2 2.3
2 Diagram
y
x
T 20 C O
p
1 8919 controlvolume

p 0 RPAgang
2
Assumptions
steady state flow
uniform
frictionless

Component
Momentum Momentumin
Force Pin Pout out

Foc P A PaA cos30 P Afios30 Pa Alsin 60

E PV A Vi PV2 Az V2 cos 30 PV3 A3 V3 sin60


V4 cos 30
PVy Ay

Fx PV A V PV Az V2 x cos 30 PV3Az v3 sin6


PV 4 Ay Vux cos 30 P A P2Azcos 30
1012 2 OC DC
1000 2 5 20 1 2 5 sin 60

1000 1 5 0.667 1.5 cos 30

6000 0.25 5000 0.25 cos 30

1000 1948.6 541.3 1299.7 1500 1732

6939 N

Y component

Fy PaAz Sin 30 P3 Az cos 60 RAY sin 30

Pv A o upV2 Az Va sin 30 PV3 As Uxcos 60


PV4A4 V4 sin 30

PV2 A
Fy PV
Afo 2 Vax sin 30 PusAz
P2A2 sin 30
V3 cos 60 PVuAy Vex son 30

1000 3 0.25 3 son 30 1000 2.5 0.1

2.5 cos 60 000 1 5 0.667 1.5 son 30

8000 0 25 sin 30

1125 312.5 750 375 1000

1687 125 N

F total
T.FI
8
nas
1138 N
7 1

Angle are tan


1 7
13.7

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