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Minor Losses in Pipe Fittings, Contractions, and Expansions

Fluid Mechanics · FE Reference Handbook section

Fluid Mechanics
5 formulas
10 exam-style examples
~55 min
All Fluid Mechanics lectures

Handbook notes for this section

Definitions and conditions exactly as the handbook states them.

  • Head losses also occur as the fluid flows through pipe fittings (i.e., elbows, valves, couplings, etc.) and sudden pipe contractions
  • Specific fittings have characteristic values of C, which will be provided in the problem statement. A generally accepted nominal
  • value for head loss in well-streamlined gradual contractions is
  • The head loss at either an entrance or exit of a pipe from or to a reservoir is also given by the hf, fitting equation. Values for C for
  • various cases are shown as follows.
  • Bober, W., and R.A. Kenyon, Fluid Mechanics, Wiley, 1980. Diagrams reprinted by permission of William Bober and Richard A. Kenyon.

Core formulas for this FE topic

Definitions, applicability, units, assumptions and worked examples for each relation.

Worked exam-style examples

The four ways this section is written on the real exam — thoughts first, then equations, then substitution.

Example 1
Bernoulli between two pipe sections

Water flows at 0.25 m³/s from a 300 mm pipe (p₁ = 250 kPa) into a 200 mm pipe at the same elevation. Neglecting losses, what is p₂?

Given

  • Q=0.25m3/sQ = 0.25 m^{3}/s
  • D1=300mm,D2=200mmD_{1} = 300 mm, D_{2} = 200 mm
  • p1=250kPap_{1} = 250 kPa
  • ρ=1,000kg/m3\rho = 1,000 kg/m^{3}

Find

p₂

Start with the thinking

  • Continuity gives both velocities; Bernoulli converts the velocity change to pressure.
  • Same elevation means the z terms cancel.
D₁=300D₂=200V₁ = 3.54 m/sV₂ = 7.96 m/s

Figure 1 — schematic for Bernoulli between two pipe sections

Step-by-step solution

  1. Areas

    A1=π(0.30)2/4=0.0707m2andA2=π(0.20)2/4=0.0314m2A_{1} = \pi(0.30)^{2}/4 = 0.0707 m^{2} and A_{2} = \pi(0.20)^{2}/4 = 0.0314 m^{2}
  2. Velocities

    V1=0.25/0.0707=3.54m/sandV2=0.25/0.0314=7.96m/sV_{1} = 0.25/0.0707 = 3.54 m/s and V_{2} = 0.25/0.0314 = 7.96 m/s
  3. Bernoulli

    p2=p1+ρ(V12−V22)/2p_{2} = p_{1} + \rho(V_{1}^{2} - V_{2}^{2})/2
  4. Velocity terms

    (3.542−7.962)/2=(12.5−63.4)/2=−25.4m2/s2(3.54^{2} - 7.96^{2})/2 = (12.5 - 63.4)/2 = -25.4 m^{2}/s^{2}
  5. Result

    p2=250,000+1,000(−25.4)=224,600Pa=225kPap_{2} = 250,000 + 1,000(-25.4) = 224,600 Pa = 225 kPa
Answer:

p₂ ≈ 225 kPa

Why the other options are there

  • 275 kPa (sign of the velocity term reversed)
  • 250 kPa (velocity change ignored)

Reference: FE Reference Handbook — Fluid Mechanics — Energy equation

Example 2
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend — Minor Losses in Pipe Fittings, Contractions, and Expansions

the thrust force on a pipe bend in a pressurized pipeline Given fluid density (rho) = 1,045 kg/m^3; flow rate (Q) = 0.0600 m^3/s; inlet velocity (V_1) = 4.8000 m/s; outlet velocity (V_2) = 1.5000 m/s; bend angle (theta) = 30.0000 deg; inlet pressure (p_1) = 251,000 Pa; inlet area (A_1) = 0.1300 m^2; outlet pressure (p_2) = 220,000 Pa; outlet area (A_2) = 0.1850 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=1,045kg/m3fluid density (rho) = 1,045 kg/m^3
  • flowrate(Q)=0.0600m3/sflow rate (Q) = 0.0600 m^3/s
  • inletvelocity(V1)=4.8000m/sinlet velocity (V_1) = 4.8000 m/s
  • outletvelocity(V2)=1.5000m/soutlet velocity (V_2) = 1.5000 m/s
  • bendangle(theta)=30.0000degbend angle (theta) = 30.0000 deg
  • inletpressure(p1)=251,000Painlet pressure (p_1) = 251,000 Pa
  • inletarea(A1)=0.1300m2inlet area (A_1) = 0.1300 m^2
  • outletpressure(p2)=220,000Paoutlet pressure (p_2) = 220,000 Pa
  • outletarea(A2)=0.1850m2outlet area (A_2) = 0.1850 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 2 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend — Minor Losses in Pipe Fittings, Contractions, and Expansions

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 1,045 kg/m^3, flow rate (Q) = 0.0600 m^3/s, inlet velocity (V_1) = 4.8000 m/s, outlet velocity (V_2) = 1.5000 m/s, bend angle (theta) = 30.0000 deg, inlet pressure (p_1) = 251,000 Pa, inlet area (A_1) = 0.1300 m^2, outlet pressure (p_2) = 220,000 Pa, outlet area (A_2) = 0.1850 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=−2837 NF_{x} = -2837\ \text{N}
  6. Step 6 — Check: returning F_x = -2,837 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=−2837 NF_{x} = -2837\ \text{N}

Why the other options are there

  • -5,673 — kept a factor of two that cancels in the correct rearrangement.
  • -1,418 — dropped that same factor in the other direction.
  • -3,120 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 3
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 2) — Minor Losses in Pipe Fittings, Contractions, and Expansions (2)

the reaction force at a pipe enlargement transition Given fluid density (rho) = 985.0 kg/m^3; flow rate (Q) = 0.2500 m^3/s; inlet velocity (V_1) = 2.2000 m/s; outlet velocity (V_2) = 3.0000 m/s; bend angle (theta) = 70.0000 deg; inlet pressure (p_1) = 240,500 Pa; inlet area (A_1) = 0.0450 m^2; outlet pressure (p_2) = 239,000 Pa; outlet area (A_2) = 0.0850 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=985.0kg/m3fluid density (rho) = 985.0 kg/m^3
  • flowrate(Q)=0.2500m3/sflow rate (Q) = 0.2500 m^3/s
  • inletvelocity(V1)=2.2000m/sinlet velocity (V_1) = 2.2000 m/s
  • outletvelocity(V2)=3.0000m/soutlet velocity (V_2) = 3.0000 m/s
  • bendangle(theta)=70.0000degbend angle (theta) = 70.0000 deg
  • inletpressure(p1)=240,500Painlet pressure (p_1) = 240,500 Pa
  • inletarea(A1)=0.0450m2inlet area (A_1) = 0.0450 m^2
  • outletpressure(p2)=239,000Paoutlet pressure (p_2) = 239,000 Pa
  • outletarea(A2)=0.0850m2outlet area (A_2) = 0.0850 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 3 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 2) — Minor Losses in Pipe Fittings, Contractions, and Expansions (2)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 985.0 kg/m^3, flow rate (Q) = 0.2500 m^3/s, inlet velocity (V_1) = 2.2000 m/s, outlet velocity (V_2) = 3.0000 m/s, bend angle (theta) = 70.0000 deg, inlet pressure (p_1) = 240,500 Pa, inlet area (A_1) = 0.0450 m^2, outlet pressure (p_2) = 239,000 Pa, outlet area (A_2) = 0.0850 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=3585 NF_{x} = 3585\ \text{N}
  6. Step 6 — Check: returning F_x = 3,585 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=3585 NF_{x} = 3585\ \text{N}

Why the other options are there

  • 7,171 — kept a factor of two that cancels in the correct rearrangement.
  • 1,793 — dropped that same factor in the other direction.
  • 3,944 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 4
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 3) — Minor Losses in Pipe Fittings, Contractions, and Expansions (3)

the anchoring force needed at a pipe contraction fitting Given fluid density (rho) = 975.0 kg/m^3; flow rate (Q) = 0.3200 m^3/s; inlet velocity (V_1) = 2.2000 m/s; outlet velocity (V_2) = 5.8000 m/s; bend angle (theta) = 75.0000 deg; inlet pressure (p_1) = 290,500 Pa; inlet area (A_1) = 0.1150 m^2; outlet pressure (p_2) = 117,000 Pa; outlet area (A_2) = 0.1550 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=975.0kg/m3fluid density (rho) = 975.0 kg/m^3
  • flowrate(Q)=0.3200m3/sflow rate (Q) = 0.3200 m^3/s
  • inletvelocity(V1)=2.2000m/sinlet velocity (V_1) = 2.2000 m/s
  • outletvelocity(V2)=5.8000m/soutlet velocity (V_2) = 5.8000 m/s
  • bendangle(theta)=75.0000degbend angle (theta) = 75.0000 deg
  • inletpressure(p1)=290,500Painlet pressure (p_1) = 290,500 Pa
  • inletarea(A1)=0.1150m2inlet area (A_1) = 0.1150 m^2
  • outletpressure(p2)=117,000Paoutlet pressure (p_2) = 117,000 Pa
  • outletarea(A2)=0.1550m2outlet area (A_2) = 0.1550 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 4 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 3) — Minor Losses in Pipe Fittings, Contractions, and Expansions (3)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 975.0 kg/m^3, flow rate (Q) = 0.3200 m^3/s, inlet velocity (V_1) = 2.2000 m/s, outlet velocity (V_2) = 5.8000 m/s, bend angle (theta) = 75.0000 deg, inlet pressure (p_1) = 290,500 Pa, inlet area (A_1) = 0.1150 m^2, outlet pressure (p_2) = 117,000 Pa, outlet area (A_2) = 0.1550 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=28496 NF_{x} = 28496\ \text{N}
  6. Step 6 — Check: returning F_x = 28,496 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=28496 NF_{x} = 28496\ \text{N}

Why the other options are there

  • 56,992 — kept a factor of two that cancels in the correct rearrangement.
  • 14,248 — dropped that same factor in the other direction.
  • 31,345 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 5
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 4) — Minor Losses in Pipe Fittings, Contractions, and Expansions (4)

the thrust force on a pipe bend in a pressurized pipeline Given fluid density (rho) = 1,045 kg/m^3; flow rate (Q) = 0.2300 m^3/s; inlet velocity (V_1) = 5.8000 m/s; outlet velocity (V_2) = 4.9000 m/s; bend angle (theta) = 80.0000 deg; inlet pressure (p_1) = 219,000 Pa; inlet area (A_1) = 0.0250 m^2; outlet pressure (p_2) = 251,500 Pa; outlet area (A_2) = 0.0300 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=1,045kg/m3fluid density (rho) = 1,045 kg/m^3
  • flowrate(Q)=0.2300m3/sflow rate (Q) = 0.2300 m^3/s
  • inletvelocity(V1)=5.8000m/sinlet velocity (V_1) = 5.8000 m/s
  • outletvelocity(V2)=4.9000m/soutlet velocity (V_2) = 4.9000 m/s
  • bendangle(theta)=80.0000degbend angle (theta) = 80.0000 deg
  • inletpressure(p1)=219,000Painlet pressure (p_1) = 219,000 Pa
  • inletarea(A1)=0.0250m2inlet area (A_1) = 0.0250 m^2
  • outletpressure(p2)=251,500Paoutlet pressure (p_2) = 251,500 Pa
  • outletarea(A2)=0.0300m2outlet area (A_2) = 0.0300 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 5 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 4) — Minor Losses in Pipe Fittings, Contractions, and Expansions (4)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 1,045 kg/m^3, flow rate (Q) = 0.2300 m^3/s, inlet velocity (V_1) = 5.8000 m/s, outlet velocity (V_2) = 4.9000 m/s, bend angle (theta) = 80.0000 deg, inlet pressure (p_1) = 219,000 Pa, inlet area (A_1) = 0.0250 m^2, outlet pressure (p_2) = 251,500 Pa, outlet area (A_2) = 0.0300 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=2975 NF_{x} = 2975\ \text{N}
  6. Step 6 — Check: returning F_x = 2,975 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=2975 NF_{x} = 2975\ \text{N}

Why the other options are there

  • 5,951 — kept a factor of two that cancels in the correct rearrangement.
  • 1,488 — dropped that same factor in the other direction.
  • 3,273 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 6
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 5) — Minor Losses in Pipe Fittings, Contractions, and Expansions (5)

the reaction force at a pipe enlargement transition Given fluid density (rho) = 990.0 kg/m^3; flow rate (Q) = 0.2200 m^3/s; inlet velocity (V_1) = 4.0000 m/s; outlet velocity (V_2) = 5.5000 m/s; bend angle (theta) = 5.0000 deg; inlet pressure (p_1) = 227,000 Pa; inlet area (A_1) = 0.0200 m^2; outlet pressure (p_2) = 63,000 Pa; outlet area (A_2) = 0.1050 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=990.0kg/m3fluid density (rho) = 990.0 kg/m^3
  • flowrate(Q)=0.2200m3/sflow rate (Q) = 0.2200 m^3/s
  • inletvelocity(V1)=4.0000m/sinlet velocity (V_1) = 4.0000 m/s
  • outletvelocity(V2)=5.5000m/soutlet velocity (V_2) = 5.5000 m/s
  • bendangle(theta)=5.0000degbend angle (theta) = 5.0000 deg
  • inletpressure(p1)=227,000Painlet pressure (p_1) = 227,000 Pa
  • inletarea(A1)=0.0200m2inlet area (A_1) = 0.0200 m^2
  • outletpressure(p2)=63,000Paoutlet pressure (p_2) = 63,000 Pa
  • outletarea(A2)=0.1050m2outlet area (A_2) = 0.1050 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 6 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 5) — Minor Losses in Pipe Fittings, Contractions, and Expansions (5)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 990.0 kg/m^3, flow rate (Q) = 0.2200 m^3/s, inlet velocity (V_1) = 4.0000 m/s, outlet velocity (V_2) = 5.5000 m/s, bend angle (theta) = 5.0000 deg, inlet pressure (p_1) = 227,000 Pa, inlet area (A_1) = 0.0200 m^2, outlet pressure (p_2) = 63,000 Pa, outlet area (A_2) = 0.1050 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=−1728 NF_{x} = -1728\ \text{N}
  6. Step 6 — Check: returning F_x = -1,728 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=−1728 NF_{x} = -1728\ \text{N}

Why the other options are there

  • -3,455 — kept a factor of two that cancels in the correct rearrangement.
  • -863.8 — dropped that same factor in the other direction.
  • -1,900 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 7
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 6) — Minor Losses in Pipe Fittings, Contractions, and Expansions (6)

the anchoring force needed at a pipe contraction fitting Given fluid density (rho) = 1,040 kg/m^3; flow rate (Q) = 0.0500 m^3/s; inlet velocity (V_1) = 3.4000 m/s; outlet velocity (V_2) = 4.9000 m/s; bend angle (theta) = 45.0000 deg; inlet pressure (p_1) = 52,500 Pa; inlet area (A_1) = 0.1050 m^2; outlet pressure (p_2) = 181,500 Pa; outlet area (A_2) = 0.1850 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=1,040kg/m3fluid density (rho) = 1,040 kg/m^3
  • flowrate(Q)=0.0500m3/sflow rate (Q) = 0.0500 m^3/s
  • inletvelocity(V1)=3.4000m/sinlet velocity (V_1) = 3.4000 m/s
  • outletvelocity(V2)=4.9000m/soutlet velocity (V_2) = 4.9000 m/s
  • bendangle(theta)=45.0000degbend angle (theta) = 45.0000 deg
  • inletpressure(p1)=52,500Painlet pressure (p_1) = 52,500 Pa
  • inletarea(A1)=0.1050m2inlet area (A_1) = 0.1050 m^2
  • outletpressure(p2)=181,500Paoutlet pressure (p_2) = 181,500 Pa
  • outletarea(A2)=0.1850m2outlet area (A_2) = 0.1850 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 7 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 6) — Minor Losses in Pipe Fittings, Contractions, and Expansions (6)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 1,040 kg/m^3, flow rate (Q) = 0.0500 m^3/s, inlet velocity (V_1) = 3.4000 m/s, outlet velocity (V_2) = 4.9000 m/s, bend angle (theta) = 45.0000 deg, inlet pressure (p_1) = 52,500 Pa, inlet area (A_1) = 0.1050 m^2, outlet pressure (p_2) = 181,500 Pa, outlet area (A_2) = 0.1850 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=−18227 NF_{x} = -18227\ \text{N}
  6. Step 6 — Check: returning F_x = -18,227 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=−18227 NF_{x} = -18227\ \text{N}

Why the other options are there

  • -36,454 — kept a factor of two that cancels in the correct rearrangement.
  • -9,114 — dropped that same factor in the other direction.
  • -20,050 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 8
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 7) — Minor Losses in Pipe Fittings, Contractions, and Expansions (7)

the thrust force on a pipe bend in a pressurized pipeline Given fluid density (rho) = 1,005 kg/m^3; flow rate (Q) = 0.0700 m^3/s; inlet velocity (V_1) = 5.0000 m/s; outlet velocity (V_2) = 3.6000 m/s; bend angle (theta) = 80.0000 deg; inlet pressure (p_1) = 115,500 Pa; inlet area (A_1) = 0.0250 m^2; outlet pressure (p_2) = 157,000 Pa; outlet area (A_2) = 0.1150 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=1,005kg/m3fluid density (rho) = 1,005 kg/m^3
  • flowrate(Q)=0.0700m3/sflow rate (Q) = 0.0700 m^3/s
  • inletvelocity(V1)=5.0000m/sinlet velocity (V_1) = 5.0000 m/s
  • outletvelocity(V2)=3.6000m/soutlet velocity (V_2) = 3.6000 m/s
  • bendangle(theta)=80.0000degbend angle (theta) = 80.0000 deg
  • inletpressure(p1)=115,500Painlet pressure (p_1) = 115,500 Pa
  • inletarea(A1)=0.0250m2inlet area (A_1) = 0.0250 m^2
  • outletpressure(p2)=157,000Paoutlet pressure (p_2) = 157,000 Pa
  • outletarea(A2)=0.1150m2outlet area (A_2) = 0.1150 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 8 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 7) — Minor Losses in Pipe Fittings, Contractions, and Expansions (7)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 1,005 kg/m^3, flow rate (Q) = 0.0700 m^3/s, inlet velocity (V_1) = 5.0000 m/s, outlet velocity (V_2) = 3.6000 m/s, bend angle (theta) = 80.0000 deg, inlet pressure (p_1) = 115,500 Pa, inlet area (A_1) = 0.0250 m^2, outlet pressure (p_2) = 157,000 Pa, outlet area (A_2) = 0.1150 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=−555.5 NF_{x} = -555.5\ \text{N}
  6. Step 6 — Check: returning F_x = -555.5 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=−555.5 NF_{x} = -555.5\ \text{N}

Why the other options are there

  • -1,111 — kept a factor of two that cancels in the correct rearrangement.
  • -277.7 — dropped that same factor in the other direction.
  • -611.0 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 9
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 8) — Minor Losses in Pipe Fittings, Contractions, and Expansions (8)

the reaction force at a pipe enlargement transition Given fluid density (rho) = 960.0 kg/m^3; flow rate (Q) = 0.1400 m^3/s; inlet velocity (V_1) = 5.4000 m/s; outlet velocity (V_2) = 5.5000 m/s; bend angle (theta) = 70.0000 deg; inlet pressure (p_1) = 183,000 Pa; inlet area (A_1) = 0.1750 m^2; outlet pressure (p_2) = 59,500 Pa; outlet area (A_2) = 0.1500 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=960.0kg/m3fluid density (rho) = 960.0 kg/m^3
  • flowrate(Q)=0.1400m3/sflow rate (Q) = 0.1400 m^3/s
  • inletvelocity(V1)=5.4000m/sinlet velocity (V_1) = 5.4000 m/s
  • outletvelocity(V2)=5.5000m/soutlet velocity (V_2) = 5.5000 m/s
  • bendangle(theta)=70.0000degbend angle (theta) = 70.0000 deg
  • inletpressure(p1)=183,000Painlet pressure (p_1) = 183,000 Pa
  • inletarea(A1)=0.1750m2inlet area (A_1) = 0.1750 m^2
  • outletpressure(p2)=59,500Paoutlet pressure (p_2) = 59,500 Pa
  • outletarea(A2)=0.1500m2outlet area (A_2) = 0.1500 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 9 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 8) — Minor Losses in Pipe Fittings, Contractions, and Expansions (8)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 960.0 kg/m^3, flow rate (Q) = 0.1400 m^3/s, inlet velocity (V_1) = 5.4000 m/s, outlet velocity (V_2) = 5.5000 m/s, bend angle (theta) = 70.0000 deg, inlet pressure (p_1) = 183,000 Pa, inlet area (A_1) = 0.1750 m^2, outlet pressure (p_2) = 59,500 Pa, outlet area (A_2) = 0.1500 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=28500 NF_{x} = 28500\ \text{N}
  6. Step 6 — Check: returning F_x = 28,500 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=28500 NF_{x} = 28500\ \text{N}

Why the other options are there

  • 56,999 — kept a factor of two that cancels in the correct rearrangement.
  • 14,250 — dropped that same factor in the other direction.
  • 31,349 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

Example 10
Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 9) — Minor Losses in Pipe Fittings, Contractions, and Expansions (9)

the anchoring force needed at a pipe contraction fitting Given fluid density (rho) = 1,005 kg/m^3; flow rate (Q) = 0.2100 m^3/s; inlet velocity (V_1) = 2.1000 m/s; outlet velocity (V_2) = 1.3000 m/s; bend angle (theta) = 75.0000 deg; inlet pressure (p_1) = 146,500 Pa; inlet area (A_1) = 0.0800 m^2; outlet pressure (p_2) = 198,000 Pa; outlet area (A_2) = 0.2000 m^2, determine the resultant force on bend (F_x) in N.

Given

  • fluiddensity(rho)=1,005kg/m3fluid density (rho) = 1,005 kg/m^3
  • flowrate(Q)=0.2100m3/sflow rate (Q) = 0.2100 m^3/s
  • inletvelocity(V1)=2.1000m/sinlet velocity (V_1) = 2.1000 m/s
  • outletvelocity(V2)=1.3000m/soutlet velocity (V_2) = 1.3000 m/s
  • bendangle(theta)=75.0000degbend angle (theta) = 75.0000 deg
  • inletpressure(p1)=146,500Painlet pressure (p_1) = 146,500 Pa
  • inletarea(A1)=0.0800m2inlet area (A_1) = 0.0800 m^2
  • outletpressure(p2)=198,000Paoutlet pressure (p_2) = 198,000 Pa
  • outletarea(A2)=0.2000m2outlet area (A_2) = 0.2000 m^2

Find

resultant force on bend (F_x), in N

Start with the thinking

  • The governing relation printed in this handbook section is Pipe bends, enlargements, and contractions (momentum force).
  • Everything except F_x is given, so isolate F_x symbolically first — never rearrange after the numbers are in.
  • Tabulate each given with its unit and confirm the units are consistent with the relation before substituting.
  • Pipe bends, enlargements, and contractions require a momentum balance to find the anchoring force on the fitting.
D₁=200D₂=100V1V2

Figure 10 — schematic for Pipe bends, enlargements, and contractions (momentum force) — solve for resultant force on bend (case 9) — Minor Losses in Pipe Fittings, Contractions, and Expansions (9)

Step-by-step solution

  1. Step 1 — State the governing relation:

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta
  2. Step 2 — Rearrange the relation so that F_x stands alone on the left-hand side.

  3. Step 3 — List the givens: fluid density (rho) = 1,005 kg/m^3, flow rate (Q) = 0.2100 m^3/s, inlet velocity (V_1) = 2.1000 m/s, outlet velocity (V_2) = 1.3000 m/s, bend angle (theta) = 75.0000 deg, inlet pressure (p_1) = 146,500 Pa, inlet area (A_1) = 0.0800 m^2, outlet pressure (p_2) = 198,000 Pa, outlet area (A_2) = 0.2000 m^2.

  4. Step 4 — Substitute the given values into the rearranged relation.

  5. Step 5 — Evaluate:

    Fx=1099 NF_{x} = 1099\ \text{N}
  6. Step 6 — Check: returning F_x = 1,099 N to

    Fx=ρQ(V2cos⁡θ−V1)+p1A1−p2A2cos⁡θF_x = \rho Q (V_2 \cos\theta - V_1) + p_1 A_1 - p_2 A_2 \cos\theta

    reproduces the given quantities, and both sides carry the same units.

Answer:
Fx=1099 NF_{x} = 1099\ \text{N}

Why the other options are there

  • 2,197 — kept a factor of two that cancels in the correct rearrangement.
  • 549.3 — dropped that same factor in the other direction.
  • 1,208 — rounded an intermediate value before the final step.

Reference: FE Handbook — Pipe Bends, Enlargements, and Contractions

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