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CELE Hydraulics & Fluid MechanicsHydrodynamics and Fluid MachineryCheat Sheet

Hydrodynamics and Fluid Machinery cheat sheet — the reference card you wish you had on exam day. Condensed from the full study notes, this is the high-yield core of Hydrodynamics and Fluid Machinery for CELE Hydraulics & Fluid Mechanics. Download, print, revise.

Exam context

On the CELE 2026, the Hydraulics & Fluid Mechanics subtest carries a "Core" weight in Professional Regulation Commission (PRC) — Board of Civil Engineering's pattern. Hydrodynamics and Fluid Machinery lands at position 9th out of 10 in the standard review order. Target score is 70% weighted average, no sub-test below 50%, and roughly a meaningful share of items come from Hydraulics & Fluid Mechanics on a typical CELE paper.

Hydrodynamics and Fluid Machinery - Cheat Sheet

Final 30-minute reference for jet forces, pipe bends, pump and turbine power calculations, and affinity laws. Focus on momentum principle, energy conversion, and exam-critical formulas.

Sections

Formulas

Formula

F = ρQv or F = ρAv²

Meaning

ρ = density (1000 kg/m³), Q = discharge (m³/s), v = velocity (m/s), A = jet area (m²)

Watch Out

Do NOT use γ (specific weight) here — momentum uses ρ (density). Common error: confusing 1000 kg/m³ with 9.81 kN/m³

When To Use

Jet strikes a stationary flat plate normally (perpendicular impact)

Formula

F_n = ρQv sin(α)

Meaning

α = angle between jet and plate surface; F_n = normal force component

Watch Out

α is measured from the plate surface, NOT from the jet direction. If plate is at 30° to jet, α = 30°, not 60°

When To Use

Jet strikes an inclined flat plate; α = 90° recovers the normal-impact formula

Formula

F = ρQv(1 − cos θ)

Meaning

θ = angle through which vane turns the jet (deflection angle)

Watch Out

This formula is for a STATIONARY vane. Moving vane uses relative velocity (v − u) where u = vane speed

When To Use

Jet strikes a curved vane (stationary); θ = 180° gives max force (F = 2ρQv)

Formula

F_relative = ρQ_rel(v_rel)(1 − cos θ)

Meaning

v_rel = (v − u), Q_rel = A(v − u); jet moves with vane at speed u

Watch Out

If v < u, the jet does not strike the vane — guard against this in problem setup

When To Use

Vane is moving (e.g., turbine bucket moving at tangential speed u)

Common Values

Value

1000 kg/m³

Symbol

ρ

Quantity

Water density

Value

9.81 kN/m³ or 9810 N/m³

Symbol

γ

Quantity

Water specific weight

Value

θ ≈ 165° to 170° (not 180° due to bucket geometry)

Symbol

θ_max

Quantity

Maximum deflection angle (Pelton bucket)

Section Title

Jet Force & Momentum Principle

Important Facts

  • Momentum is conserved: inlet momentum − outlet momentum = force × time
  • For a jet splitting on a smooth vane, assume discharge splits proportionally to deflection angles (conservation of Q)
  • Pressure force pA acts at pipe inlet/outlet; must be included in momentum balance for pipe bends
  • Kinetic energy loss = 0.5ρQ(v² inlet − v² outlet) when flow undergoes sudden expansion or collision

Key Definitions

Term

Momentum principle

Example

Jet hitting a plate: the plate exerts force on jet to stop it; by Newton's 3rd law, jet exerts equal/opposite force on plate

Definition

Force on a fluid = mass rate × change in velocity: ΣF = ρQ(v_out − v_in)

Term

Relative velocity (moving vane)

Example

Jet at 20 m/s, vane moving at 5 m/s → relative velocity = 15 m/s

Definition

Velocity of jet relative to the vane frame = (v_jet − v_vane)

Term

Deflection angle (θ)

Example

Pelton bucket turns jet 180° → θ = 180°, cos(180°) = −1, so F = 2ρQv (maximum)

Definition

Angle through which the vane changes the direction of the jet

Diagrams To Know

  • Jet normal to flat plate (force perpendicular to plate)
  • Jet on inclined plate at angle α (resolve force into normal and tangential components)
  • Curved vane deflecting jet by angle θ (force along bisector of deflection for symmetric vane)
  • Moving vane with relative velocity triangle (jet velocity, vane velocity, relative velocity)

Reactions Or Equations

Note

Positive direction is chosen; negative result means force opposes chosen direction

Equation

ΣF_x = ρQ(v_x,out − v_x,in)

Conditions

Applies to control volume; subscripts x, y for coordinate directions

Formulas

Formula

F_x = ρQ(v_{2x} − v_{1x}) + (p_1 A_1)_x − (p_2 A_2)_x

Meaning

Apply momentum in x-direction: ρ, Q as before; p_i = pressure (Pa), A_i = area (m²); subscript indicates component

Watch Out

Pressure forces pA have direction components — a 90° bend has (p₁A₁) horizontal and (p₂A₂) vertical. Sign matters!

When To Use

Pipe bend with inlet 1 and outlet 2; must account for both momentum change AND pressure forces

Formula

F_resultant = √(F_x² + F_y²)

Meaning

Magnitude of anchoring force (what the support/anchor must provide to hold the pipe)

Watch Out

Direction of resultant: θ = arctan(F_y/F_x) — this is often asked in exams

When To Use

After computing F_x and F_y separately; gives total magnitude

Common Values

Value

101.325 kPa (absolute)

Symbol

p_atm

Quantity

Atmospheric pressure (gauge = 0)

Value

98.1 kPa (approximately 100 kPa)

Symbol

p = ρgh

Quantity

Pressure from 10 m water column

Section Title

Force on Pipe Bends

Important Facts

  • For a horizontal pipe at same elevation: p₁ = p₂ if no friction (ideal case), so pressure forces may cancel on certain bend orientations
  • A 90° bend results in maximum force when inlet/outlet diameters are equal and pressures are equal
  • In practice, pressure at outlet may differ due to depth change (use hydrostatic pressure if pipe rises or falls)
  • Anchor reaction is perpendicular to the resultant force direction

Key Definitions

Term

Anchoring force

Example

90° horizontal bend: anchoring force = √(F_x² + F_y²) directed opposite to the resultant momentum + pressure force

Definition

Reaction force exerted by pipe supports/anchors to hold the bend against the dynamic force of flowing water

Term

Control volume

Example

Includes the bend itself and the fluid within it; exterior forces (pressure at ends, anchor reaction) balance momentum change

Definition

Imaginary fixed region around the pipe bend; momentum balance applies across inlet and outlet faces

Diagrams To Know

  • 90° horizontal bend: identify pressure forces at inlet (pointing right) and outlet (pointing up), plus momentum change
  • Reducing bend (larger to smaller diameter): velocity increases at outlet, pressure decreases (Bernoulli); both affect force
  • Vertical bend (pipe rising): account for weight of water in bend, change in elevation head, and hydrostatic pressure difference

Reactions Or Equations

Note

Common case: inlet vertical (v_1y ≠ 0), outlet horizontal (v_2y = 0) → requires both terms

Equation

F_y = ρQ(v_{2y} − v_{1y}) + (p_1 A_1)_y − (p_2 A_2)_y

Conditions

Same momentum principle applied to y-direction; complete vector analysis

Formulas

Formula

P_input = (γQH)/η

Meaning

γ = 9.81 kN/m³, Q = discharge (m³/s), H = head added by pump (m), η = pump efficiency (decimal 0–1)

Watch Out

η goes in the denominator (divide by efficiency). Small η means large input power needed. Common error: multiply by η instead of dividing

When To Use

Calculate motor/engine power required to drive a pump; H is the total head rise across pump

Formula

P_hydraulic = γQH

Meaning

Useful water power (output) delivered to the fluid; same units (kW if γ in kN/m³, Q in m³/s, H in m)

Watch Out

This is NOT the input power — it is the energy imparted to water. Always multiply by efficiency to get actual motor power

When To Use

When only the hydraulic power is asked (ideal case, η = 1); or to verify efficiency: η = P_hydraulic / P_input

Formula

Q_1 / Q_2 = N_1 / N_2

Meaning

Affinity law for discharge: proportional to rotational speed; N in rpm

Watch Out

This is LINEAR: if speed doubles, discharge doubles. Do NOT square or cube

When To Use

Pump speed changes (e.g., variable-frequency drive); find new discharge or speed from this ratio

Formula

H_1 / H_2 = (N_1 / N_2)²

Meaning

Affinity law for head: proportional to speed squared

Watch Out

Square the speed ratio — very different from discharge law. If N doubles, H increases 4×

When To Use

Pump speed changes; find new head. This is QUADRATIC

Formula

P_1 / P_2 = (N_1 / N_2)³

Meaning

Affinity law for power: proportional to speed cubed

Watch Out

Cube the speed ratio. If N doubles, P increases 8×. This is why variable-speed drives save energy

When To Use

Pump speed changes; find new power requirement. This is CUBIC (most aggressive)

Formula

NPSH_required ≤ NPSH_available

Meaning

NPSH = net positive suction head; R = required (depends on pump design), A = available (depends on site/conditions)

Watch Out

If NPSH_available < NPSH_required, cavitation occurs (damage, noise, loss of efficiency). Site elevation and suction line losses reduce available NPSH

When To Use

Check for cavitation risk on pump suction side; typically given in pump datasheets

Common Values

Value

70–90%

Symbol

η

Quantity

Typical centrifugal pump efficiency

Value

9.81 kN/m³

Symbol

γ

Quantity

Specific weight of water

Value

2.34 kPa (absolute)

Symbol

p_v

Quantity

Vapor pressure of water at 20°C

Value

6–8 m (atmospheric pressure limits absolute)

Symbol

h_s,max

Quantity

Typical suction lift limit (centrifugal pump)

Section Title

Pump Power & Performance

Important Facts

  • Affinity laws assume pump operates at same point on efficiency curve (geometrically similar flow patterns)
  • When speed changes: Q ∝ N, H ∝ N², P ∝ N³ — power is most sensitive to speed changes
  • Pump operates at intersection of pump curve (P, H, η vs Q) and system curve (head losses vs Q)
  • Impeller diameter change also obeys affinity laws: Q ∝ D, H ∝ D², P ∝ D³
  • NPSH_available = p_atm/γ − h_s − h_f,suction − p_v/γ (where h_s = suction lift, h_f = friction loss, p_v = vapor pressure)
  • At high altitude, p_atm decreases → NPSH_available decreases → cavitation risk increases

Key Definitions

Term

Head (H)

Example

Pump lifts water 30 m vertically at low speed: H ≈ 30 m + suction losses + discharge losses

Definition

Height equivalent of pressure or energy per unit weight of water; combines pressure head, velocity head, and elevation head

Term

Pump efficiency (η)

Example

Pump with η = 80%: input 100 kW → delivers 80 kW to water (20 kW lost as heat, friction, turbulence)

Definition

Ratio of hydraulic power output to input (shaft) power: η = (γQH) / P_input; typically 70–90% for centrifugal pumps

Term

NPSH (net positive suction head)

Example

Atmospheric pressure 101.325 kPa, vapor pressure at 20°C ≈ 2.3 kPa, suction line elevation +2 m → NPSH_available calculated from Bernoulli

Definition

Pressure head available above vapor pressure at pump inlet; ensures fluid stays liquid inside pump

Term

Cavitation

Example

High-speed pump at high altitude or with long suction line: low NPSH → cavitation → pitting of impeller vanes

Definition

Vapor bubble formation when local pressure drops below vapor pressure; bubbles collapse, causing erosion and noise

Diagrams To Know

  • Pump performance curve: H and η vs discharge Q (typical bell-shaped η curve, H curve may slope down or flat)
  • System curve: H_total = H_static + H_friction(Q); intersection with pump curve = operating point
  • NPSH curve for a pump: shows NPSH_required increasing with Q; plot against NPSH_available from site
  • Affinity law comparison: three speed-ratio examples showing linear (Q), quadratic (H), and cubic (P) relationships

Reactions Or Equations

Note

Rearrange to find input power given η, Q, H or to find hydraulic power given input power and η

Equation

η = (γQH) / P_input = P_hydraulic / P_input

Conditions

Energy balance across pump; efficiency always between 0 and 1

Formulas

Formula

P_output = η × γ × Q × H

Meaning

η = turbine efficiency (0–1), γ = 9.81 kN/m³, Q = discharge (m³/s), H = net head available (m)

Watch Out

Multiply by η (opposite of pump formula where you divide). High efficiency and high head/flow = large power. Common exam trap: reversing pump/turbine formulas

When To Use

Calculate electrical/mechanical power generated by a turbine from flow and head

Formula

H_net = H_gross − H_losses

Meaning

H_gross = total available head (elevation difference), H_losses = friction in intake, penstock, tailrace (m)

Watch Out

H_losses can be 5–15% of H_gross in real projects; ignoring losses overestimates power

When To Use

Refine power calculation to account for pipe/intake friction losses in hydropower plants

Formula

Specific speed: N_s = (N × √Q) / H^(3/4)

Meaning

N = rpm, Q = discharge (m³/s), H = head (m); N_s is dimensionless turbine characteristic; N_s in SI ≈ 0.87 × N_s (US)

Watch Out

Specific speed determines turbine type — don't confuse with ordinary rpm; also be careful with unit consistency (SI vs US)

When To Use

Classify turbine type: Pelton (low N_s ≈ 1–4), Turgo (N_s ≈ 4–10), Crossflow (N_s ≈ 10–100), Francis (N_s ≈ 60–300), Kaplan (N_s ≈ 200–900)

Common Values

Value

1–4

Symbol

N_s (SI)

Quantity

Pelton wheel specific speed range

Value

60–300

Symbol

N_s (SI)

Quantity

Francis turbine specific speed range

Value

200–900

Symbol

N_s (SI)

Quantity

Kaplan turbine specific speed range

Value

90–95%

Symbol

η

Quantity

Typical Pelton efficiency

Value

88–92%

Symbol

η

Quantity

Typical Francis efficiency

Value

85–92% (varies with design head)

Symbol

η

Quantity

Typical Kaplan efficiency

Section Title

Turbine Power & Classification

Important Facts

  • Impulse turbines: all available head converts to kinetic energy in jet; nozzle designs crucial; efficient single or multi-jet operation
  • Reaction turbines: submerged in pressurized casing; require draft tube to extract tail water energy; efficient over wider operating range
  • Francis turbine: curved runner blades, medium head/flow; most common for hydropower; runaway speed ≈ 1.5–1.8 × rated speed
  • Kaplan (propeller) turbine: adjustable blade pitch allows efficiency over wide flow range; large discharge, low head (tidal, run-of-river)
  • Pelton bucket design: enters at center, exits to sides (180° deflection ≈ 165–170° practical) to maximize momentum transfer with minimal splash
  • Power increases with H^1 (linear) and Q^1 (linear), so doubling head OR doubling flow doubles power; N_s = (N√Q)/H^0.75 guides selection

Key Definitions

Term

Impulse turbine

Example

Small flow, high head (>500 m); single or multiple jets on a bucket-wheel; efficient at part-load

Definition

Jet(s) strike moving buckets; momentum transfer drives rotor (NOT pressure drop across blades). Example: Pelton wheel

Term

Reaction turbine

Example

Large flow, medium head (5–300 m); submerged runner in spiral casing; requires draft tube for efficiency

Definition

Pressure drop across moving blades accelerates flow through runner; both pressure and momentum contribute to torque. Examples: Francis, Kaplan

Term

Net head (H_net)

Example

Reservoir at +100 m, tailwater at +10 m, losses = 8 m → H_net = 100 − 10 − 8 = 82 m

Definition

Effective pressure head delivered to turbine after subtracting intake, penstock, and tailrace friction losses

Term

Specific speed (N_s)

Example

Francis turbine typically N_s = 60–300; Pelton typically N_s = 1–4

Definition

Dimensionless parameter combining speed, flow, and head; characterizes turbine geometry and performance

Diagrams To Know

  • Pelton wheel: bucket geometry, jet entry/exit, tangential velocity vector diagram
  • Francis runner: spiral casing, curved blades, discharge direction; draft tube below
  • Kaplan runner: adjustable blades, hub, ring structure; axial flow; draft tube configuration
  • Turbine classification chart: N_s on x-axis (log scale), turbine type and head range labeled
  • Energy conversion: reservoir elevation → penstock kinetic energy → runner rotation → generator power

Reactions Or Equations

Note

Typical η = 85–92% for modern turbines; Pelton best (90–95%), Kaplan varies (85–92% depending on design head)

Equation

η = P_output / P_available = P_output / (γQH_net)

Conditions

Defines turbine efficiency; product of hydraulic, mechanical, and volumetric efficiencies

Formulas

Formula

γ = ρ × g; γ = 9.81 kN/m³ or 9810 N/m³

Meaning

ρ = density (1000 kg/m³), g = gravitational acceleration (9.81 m/s²); γ relates mass and weight

Watch Out

Do NOT use 9.81 kN/m³ in momentum formulas — use ρ = 1000 kg/m³. Two different contexts!

When To Use

When power formula requires γ instead of ρ; converting between weight and mass flows

Formula

Q [m³/s] = A [m²] × v [m/s]

Meaning

Discharge = area × velocity; fundamental continuity equation for incompressible flow

Watch Out

Cross-sectional area must be perpendicular to flow direction; for pipe, A = π(D/2)²

When To Use

Convert between velocity and discharge; find jet area from discharge and velocity

Formula

1 kW = 1 kN/m³ × 1 m³/s × 1 m = γ [kN/m³] × Q [m³/s] × H [m]

Meaning

Power in kW when using γ in kN/m³, Q in m³/s, H in m

Watch Out

If using N/m³ for γ, power comes out in watts (W); if using kN/m³, power is in kW. Always verify units

When To Use

Pump/turbine power calculations; simple dimensional check

Formula

Pressure head: h = p / γ [m]

Meaning

Convert pressure (Pa or kPa) to equivalent water column height (m); h = p / ρg

Watch Out

γ = 9.81 kN/m³; if p = 98.1 kPa, h = 98.1 kPa / 9.81 kN/m³ = 10 m (exactly)

When To Use

Total head analysis (elevation + pressure + velocity head); NPSH calculations

Formula

Velocity head: h_v = v² / (2g) [m]

Meaning

Kinetic energy expressed as equivalent head; g = 9.81 m/s²

Watch Out

Even at high velocity (e.g., 10 m/s), velocity head = 100/(2×9.81) ≈ 5.1 m — often small compared to pressure/elevation head

When To Use

Bernoulli equation; total head in pipes with significant velocity

Common Values

Value

1000 kg/m³

Symbol

ρ

Quantity

Water density

Value

9.81 kN/m³

Symbol

γ

Quantity

Water specific weight (SI)

Value

9.81 m/s²

Symbol

g

Quantity

Gravitational acceleration

Value

9.81 kPa

Symbol

p = γh

Quantity

Pressure equivalent of 1 m water

Value

101.325 kPa = 10.33 m water

Symbol

p_atm

Quantity

Atmospheric pressure (standard)

Section Title

Practical Hydraulic Calculations & Unit Conversions

Important Facts

  • Bernoulli is valid along a streamline for frictionless, steady, incompressible flow
  • In real pipes, add friction head loss: H_friction ≈ f(L/D)(v²/2g) (Darcy-Weisbach); reduces net available head
  • Pressure units: 1 kPa = 1000 Pa = 0.00987 m of water (approximately); 100 kPa ≈ 10.2 m water column
  • Discharge in pipes remains constant (continuity): A₁v₁ = A₂v₂; if pipe reduces, velocity increases and pressure decreases (Bernoulli)

Key Definitions

Term

Total head (H_total)

Example

Pump inlet at −2 m elevation, p = 40 kPa, v = 1 m/s: total head = −2 + 40/9.81 + 1²/19.62 ≈ −2 + 4.08 + 0.05 ≈ 2.1 m

Definition

Sum of elevation, pressure, and velocity heads: H_total = z + p/γ + v²/(2g) (Bernoulli constant along streamline)

Term

Static head

Example

Reservoir 40 m above discharge, zero gauge pressure: H_static = 40 m (ignoring velocity and losses)

Definition

Elevation difference + pressure head (no velocity component); H_static = Δz + Δp/γ

Diagrams To Know

  • Hydraulic grade line (HGL): plot of (p/γ + z) vs distance; shows available pressure head at each point
  • Energy grade line (EGL): plot of (p/γ + z + v²/2g) vs distance; lies above HGL by velocity head; drops due to friction
  • Pump and system curve: H vs Q; operating point at intersection; affinity law scaling of pump curve for different speeds

Reactions Or Equations

Note

If no friction (ideal): total head is constant. Real flow: head decreases downstream due to h_f

Equation

Bernoulli: (p₁/γ) + z₁ + (v₁²/2g) = (p₂/γ) + z₂ + (v₂²/2g) + h_f

Conditions

Steady, incompressible flow along a streamline; h_f = friction loss between points 1 and 2

Must Remember

  • Jet force on stationary flat plate: F = ρQv = ρAv² (MOMENTUM, NOT pressure). Use ρ = 1000 kg/m³, not γ = 9.81 kN/m³.
  • Moving vane force uses RELATIVE VELOCITY (v − u), not absolute jet velocity v. If vane speed u > jet speed v, vane misses the jet.
  • Curved vane deflects jet by angle θ: force F = ρQv(1 − cos θ). Maximum at θ = 180° (F = 2ρQv). Always check deflection angle in exam.
  • Pump INPUT power formula: P_input = (γQH) / η — divide by efficiency. Turbine OUTPUT power: P_output = η × γ × Q × H — multiply by efficiency. OPPOSITE conventions!
  • Affinity laws (with speed change): Q ∝ N (linear), H ∝ N² (quadratic), P ∝ N³ (cubic). Doubling speed quadruples head and octuples power — massive effect on motor sizing.
  • Impulse turbines (Pelton): high head (>500 m), small discharge, N_s = 1–4. Reaction turbines (Francis/Kaplan): medium head (5–300 m), large discharge, N_s = 60–900. Turbine TYPE determined by specific speed.
  • Pipe bend: include BOTH momentum change (ρQΔv) AND pressure forces (pA) in each direction. Forgetting pressure forces is a common exam killer.
  • NPSH_required > NPSH_available → cavitation (pump damage, noise, loss of prime). High altitude, high speed, long suction line ALL reduce NPSH_available — guard against cavitation.
  • Pressure head conversion: 1 kPa ≈ 0.102 m water; 100 kPa ≈ 10.2 m. Velocity head at 10 m/s = 100/(2×9.81) ≈ 5.1 m. Always include velocity head in Bernoulli if flow speed is high (>3 m/s).
  • Specific speed N_s = (N√Q) / H^(0.75) (SI units) uniquely identifies turbine type. Mixing SI and US units for N_s is a common error; always confirm unit system in exam question.

Last Minute Tips

  • ρ vs γ CRITICAL: Momentum formulas use ρ (kg/m³); power formulas use γ (kN/m³ or N/m³). Wrong choice = wrong answer by factor of 10. Double-check every formula substitution.
  • Pump vs Turbine Power: Pump divides by η (input/efficiency ratio), Turbine multiplies by η (output = efficiency × available power). Reverse it = instant wrong answer. Write both formulas side-by-side before solving.
  • Affinity Law Exponents: Remember Q is LINEAR (×N), H is QUADRATIC (×N²), P is CUBIC (×N³). If you guess wrong on exponent, entire calculation fails. Visual mnemonic: Q-line, H-square, P-cube.
  • Deflection Angle θ in Jet-Vane: θ is total deflection (how much the vane turns the jet), NOT the angle from horizontal. Pelton bucket deflects ~165° (not 180° due to geometry). Read problem carefully for angle definition.
  • Exam Time Saver: Always verify units before plugging numbers in. If γ in kN/m³, Q in m³/s, H in m → power in kW directly. If units mismatch, recalculate. One minute spent on unit check saves 5 minutes of debugging wrong answers.

Comparison Tables

Rows

Values

  • >500 m (very high)
  • 5–300 m (medium)

Property

Head range

Values

  • Small to medium
  • Large

Property

Discharge range

Values

  • 1–4
  • 60–300 (Francis); 200–900 (Kaplan)

Property

Specific speed (N_s, SI)

Values

  • Potential → kinetic (nozzle) → momentum transfer
  • Pressure drop across blades; pressure + momentum

Property

Energy conversion

Values

  • Buckets on wheel rim
  • Submerged curved blades in spiral casing

Property

Runner type

Values

  • No (atmospheric discharge)
  • Yes (extracts tail water energy)

Property

Draft tube required?

Values

  • 90–95%
  • 88–92% (varies)

Property

Efficiency at rated load

Values

  • Good (maintains high efficiency down to ~30% load)
  • Francis: moderate; Kaplan: excellent (adjustable blades)

Property

Part-load efficiency

Values

  • High head: mountain reservoirs, run-of-river
  • Francis: medium head hydropower; Kaplan: tidal, low-head run-of-river

Property

Common applications

Columns

  • Feature
  • Impulse (Pelton)
  • Reaction (Francis/Kaplan)

Table Title

Impulse vs Reaction Turbines

Rows

Values

  • Adds head (lifts fluid)
  • Extracts head (generates power)

Property

Function

Values

  • Mechanical → hydraulic
  • Hydraulic → mechanical

Property

Energy conversion

Values

  • P_input = (γQH) / η
  • P_output = η × γ × Q × H

Property

Power formula

Values

  • Divide (denominator)
  • Multiply (coefficient)

Property

Efficiency location

Values

  • 70–90% (centrifugal)
  • 85–95% (modern turbines)

Property

Typical efficiency

Values

  • Q ∝ N (linear)
  • Q ∝ N (linear)

Property

Affinity law: Q

Values

  • H ∝ N² (quadratic)
  • H ∝ N² (quadratic)

Property

Affinity law: H

Values

  • P ∝ N³ (cubic)
  • P ∝ N³ (cubic)

Property

Affinity law: P

Values

  • Yes — suction side (NPSH_required check)
  • No — pressure side; operates under submergence

Property

Cavitation risk?

Columns

  • Aspect
  • Pump
  • Turbine

Table Title

Pump vs Turbine — Power & Efficiency

Rows

Values

  • F = ρQv = ρAv²
  • v = jet velocity, A = jet area; result is force perpendicular to plate

Property

Jet on stationary flat plate (normal impact)

Values

  • F_n = ρQv sin(α)
  • α is angle between jet and plate surface; α = 90° gives normal impact formula

Property

Jet on inclined plate at angle α

Values

  • F = ρQv(1 − cos θ)
  • θ = 180° → F = 2ρQv (max force); θ = 90° → F ≈ 1.41ρQv

Property

Jet on curved vane (stationary), deflection θ

Values

  • F = ρ(v−u)Q_rel(1 − cos θ)
  • Use relative velocity (v − u); if v < u, jet misses vane. Typical in turbines

Property

Jet on moving vane at speed u, deflection θ

Columns

  • Scenario
  • Formula
  • Notes

Table Title

Jet Force Formulas — Quick Reference

Rows

Values

  • Q₂ = Q₁ × (N₂/N₁)
  • Q doubles (×2)

Property

Discharge (Q)

Values

  • H₂ = H₁ × (N₂/N₁)²
  • H increases ×4

Property

Head (H)

Values

  • P₂ = P₁ × (N₂/N₁)³
  • P increases ×8 (cubic!)

Property

Power (P)

Values

  • NPSH_required ∝ N²
  • NPSH requirement increases ×4; risk increases at high speed

Property

Cavitation/NPSH

Columns

  • Parameter
  • Relationship
  • Example: if N doubles (×2)

Table Title

Affinity Laws — Scaling Pump/Turbine Performance

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