Fluid Mechanics

Chapter 13
Fluid Measurement, Experiments, and Data Analytics

Bachelors Program in Construction Technology
Fluid Mechanics   •   Bachelor

Fluid Measurement, Experiments, and Data Analytics

Introduction and Context

Fluid mechanics becomes an engineering science when fluid behavior is measured, compared with theory, and used to support decisions. In construction and infrastructure projects, engineers measure pressure in water-supply systems, velocity in channels, discharge through pipes and pumps, and level in tanks, reservoirs, excavations, and drainage structures. Reliable measurement supports hydraulic design, commissioning, operational control, safety verification, energy assessment, and dispute resolution.

A measurement is not simply a number displayed by an instrument. It is an observation produced by an instrument, a method, an operator, and an environmental condition. The quality of the result depends on instrument selection, installation, calibration, sampling, data processing, and reporting. This chapter develops a practical framework for obtaining defensible hydraulic data and converting it into engineering information.

Learning Objectives

By the end of this chapter, students should be able to:

  1. Select suitable instruments for pressure, velocity, discharge, and level measurement.
  2. Explain the operating principles and limitations of common hydraulic instruments.
  3. Plan a safe and repeatable fluid-mechanics experiment.
  4. Calibrate sensors and distinguish accuracy, precision, resolution, and repeatability.
  5. Estimate uncertainty and propagate uncertainty through basic calculations.
  6. Analyze hydraulic data using spreadsheets and elementary statistical methods.
  7. Detect poor-quality data, outliers, drift, and physically implausible results.
  8. Present experimental findings in a technically credible report.

1. Measurement as an Engineering Process

The measurement chain consists of five linked stages:

  1. Measurand definition: identify what is to be measured, such as gauge pressure at a pipe tap or average discharge through a flume.
  2. Sensing: convert a physical quantity into a mechanical, electrical, optical, or digital signal.
  3. Transmission and recording: transfer the signal to a display, data logger, or computer.
  4. Reduction: convert raw readings into engineering variables using calibration equations and physical relationships.
  5. Interpretation: compare results with design values, standards, theory, or acceptance criteria.

The measurand must be defined precisely. For example, “water level” could mean the free-surface elevation relative to a benchmark, the depth above a channel bed, or the level reported by a pressure transducer. These quantities are related but not interchangeable.

Important measurement terminology

TermMeaning
AccuracyCloseness of a result to the accepted reference value
PrecisionCloseness of repeated results to one another
ResolutionSmallest change that an instrument can display or distinguish
SensitivityChange in output per unit change in input
RepeatabilityAgreement under the same method, operator, and conditions
ReproducibilityAgreement when important conditions, such as operators or laboratories, change
RangeInterval between lower and upper operating limits
DriftChange in indication over time when the measurand is constant
HysteresisDifferent output for increasing and decreasing input at the same value
UncertaintyQuantified doubt associated with a measurement result

Accuracy and precision are different. A pressure sensor may give tightly grouped readings that are all biased by 3 kPa; it is precise but not accurate. Calibration is needed to identify and, where justified, correct such bias.

2. Measuring Pressure

Pressure is the normal force exerted per unit area. For a static fluid,

p = F/A

where p is pressure in pascals (Pa), F is normal force in newtons (N), and A is area in square metres (m²). Pressure is a scalar field, although the force exerted by pressure acts normal to a surface.

Pressure may be reported as absolute pressure, gauge pressure, or vacuum pressure. Absolute pressure is measured relative to a perfect vacuum. Gauge pressure is measured relative to local atmospheric pressure:

pabs = pg + patm

where pabs is absolute pressure, pg is gauge pressure, and patm is atmospheric pressure. The relationship is valid when all pressures use consistent units. A negative gauge pressure indicates pressure below atmospheric pressure; it does not necessarily indicate negative absolute pressure.

For a fluid at rest, pressure variation with elevation is described by

p2 - p1 = ρg(z1 - z2)

where ρ is fluid density (kg/m³), g is gravitational acceleration (m/s²), and z is elevation measured upward. This hydrostatic relationship assumes a fluid at rest, approximately constant density, and negligible capillary effects.

Pressure instruments

Piezometers are vertical transparent tubes connected to a pipe or vessel. The liquid rises to a height representing pressure head. They are simple and accurate for low positive pressures in clean liquids, but they are unsuitable for high pressure, gases, contaminated fluids, or negative gauge pressure.

Manometers use a liquid column, often a denser fluid such as mercury, to compare pressure. A differential manometer measures the pressure difference between two points. It is valuable for laboratory work because the physical principle is direct, but reading menisci and correcting for density and elevation require care.

Bourdon-tube gauges use elastic deformation of a curved metal tube. They are inexpensive and robust, but mechanical friction, vibration, temperature, and hysteresis can affect readings.

Diaphragm and strain-gauge transducers convert deformation into an electrical signal. They are suitable for data logging and automation. Their installation must consider overpressure protection, temperature effects, electrical noise, and compatibility between the wetted material and the fluid.

Differential-pressure transmitters measure the difference between two pressure ports. With suitable primary devices, such as an orifice plate or Venturi meter, they can be used to infer flow rate. The pressure taps must be correctly located and free of air pockets or sediment.

Pressure measurement practice

Install pressure taps flush with the pipe wall and orient them to avoid collecting air or solids. Isolate the instrument with valves so that it can be removed safely. Before recording, allow the system to reach steady operating conditions and check for zero offset. Pressure pulsation can be reduced with a snubber, damping element, or appropriate digital averaging, but excessive filtering may hide real transients.

3. Measuring Velocity and Discharge

Velocity is a vector, whereas discharge is the volume of fluid passing a section per unit time. The general discharge relationship is

Q = ∫A Vn dA

where Q is discharge (m³/s), A is the flow cross-section, and Vn is the component of velocity normal to the area. If velocity is uniform and perpendicular to the section, this reduces to

Q = VA

where V is mean velocity. The simplified equation must not be used with a local point velocity unless that velocity is demonstrably representative of the cross-sectional mean.

Velocity instruments

Pitot and Pitot-static tubes measure stagnation and static pressure. For incompressible flow under appropriate conditions, velocity can be estimated from

V = Cp √(2∆p/ρ)

where ∆p is the measured pressure difference, ρ is density, and Cp is a calibration coefficient. The ideal equation assumes negligible elevation difference, low compressibility, and a properly aligned probe. The coefficient accounts for probe geometry and real-flow effects.

Current meters use a rotating propeller or cup. A calibration relation commonly has the form

V = a + bN

where N is rotational frequency and a and b are experimentally determined constants. The equation must be used only within the calibration range.

Acoustic Doppler instruments estimate velocity from the frequency shift of sound scattered by suspended particles. They are useful in open channels and rivers but can be affected by sediment concentration, air entrainment, reflections, and insufficient measurement depth.

Electromagnetic meters infer velocity from the voltage induced as a conductive fluid moves through a magnetic field. They have no moving parts and work well with conductive liquids, but they require a full pipe and appropriate electrical conductivity.

Ultrasonic transit-time meters compare upstream and downstream travel times of sound. They are convenient for temporary or non-invasive pipe measurements, although air bubbles, poor transducer placement, and unsuitable pipe conditions can cause error.

Discharge measurement methods

For a full pipe, discharge may be determined by a calibrated flow meter, a velocity-area method, or a differential-pressure primary device. In open channels, common methods include the current-meter method, acoustic Doppler measurement, weirs, flumes, and the volumetric method.

For a known tank volume, the volumetric method is

Q = ∆V/∆t

where ∆V is the collected volume and ∆t is the collection time. It is conceptually simple, but timing uncertainty, splashing, leakage, and difficulty measuring the final volume may be significant.

A sharp-crested rectangular weir may be used with a suitable calibrated equation. Because coefficients depend on geometry, crest condition, approach flow, and head measurement, students should use the equation specified by the relevant standard or laboratory calibration rather than treating a coefficient as universal.

4. Measuring Fluid Level

Level may be measured directly or inferred from pressure. Direct methods include graduated staffs, sight glasses, floats, ultrasonic sensors, and radar instruments. A submerged pressure sensor measures liquid head according to

pg = ρgh

where h is the vertical liquid depth above the sensing point. This formula assumes a static or slowly varying liquid, known density, and a properly vented reference for a gauge transducer.

Level instruments must be referenced to a datum. A statement such as “level = 1.2 m” is incomplete unless the reference surface is known. Construction projects often use a site benchmark or a surveyed elevation. Temperature, foam, turbulence, sediment deposition, and changing fluid density can affect level readings.

Ultrasonic level sensors measure travel time of a sound pulse reflected from the surface. They are non-contact devices but may be affected by vapor, foam, angled surfaces, and temperature. Radar sensors generally perform better in vaporous or dusty environments but require appropriate installation and configuration.

5. Planning a Fluid Experiment

A sound experiment begins with a question that can be answered by measured evidence. For example: “How does discharge through the test pipe vary with pump speed?” is more useful than “Investigate flow.”

A complete plan should specify:

  • the hypothesis or expected relationship;
  • independent, dependent, and controlled variables;
  • apparatus, dimensions, fluid properties, and instrument ranges;
  • operating procedure and stabilization criteria;
  • number and spacing of test points;
  • calibration and zero checks;
  • sampling frequency and duration;
  • safety controls;
  • data-storage format and file naming;
  • method of uncertainty estimation; and
  • acceptance criteria for valid results.

Repeated observations are important. If the objective is to estimate a mean under stable conditions, several readings should be taken at each operating point. If the objective is to study transients, averaging may be inappropriate because it can remove the phenomenon of interest.

Experimental controls and safety

Hydraulic experiments can involve pressurized water, rotating machinery, electricity, slippery floors, and sudden release of stored energy. Hoses and fittings must be rated for the maximum pressure. Guards should remain in place around pumps and couplings. Electrical equipment must be protected from water, and isolation valves should be closed before dismantling components. A risk assessment should identify hazards, controls, emergency shutdown procedures, and waste-disposal requirements.

A stable test condition should be defined operationally, for example: pressure and discharge vary by less than a specified percentage over a specified observation period. “Wait until stable” is not a reproducible procedure.

6. Calibration and Sensor Quality

Calibration compares an instrument with a reference over a defined range. A calibration may produce a correction table, a graph, or a fitted equation. For a linear sensor, a useful model is

y = a + bx

where x is the reference input, y is the instrument output, a is the intercept, and b is sensitivity. The fitted relation should not be extrapolated beyond the calibration range without technical justification.

A practical calibration procedure is:

  1. Inspect the instrument and record identification, range, resolution, and last calibration date.
  2. Select reference points covering the intended operating range.
  3. Apply increasing inputs and record stabilized outputs.
  4. Repeat selected points, including zero and full-scale checks.
  5. If hysteresis may occur, repeat points while decreasing the input.
  6. Fit or calculate corrections and examine residuals.
  7. Record reference uncertainty, environmental conditions, and operator details.
  8. Label the instrument with status and next calibration date.

The correction at a point can be written as

c = xref - xind

where c is correction, xref is the reference value, and xind is the indicated value. A correction is added to the indication only when the calibration convention and sign have been established clearly.

Calibration does not guarantee that an instrument is suitable. A sensor can be well calibrated but have insufficient range, resolution, response time, chemical compatibility, or environmental protection.

7. Uncertainty and Statistical Treatment

A measurement result should be reported as an estimate plus an uncertainty where the decision requires it. Uncertainty is not the same as a mistake. Mistakes include reversed leads, incorrect units, or transcription errors; they should be corrected rather than hidden inside an uncertainty estimate.

For repeated readings x1, x2, …, xn, the arithmetic mean is

x̄ = (1/n) ∑i=1n xi

and the sample standard deviation is

s = √[∑i=1n (xi − x̄)²/(n − 1)]

The standard deviation describes the spread of observations. The standard uncertainty of the mean, when independent repeated observations are appropriate, is

uA = s/√n

where n is the number of observations. This reduction applies to random variation in the mean; it does not remove calibration bias or systematic effects.

Instrument specifications, calibration certificates, resolution, and environmental estimates may provide other uncertainty components. If independent standard uncertainties contribute to a result, a basic combined estimate is

uc = √(u1² + u2² + … + uk²)

This root-sum-square approach assumes the components are expressed in the same units and are uncorrelated. Correlated components require covariance terms. For a result y = f(x1, x2, …, xm), first-order propagation is

uy² = ∑i=1m (∂f/∂xi)²ui²

for independent inputs. The partial derivatives describe sensitivity to each input.

For discharge calculated as Q = VA, with independent uncertainties in mean velocity and area,

uQ/Q = √[(uV/V)² + (uA/A)²]

This relative form follows from the general propagation equation and is valid for small uncertainties.

Worked Example 1: discharge and uncertainty

A test pipe has measured mean velocity V = 1.80 ± 0.05 m/s. Its internal diameter is D = 0.100 ± 0.001 m. For a circular pipe,

A = πD²/4

Thus,

A = π(0.100)²/4 = 0.007854 m²

The discharge is

Q = VA = 1.80 × 0.007854 = 0.01414 m³/s

The relative uncertainty is

uQ/Q = √[(0.05/1.80)² + (2×0.001/0.100)²]
= √(0.0278² + 0.0200²)
= 0.0342

Therefore,

uQ = 0.01414 × 0.0342 = 0.00048 m³/s

A suitable report, subject to the stated uncertainty convention, is Q = 0.01414 ± 0.00048 m³/s, or approximately 14.14 ± 0.48 L/s. The factor 2 multiplying the relative diameter uncertainty occurs because area depends on diameter squared.

8. Spreadsheet and Data Analytics Workflow

A spreadsheet should preserve raw evidence rather than overwrite it. A robust workbook commonly contains:

  1. Read-me sheet: purpose, units, operator, date, apparatus, and file version.
  2. Raw-data sheet: unmodified instrument readings and timestamps.
  3. Calibration sheet: reference data, fitted coefficients, corrections, and residuals.
  4. Calculations sheet: formulas converting readings into pressure, velocity, discharge, or level.
  5. Statistics sheet: means, standard deviations, uncertainty estimates, and flagged values.
  6. Charts sheet: appropriately labelled plots.
  7. Report sheet: selected results and conclusions.

Every column needs a heading and unit. Cell formulas should be visible and auditable. Hard-coded constants should be identified, and input cells should be visually distinguished from calculated cells. A change log is particularly important when spreadsheet results support payment, compliance, or safety decisions.

Useful analyses include:

  • time-series plots to reveal drift or transients;
  • scatter plots of discharge against pressure difference or pump speed;
  • residual plots to assess a fitted model;
  • moving averages for visualization of trends, not for concealing instability;
  • minimum, maximum, mean, and standard deviation;
  • linear regression where a linear model is physically justified; and
  • dimensional checks and comparisons with conservation laws.

The coefficient of determination, often written R², indicates how much variation in the observed response is represented by a fitted regression model. It does not prove causation, validate the physical model, or demonstrate accurate extrapolation. A physically poor model can still produce a high R² over a narrow range.

Data-quality checks

Before analysis, check for missing timestamps, duplicate records, impossible negative values, unit mismatches, sensor saturation, abrupt discontinuities, and values outside the instrument range. An apparent outlier should be investigated using notes, repeat measurements, and physical reasoning. It should not be deleted solely because it disagrees with a preferred theory.

Dimensional analysis is a powerful check. For example, ρgQH has units

(kg/m³)(m/s²)(m³/s)(m) = kg·m²/s³ = W

so it represents a power scale, as expected for hydraulic power.

9. Case Application: Commissioning a Pumped Water Line

Background

This illustrative case concerns commissioning a temporary pumped water line supplying a construction-site storage tank. The contractor must verify that the line delivers at least 12 L/s at the planned operating condition without exceeding the allowable pressure.

Problem

The line includes a pump, a full pipe, a pressure gauge near the discharge, and a clamp-on ultrasonic flow meter. The flow meter has not recently been checked against an independent method. Pressure fluctuates during pump start-up, and the tank level rises during the test.

Analysis and approach

The engineering team defines the measurands as steady discharge at the pipe outlet and gauge pressure at the specified pressure tap. They inspect the pipe for full-bore conditions, install the ultrasonic sensors according to the manufacturer’s straight-run requirements, and record pipe diameter and fluid temperature. The gauge is compared with a calibrated reference gauge at several pressure points.

Three operating points are selected: low, normal, and high pump speed. At each point, the pump is allowed to stabilize for two minutes, followed by 60 seconds of one-second readings. Start-up data are excluded from the steady-state analysis but retained for transient review. A timed tank-volume increase provides an independent discharge check at the normal point.

The spreadsheet stores raw readings, calibration information, formulas, and flags. At the normal point, the ultrasonic meter reports a mean of 12.4 L/s with a standard deviation of 0.18 L/s. The timed-volume method reports 12.1 L/s. The difference is 0.3 L/s, or about 2.5% relative to the volumetric result. The team investigates whether timing, tank-level reading, or meter installation explains the difference before accepting the result.

The pressure gauge indicates 420 kPa gauge at the discharge. Atmospheric pressure is recorded separately if absolute pressure is required. The team confirms that this pressure is below the specified allowable value and reports pressure type explicitly.

Outcome

After correcting a small zero offset and improving transducer alignment, the normal-point discharge is reported as 12.2 L/s with an expanded uncertainty stated in the commissioning report. The line satisfies the minimum flow requirement, and the pressure remains within the allowable operating range. The report recommends periodic verification because sediment and sensor movement may affect future readings.

Learning points

The case demonstrates that commissioning is not satisfied by a single display reading. Independent checks, explicit measurand definitions, stabilization criteria, calibration records, uncertainty statements, and traceable data files are necessary for a defensible conclusion.

10. Technical Reporting and Professional Responsibilities

A technical report should allow a competent reader to understand what was done and judge whether the conclusion follows from the evidence. A suitable structure is:

  • title, author, date, and revision;
  • purpose and scope;
  • theory and governing equations;
  • apparatus and instrument specifications;
  • calibration procedure;
  • method and safety controls;
  • raw-data summary;
  • calculations and uncertainty method;
  • graphs and tables with units;
  • results and comparison with expected behavior;
  • limitations and anomalies;
  • conclusion and recommendations; and
  • references and appendices containing detailed data.

Graphs should show variable names, units, scales, legends, and uncertainty bars where meaningful. Do not use excessive decimal places. The number of reported digits should reflect instrument resolution and uncertainty.

Professional ethics require honest treatment of data. Results must not be selectively reported to achieve a contractual or academic target. If a sensor failed, a test condition was unstable, or a model was extrapolated, the limitation should be stated. Personal data, site-security information, and client data should be protected under applicable policies. Digital records should be backed up, access-controlled, and versioned.

11. Contemporary Tools and Best Practices

Modern projects increasingly use wireless pressure nodes, cloud-connected loggers, digital twins, remote sensing, and automated anomaly detection. These tools can improve temporal coverage, but they do not eliminate the need for calibration or engineering judgment. Artificial-intelligence systems may identify unusual patterns or assist with forecasting, but the training data, false-alarm rate, missing-data treatment, and decision authority must be documented. An algorithm should not silently replace a physical check when failure could threaten safety.

Best practice is to combine automation with independent verification: maintain raw data, synchronize clocks, record metadata, calibrate against traceable references, use physically informed limits, and review flagged results by a qualified person. The central principle is simple: measurement technology supports engineering judgment; it does not substitute for it.

Chapter Summary

Fluid measurement links hydraulic theory with construction practice. Pressure may be measured using piezometers, manometers, mechanical gauges, and electronic transducers. Velocity and discharge require attention to velocity profiles, cross-sectional averaging, instrument calibration, and flow conditions. Level measurements must be tied to a clear datum and may be direct or inferred from hydrostatic pressure.

Reliable experiments begin with defined measurands, controlled variables, stabilization criteria, calibration checks, safe procedures, and a documented data plan. Statistical tools such as the mean, standard deviation, standard uncertainty, and uncertainty propagation help quantify the quality of results. Spreadsheets should preserve raw data, expose formulas, enforce units, and support transparent plots and checks. Technical reports should communicate methods, evidence, uncertainty, limitations, and conclusions honestly. Digital and AI-enabled tools are valuable when combined with traceability, physical reasoning, cybersecurity, and professional accountability.

Key Terms

Measurand: The specific quantity intended to be measured.

Gauge pressure: Pressure measured relative to local atmospheric pressure.

Absolute pressure: Pressure measured relative to a perfect vacuum.

Hydrostatic pressure: Pressure distribution in a fluid at rest.

Piezometer: A tube used to indicate pressure head in a liquid.

Manometer: An instrument that compares pressure using liquid-column heights.

Pitot tube: A probe used to relate stagnation and static pressure to velocity.

Discharge: Volume flow rate through a cross-section.

Calibration: Comparison of an instrument with a reference to establish indication and correction.

Accuracy: Closeness of a result to an accepted reference value.

Precision: Closeness of repeated results to each other.

Resolution: Smallest distinguishable change in an instrument indication.

Drift: Time-dependent change in indication for a constant measurand.

Hysteresis: Dependence of indication on whether the input is increasing or decreasing.

Uncertainty: Quantified doubt associated with a measurement result.

Standard deviation: Measure of the spread of repeated observations.

Data logger: Device that records measurements, commonly with timestamps.

Residual: Difference between an observed value and a fitted or predicted value.

Measuring datum: Reference elevation or surface from which level is reported.

Traceability: Property of a result that can be related to a reference through documented calibrations.

Review Questions

Short Answer Questions

  1. Distinguish accuracy from precision in hydraulic measurement.
  2. What is the difference between gauge pressure and absolute pressure?
  3. Why is a point velocity not automatically equal to mean pipe velocity?
  4. State two limitations of an ultrasonic level sensor.
  5. Why should raw experimental data be preserved in a spreadsheet?

Long Answer Questions

  1. Explain the operating principles, advantages, and limitations of piezometers, manometers, Bourdon gauges, and electronic pressure transducers.
  2. Describe a complete procedure for planning and conducting a discharge experiment in a laboratory pipe system.
  3. Explain calibration, including zero checks, increasing and decreasing runs, hysteresis, residuals, and calibration-range limitations.
  4. Derive the uncertainty relation for discharge calculated from independent measurements of velocity and pipe diameter.
  5. Discuss how a technical report should communicate experimental method, uncertainty, limitations, and conclusions.

Analytical / Application Questions

  1. A full circular pipe has diameter 150 mm and mean velocity 2.0 m/s. Calculate the discharge and explain which assumptions are required.
  2. Five pressure readings are 198, 201, 200, 202, and 199 kPa. Calculate the mean and sample standard deviation, then comment on repeatability.
  3. Design a commissioning test for a pumped construction-site water line. Specify measurands, instruments, calibration checks, stabilization criteria, safety controls, data analysis, and acceptance decision rules.

Multiple Choice Questions with Answers

Question 1

Which equation defines discharge for a velocity field across an area?

A. Q = p/A

B. Q = ∫_A V_n dA

C. Q = ρgH

D. Q = F t

Correct Answer: B. Q = ∫_A V_n dA

Question 2

A pressure of 250 kPa gauge is measured where atmospheric pressure is 101 kPa. What is the approximate absolute pressure?

A. 149 kPa

B. 250 kPa

C. 351 kPa

D. 25.7 kPa

Correct Answer: C. 351 kPa

Question 3

Which instrument is most directly based on liquid-column height?

A. Bourdon-tube gauge

B. Manometer

C. Electromagnetic flow meter

D. Radar level sensor

Correct Answer: B. Manometer

Question 4

A pipe has area 0.005 m² and mean velocity 3 m/s. What is the discharge?

A. 0.00167 m³/s

B. 0.008 m³/s

C. 0.015 m³/s

D. 0.60 m³/s

Correct Answer: C. 0.015 m³/s

Question 5

What does standard deviation primarily describe?

A. The calibration range

B. The spread of repeated observations

C. The absolute pressure

D. The instrument’s response time

Correct Answer: B. The spread of repeated observations

Question 6

For independent uncertainty components, the basic combined uncertainty is commonly calculated using:

A. Their arithmetic product

B. The largest component only

C. The root sum of squares

D. Their subtraction in measurement order

Correct Answer: C. The root sum of squares

Question 7

Why must a pressure measurement specify whether it is gauge or absolute?

A. Because the units change automatically

B. Because the reference pressure differs

C. Because gauge pressure has no sign

D. Because absolute pressure is always zero

Correct Answer: B. Because the reference pressure differs

Question 8

Which spreadsheet practice best supports auditability?

A. Overwriting raw readings with corrected values

B. Removing all unusual observations

C. Separating raw data, calibration, calculations, and results

D. Using unlabeled numerical columns

Correct Answer: C. Separating raw data, calibration, calculations, and results

Question 9

A sensor gives tightly grouped readings that are all 3 kPa higher than the reference. The sensor is best described as:

A. Precise but biased

B. Inaccurate and imprecise necessarily

C. Low-resolution only

D. Uncalibrated in units only

Correct Answer: A. Precise but biased

Question 10

For a circular pipe, if diameter is doubled while mean velocity remains constant, discharge becomes:

A. Half as large

B. Twice as large

C. Four times as large

D. Unchanged

Correct Answer: C. Four times as large

Fluid Mechanics
Chapter 13 of 14