Energy Management

Chapter 4
Energy Auditing and Measurement

Specialization
Energy Management   •   Specialization

Energy Auditing and Measurement

Introduction

Energy auditing is the systematic investigation of how energy enters, is distributed, converted, and used within a facility, process, transport system, or organization. It combines engineering measurement, operational observation, data analysis, and economic evaluation. The purpose is not merely to identify equipment that consumes energy, but to explain why energy is consumed, determine whether consumption is technically justified, and develop reliable opportunities for improvement.

An audit is only as credible as its boundary definition, measurements, assumptions, and documentation. A technically attractive recommendation based on poor measurements may produce a misleading saving estimate. Conversely, a carefully designed preliminary audit can identify low-cost improvements and justify a more detailed investigation.

Energy auditing supports energy-management systems, carbon-reduction programs, maintenance planning, capital investment, regulatory compliance, and operational control. It is therefore both a technical activity and a management process.

Learning Objectives

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

  1. Distinguish preliminary, targeted, and detailed energy audits.
  2. Define audit boundaries, energy streams, baselines, and performance indicators.
  3. Select and use appropriate meters and instruments.
  4. Design representative sampling plans for variable systems.
  5. Apply mass balances, energy balances, and end-use analysis.
  6. Estimate measurement uncertainty and propagate uncertainty into calculated results.
  7. Evaluate energy-saving opportunities technically and economically.
  8. Prepare a defensible audit report and communicate its limitations.

1. Audit Scope, Boundaries, and Levels

1.1 The audit boundary

Before taking measurements, the auditor defines what is included. A boundary may encompass an entire building, a production line, a boiler house, a compressed-air system, or a single process unit. Boundary definition should identify:

  • energy sources entering the boundary;
  • useful products or services leaving it;
  • waste streams and rejected heat;
  • internal transfers between subsystems;
  • operating periods and abnormal conditions;
  • ownership and responsibility for equipment.

A boundary prevents double counting. For example, electricity used by a central chiller should not be counted again as electricity consumed by each served office unless the accounting purpose explicitly requires allocation.

1.2 Levels of audit

A preliminary audit, sometimes called a walk-through audit, uses utility bills, interviews, visual inspection, nameplate data, and limited measurements. It rapidly identifies obvious inefficiencies and determines whether further work is justified.

A targeted audit examines one system or issue, such as boiler efficiency, refrigeration, compressed air, or peak electrical demand. It is narrower than a whole-facility audit but can involve substantial instrumentation.

A detailed audit establishes measured baselines, develops energy and mass balances, quantifies savings, assesses implementation costs, and evaluates financial and operational risks. It normally requires measurements over representative operating conditions and, for variable facilities, over multiple days or production cycles.

An investment-grade audit goes further by reducing uncertainty sufficiently for a financing or performance-contracting decision. It may include calibrated permanent metering, detailed simulation, construction quotations, and measurement-and-verification provisions.

Audit typeMain purposeTypical evidenceTypical output
PreliminaryScreen opportunitiesBills, inspection, interviewsOpportunity register
TargetedDiagnose a systemTemporary meters and operating testsSystem-specific recommendations
DetailedQuantify projectsMetered data, balances, engineering analysisSavings, cost, risks, implementation plan
Investment-gradeSupport financingHigh-quality baseline and cost evidenceBankable project proposal

2. The Audit Process

A professional audit usually follows these stages:

  1. Planning: establish objectives, scope, confidentiality, safety requirements, deliverables, and access to records.
  2. Pre-audit data collection: obtain utility bills, production data, operating schedules, equipment inventories, maintenance records, tariffs, and previous studies.
  3. Site survey: verify equipment, observe operating practices, identify control modes, and locate measurement points.
  4. Measurement plan: select instruments, variables, locations, logging intervals, duration, and quality checks.
  5. Analysis: normalize data, construct balances, calculate performance indicators, and identify causes of losses.
  6. Opportunity evaluation: estimate energy, demand, cost, emissions, investment, interactions, and risks.
  7. Reporting: document methods, data quality, findings, recommendations, assumptions, and limitations.
  8. Follow-up: support implementation and verify actual performance.

The audit is iterative. Early measurements may reveal that the initial boundary or sampling plan is inadequate. Good practice permits the plan to be revised while preserving a clear record of decisions.

3. Energy Accounting and Performance Indicators

3.1 Energy forms and common units

Energy may be purchased as electricity, natural gas, fuel oil, steam, hot water, chilled water, or vehicle fuel. All streams should be expressed in consistent units for comparison. Electrical energy is commonly recorded in kWh, fuels in mass or volume, and thermal energy in MJ, GJ, or kWh-th.

The conversion between electrical energy and joules is:

1 kWh = 3.6 MJ

This conversion does not imply that electricity and fuel have equal economic or environmental value. Tariffs, primary-energy factors, and emission factors must be applied according to the stated analytical purpose.

3.2 Energy balance

For a defined period and system boundary, the general balance is:

Ein = Euseful + Eloss + ΔEstorage

where Ein is energy entering the boundary, Euseful is energy delivered to the intended service or product, Eloss is energy rejected or dissipated, and ΔEstorage is the change in energy stored within the boundary. At steady state, or over a period in which storage change is negligible, ΔEstorage ≈ 0.

For a process with several inputs and outputs, a more explicit expression is:

∑Ein − ∑Eout = ΔEstorage

The balance is an accounting identity; it does not by itself identify the cause of a loss. Measurement error, unmeasured streams, and inconsistent boundaries can also appear as an apparent loss.

3.3 Mass balance

For a nonreactive steady-flow system:

∑ṁin = ∑ṁout

where ṁ is mass flow rate, measured in kg/s or another consistent unit. For a general system:

∑ṁin − ∑ṁout = dM/dt

where M is mass stored within the boundary. Mass balances are essential in boilers, cooling towers, compressed-air systems, water systems, and production processes.

3.4 Useful performance indicators

Energy-use intensity may be defined as:

EUI = E / A

where E is energy consumed over a specified period and A is floor area, usually expressed in m². In manufacturing, a more useful indicator may be:

SEC = E / P

where SEC is specific energy consumption and P is production output, such as tonnes, units, or litres. Indicators must state the period, boundary, product quality, and whether energy is site or source energy.

For equipment converting input energy into useful output:

η = Euseful / Einput

Efficiency is dimensionless when numerator and denominator use compatible energy units. It is meaningful only when the useful output is clearly defined.

4. Measurement and Instrumentation

4.1 Measurement principles

The auditor should measure variables that explain energy use rather than simply collecting large quantities of data. Typical variables include electrical power, voltage, current, power factor, fuel flow, steam pressure and temperature, water flow, air pressure, temperature, humidity, production rate, occupancy, and operating status.

Instrument selection depends on range, accuracy, response time, installation constraints, safety category, data-logging capability, and calibration status. A meter should be suitable for the expected value, not merely capable of measuring it. Operating near the middle of the instrument range generally improves resolution and reduces relative error.

4.2 Common instruments

VariableTypical instrumentImportant precautions
Electrical powerPower analyzer or revenue-grade meterCorrect phase connection and CT orientation
CurrentClamp meter or current transformerConductor access, jaw closure, safety rating
VoltageDigital multimeter or power analyzerCorrect category rating and phase-to-phase selection
Fuel flowPositive-displacement, turbine, ultrasonic, or coriolis meterFluid properties and straight-pipe requirements
Water flowMagnetic or ultrasonic flow meterPipe full condition and installation geometry
TemperatureThermocouple, RTD, infrared cameraEmissivity, contact quality, calibration
PressureManometer or pressure transducerZeroing, impulse-line condition, range
HumidityHygrometer or psychrometerSensor placement and response time
Light levelIlluminance meterCosine response and representative locations

Electrical power in a balanced three-phase system can be estimated by:

P = √3 VL IL cosφ

where P is real power in watts, VL is line-to-line RMS voltage in volts, IL is line current in amperes, and cosφ is power factor. This expression assumes a balanced sinusoidal system. For systems with significant waveform distortion or imbalance, a true-power analyzer should be used rather than relying on this simplified equation.

For a single-phase circuit:

P = V I cosφ

For thermal flow in a liquid circuit:

Q̇ = ṁ cp (Tout − Tin)

where Q̇ is heat-transfer rate in watts, ṁ is mass flow rate in kg/s, cp is specific heat capacity in J/(kg·K), and temperatures are in °C or K differences. The equation assumes negligible phase change, uniform properties, and sufficiently accurate flow and temperature measurements.

For steam or refrigerant systems, enthalpy differences are generally more appropriate:

Q̇ = ṁ (hout − hin)

where h is specific enthalpy in J/kg. Property values should come from a recognized property source or verified reference, not an unsupported estimate.

4.3 Meter installation and data quality

A correct instrument can produce incorrect results if installed poorly. Common causes include turbulence near flow meters, partially filled pipes, heat conduction along temperature probes, incorrect current-transformer polarity, loose electrical connections, sensor drift, and logging intervals that miss short demand peaks.

Every measurement record should include instrument identification, range, stated accuracy, calibration date, installation point, timestamp, units, logger interval, weather or production conditions, and unusual events. Photographs and sketches are valuable evidence.

5. Sampling and Data Collection

A measurement period must represent the operating condition for which the recommendation will be made. A single instantaneous reading is often inadequate for cycling equipment, variable production, intermittent occupancy, or demand-sensitive tariffs.

Sampling design should address:

  • population: the equipment, days, shifts, or products being studied;
  • sampling unit: a reading, operating cycle, shift, or production batch;
  • stratification: division into operating modes, seasons, production levels, or occupancy states;
  • frequency: interval between observations;
  • duration: total time needed to capture variability;
  • missing data: rules for flagging, estimating, or excluding records.

For a mean estimated from independent observations, the standard error is:

SE(ȳ) = s / √n

where ȳ is the sample mean, s is sample standard deviation, and n is sample size. This relationship assumes observations are sufficiently independent. Autocorrelated time-series data contain less independent information than their record count suggests.

For a proportion when a simple random sample is appropriate, a commonly used planning approximation is:

n = z² p(1 − p) / e²

where n is required sample size, z is the standard-normal value for the selected confidence level, p is the anticipated proportion, and e is the allowable absolute error. In energy audits, this formula is only a starting point; operating regimes, finite populations, cost, and time dependence may require a different design.

A practical approach is to first collect exploratory data, examine variability, divide the system into meaningful operating modes, and then extend logging until the data cover all relevant conditions.

6. Measurement Uncertainty

6.1 Accuracy, precision, and uncertainty

Accuracy describes closeness to a reference value; precision describes repeatability. Measurement uncertainty expresses the plausible range associated with a result. It includes instrument specification, calibration, installation, environmental effects, resolution, repeatability, and model assumptions.

If independent uncertainty components are represented by standard uncertainties u1, u2, …, the combined standard uncertainty is often estimated by root-sum-square:

uc = √(u1² + u2² + ⋯ + uk²)

This assumes the components are independent or uncorrelated. If correlation exists, covariance terms should be included:

uc² = ∑(∂f/∂xi)²ui² + 2∑i<j(∂f/∂xi)(∂f/∂xj)ui uj rij

where y = f(x1, x2, …, xn), rij is the correlation coefficient, and partial derivatives describe sensitivity to each input. The covariance form is important when measurements share a reference or systematic influence.

For a result reported with expanded uncertainty:

U = k uc

where k is a coverage factor selected for the desired coverage probability and distributional assumptions. A value near 2 is commonly used for approximately 95% coverage under suitable conditions, but it is not universally valid.

6.2 Example: uncertainty in thermal energy

A water-heating system has measured mass flow ṁ = 2.00 ± 0.04 kg/s, temperature rise ΔT = 25.0 ± 0.5 K, and cp = 4.18 kJ/(kg·K). Assuming independent uncertainties and treating the heat capacity as exact for this illustration:

Q̇ = 2.00 × 4.18 × 25.0 = 209 kW

The relative standard uncertainty is approximately:

uQ/Q̇ = √[(0.04/2.00)² + (0.5/25.0)²] = 0.0283

Thus, the standard uncertainty is approximately uQ = 209 × 0.0283 = 5.9 kW. An approximate expanded uncertainty with k = 2 is ±11.8 kW, giving a result of approximately 209 ± 12 kW under the stated assumptions. The example demonstrates why a seemingly small temperature uncertainty can materially affect a calculated heat rate.

7. Baselines, Normalization, and Savings

A baseline is the reference energy performance against which improvement is assessed. It may be a historical period, a calibrated model, a control group, or a pre-project operating condition. The baseline must account for relevant independent variables such as production, weather, occupancy, operating hours, and product mix.

A simple production-normalized indicator is useful only when energy is approximately proportional to production and fixed loads are small. A more realistic linear model may be written as:

E = a + bP

where E is energy use, P is production, a is estimated fixed energy, and b is variable energy per unit of production. The model should be checked using residuals, adequate data range, and operational knowledge. Correlation alone does not establish causation.

Weather-dependent buildings may use temperature-based variables such as heating degree-days or cooling degree-days. Savings should be calculated using comparable conditions, not simply by subtracting two uncontrolled bills.

For a proposed efficiency measure:

Esaving = Ebaseline − Epost

where both terms refer to the same boundary, period, and normalized operating conditions. If demand charges, fuel tariffs, export credits, or interactive effects are relevant, energy savings and monetary savings must be calculated separately.

8. Identifying and Evaluating Energy-Saving Opportunities

Opportunities commonly arise from five mechanisms:

  1. reducing unnecessary demand;
  2. improving conversion efficiency;
  3. recovering waste energy;
  4. improving control and scheduling;
  5. replacing equipment or changing the process.

Each opportunity should state the affected equipment, mechanism of saving, implementation action, expected energy and demand effects, investment, operating impact, technical life, and risks.

A simple payback period is:

SPP = C0 / Sa

where C0 is initial investment and Sa is annual monetary saving. Simple payback ignores discounting, taxes, residual value, degradation, and savings after payback. For larger decisions, discounted cash flow methods are preferable. Net present value is:

NPV = −C0 + ∑[CFt/(1+r)t]

where CFt is net cash flow in year t, r is the discount rate, and the summation covers the project life. Energy-price escalation and maintenance costs should be included only when supported by explicit assumptions.

Interactions must be considered. For example, reducing lighting load may reduce cooling demand but may increase heating demand in a cold climate. Lowering compressed-air pressure may save compressor energy but could affect product quality. A technically efficient measure is not acceptable if it creates an uncontrolled safety or production risk.

9. Applied Case: Illustrative Manufacturing Audit

Background

The following is an illustrative case. A food-processing plant operates two shifts per day and purchases electricity and natural gas. Management suspects that the compressed-air system and hot-water generation are inefficient.

Problem and initial investigation

Utility bills show annual electricity use of 1,200 MWh and gas use of 18,000 GJ. Production varies by month, so annual totals alone cannot establish performance. A preliminary walk-through identifies three compressors, an oversized air receiver, an operating pressure higher than several machines require, and simultaneous heating and cooling in one process area.

Measurement plan

The audit team installs a three-phase power logger on each compressor for fourteen days, records discharge pressure and compressor status, measures night-time flow using an ultrasonic meter, and records production by shift. For the hot-water loop, flow and supply/return temperatures are logged at five-minute intervals. Instrument ranges and calibration information are recorded before installation.

Analysis

The compressor data show that one machine remains loaded during low-production periods. Night-time flow is 18% of daytime flow, indicating leaks or open-use points. Pressure reduction tests show that the critical process remains within its required operating range at a lower header pressure. However, the pressure test is conducted only during normal production; it must be repeated during start-up and the most demanding product changeover before implementation.

The hot-water data show that the measured heat delivered is substantially below the gas input implied by the boiler meter. The difference may represent stack loss, jacket loss, distribution loss, cycling loss, or meter-boundary mismatch. The team therefore avoids describing the entire difference as recoverable saving. Combustion testing and flue-temperature measurements are recommended before specifying a heat-recovery project.

Solution package

The recommended sequence is:

  1. repair leaks and eliminate inappropriate open blowing;
  2. install automatic compressor sequencing;
  3. reduce header pressure only after verifying end-use requirements;
  4. improve insulation and control of the hot-water distribution system;
  5. investigate boiler combustion and heat recovery with a targeted audit.

The first two measures require modest investment and have low production risk. The pressure reduction is conditional on validation. Heat recovery is deferred until the energy balance closes within an acceptable uncertainty range.

Outcome and learning points

The case illustrates that a credible audit distinguishes measured facts from hypotheses. It also demonstrates the importance of operating modes, system interactions, measurement boundaries, and staged implementation. The best recommendation is not always the one with the largest theoretical saving; it is the one whose saving, cost, risk, and verification method are sufficiently understood.

10. Audit Reporting and Professional Practice

A professional report should be reproducible by another competent analyst. A useful structure is:

  • executive summary and decision requests;
  • facility description and audit objectives;
  • scope, boundaries, exclusions, and dates;
  • energy and production data sources;
  • instrumentation and calibration information;
  • measurement plan and sampling limitations;
  • baseline and normalization method;
  • energy and mass balances;
  • identified opportunities;
  • savings, uncertainty, cost, and economic analysis;
  • implementation sequence and responsibilities;
  • measurement-and-verification plan;
  • appendices containing raw data, calculations, drawings, and assumptions.

Recommendations should be prioritized using criteria such as saving potential, investment, payback or NPV, operational risk, ease of implementation, maintenance requirements, safety, and strategic value. Reported precision should not exceed the quality of the evidence. A calculated saving of 1.237% is not credible if the baseline uncertainty is ±5%.

Auditors have ethical duties to disclose conflicts of interest, protect confidential operational information, distinguish observed conditions from estimates, and avoid overstating savings. Measurements involving energized equipment, pressure systems, hot surfaces, confined spaces, or process chemicals require appropriate permits, personal protective equipment, and competent personnel. Applicable electrical, pressure-vessel, environmental, metering, and occupational-safety requirements must be checked in the relevant jurisdiction.

11. Digital Tools, Automation, and Emerging Practice

Submetering, cloud loggers, building-management systems, digital twins, and machine-learning anomaly detection can improve audit speed and persistence. Automated analytics can identify baseload changes, simultaneous heating and cooling, unusual demand peaks, and equipment cycling. However, algorithms inherit errors from sensors, missing data, biased training data, and changing operating conditions.

AI-generated diagnoses should be treated as screening evidence, not as a substitute for engineering verification. Data governance should address cybersecurity, access control, retention, ownership, privacy, and traceability. A model should be validated against measured performance and should expose uncertainty rather than presenting a false impression of precision.

Contemporary audits increasingly integrate energy, carbon, water, and production data. This broader perspective is valuable, but the audit boundary must remain explicit. A reduction in site electricity may increase embodied emissions or water use elsewhere; decisions should therefore state the selected system boundary and environmental accounting method.

Best-Practice Checklist

Before closing an audit, confirm that:

  • the boundary and exclusions are explicit;
  • all major energy streams are identified;
  • meters are appropriate, safe, and documented;
  • data cover relevant operating modes;
  • units and conversion factors are consistent;
  • balances are checked and unexplained residuals investigated;
  • uncertainty is reported where it affects decisions;
  • savings are normalized to comparable conditions;
  • interactions and operational risks are assessed;
  • recommendations have owners, costs, priorities, and verification methods;
  • conclusions distinguish measurements, calculations, assumptions, and professional judgment.

Chapter Summary

Energy auditing is a structured process for understanding energy flows and converting evidence into practical decisions. Preliminary audits screen opportunities; targeted and detailed audits diagnose systems and quantify savings; investment-grade audits support financing. Reliable work begins with clear boundaries, consistent units, representative sampling, suitable instrumentation, and documented operating conditions.

Mass and energy balances provide the accounting framework, while performance indicators connect consumption to useful output, area, occupancy, or production. Metering must address installation quality, calibration, range, sampling interval, and safety. Measurement uncertainty should be estimated and propagated, especially when savings depend on differences between measured quantities. Baselines must be normalized for production, weather, occupancy, and other relevant variables.

An effective audit report is transparent, reproducible, and decision-oriented. It communicates technical potential together with cost, risk, uncertainty, implementation requirements, and verification methods. Digital tools and AI can strengthen monitoring and anomaly detection, but professional judgment, data governance, and field verification remain essential.

Key Terms

Audit boundary: Defined physical, organizational, and temporal limits of an audit.

Baseline: Reference energy performance used for comparison.

Calibration: Comparison and adjustment of an instrument against a recognized reference.

Coverage factor: Multiplier used to obtain expanded uncertainty from standard uncertainty.

Detailed audit: Investigation using measurements and analysis sufficient to quantify opportunities.

Energy balance: Accounting relationship between energy entering, leaving, being used, and stored.

Energy-use intensity: Energy consumption per unit of area, output, or another reference variable.

Expanded uncertainty: Uncertainty interval obtained by multiplying combined standard uncertainty by a coverage factor.

Mass balance: Accounting relationship between mass entering, leaving, and accumulating.

Measurement-and-verification: Process for determining whether implemented savings have occurred.

Normalization: Adjustment of energy data to comparable operating or external conditions.

Power factor: Ratio of real power to apparent power in an electrical system.

Preliminary audit: Initial survey using limited measurements to screen opportunities.

Sampling: Planned selection of observations intended to represent a larger population or operating period.

Specific energy consumption: Energy consumed per unit of production or service.

Standard uncertainty: Uncertainty expressed as an estimated standard deviation.

Targeted audit: Investigation focused on a particular system or problem.

True power: Actual average electrical power transferred to a load.

Uncertainty propagation: Calculation of how input uncertainties affect a reported result.

Useful energy: Energy delivered to the intended service or productive output.

Review Questions

Short Answer Questions

  1. What is the purpose of defining an audit boundary?
  2. Distinguish accuracy, precision, and measurement uncertainty.
  3. State two conditions under which a single spot measurement may be misleading.
  4. What information should accompany a logged measurement?
  5. Why should energy savings be normalized for production or weather?

Long Answer Questions

  1. Explain the differences among preliminary, targeted, detailed, and investment-grade audits.
  2. Describe how you would design a measurement plan for a variable compressed-air system.
  3. Explain the role and limitations of mass and energy balances in an audit.
  4. Discuss how uncertainty should influence the presentation of an energy-saving opportunity.
  5. Develop a recommended structure for a professional energy-audit report and justify each major section.

Analytical / Application Questions

  1. A pump system has measured flow, pressure, and electrical input that vary by operating mode. Design a sampling and calculation method for estimating annual efficiency, stating the assumptions and uncertainty issues you would address.
  2. A factory’s energy use rises while production also rises. Explain how you would determine whether energy performance improved, using a baseline model and appropriate normalization.
  3. An audit identifies a large difference between fuel input and measured useful heat. Propose a diagnostic sequence that separates measurement error, conversion loss, distribution loss, and genuine saving potential.

Multiple Choice Questions with Answers

Question 1

Which audit level is primarily intended to screen opportunities using bills, interviews, visual inspection, and limited measurements?

A. Preliminary audit

B. Investment-grade audit

C. Commissioning audit

D. Forensic audit

Correct Answer: A. Preliminary audit

Question 2

For a steady-state system with negligible storage change, which relationship represents the energy balance?

A. E_in = E_useful + E_loss

B. E_in = E_useful − E_loss

C. E_loss = E_in + E_useful

D. E_useful = E_in + E_loss

Correct Answer: A. E_in = E_useful + E_loss

Question 3

A thermal system has mass flow 2 kg/s, specific heat 4 kJ/(kg·K), and temperature rise 10 K. What is the heat-transfer rate?

A. 8 kW

B. 20 kW

C. 80 kW

D. 800 kW

Correct Answer: C. 80 kW

Question 4

Which condition most clearly requires a true-power analyzer rather than reliance on the simplified balanced three-phase equation?

A. A balanced sinusoidal load

B. A purely resistive single-phase heater

C. A system with significant waveform distortion and phase imbalance

D. A constant-voltage DC circuit

Correct Answer: C. A system with significant waveform distortion and phase imbalance

Question 5

If independent standard uncertainties are present, which method is commonly used to combine them?

A. Simple addition of all nominal values

B. Root-sum-square combination

C. Division by the number of variables

D. Selection of the largest measured value

Correct Answer: B. Root-sum-square combination

Question 6

In the baseline model E = a + bP, what does b represent?

A. Fixed energy use

B. Production-independent uncertainty

C. Variable energy use per unit of production

D. The discount rate

Correct Answer: C. Variable energy use per unit of production

Question 7

Why is night-time compressed-air flow often measured during an audit?

A. To determine boiler stack temperature

B. To estimate standby losses, leaks, or inappropriate use

C. To calculate lighting illuminance

D. To measure building occupancy directly

Correct Answer: B. To estimate standby losses, leaks, or inappropriate use

Question 8

A project costs $50,000 and produces annual monetary savings of $10,000. What is its simple payback period?

A. 0.2 years

B. 2 years

C. 5 years

D. 50 years

Correct Answer: C. 5 years

Question 9

Which statement about a mass balance for a general system is correct?

A. Input mass always equals output mass regardless of storage

B. Input minus output equals the rate of mass accumulation

C. Output mass must exceed input mass

D. Mass balance applies only to electrical systems

Correct Answer: B. Input minus output equals the rate of mass accumulation

Question 10

Which reporting practice is most professionally defensible?

A. Reporting more decimal places to appear precise

B. Presenting estimated savings without assumptions

C. Separating measured facts, calculations, assumptions, and limitations

D. Excluding unfavorable measurement results

Correct Answer: C. Separating measured facts, calculations, assumptions, and limitations

Energy Management
Chapter 4 of 14