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FE Chemical Practice Problems: 17 Free Questions with Solutions

17 free worked problems across 17 knowledge areas, with handbook references and explanations of every wrong choice. 110 original four-choice problems mapped to the current FE Chemical knowledge areas, with complete worked solutions.

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Material and energy balances, transport phenomena, thermodynamics, separations, reaction engineering, process design, controls, and safety account for 80 of this form's 110 problems.

FE Chemical is one of the seven NCEES Fundamentals of Engineering (FE) exams. In most U.S. states, passing the FE exam with an accredited degree is the step to Engineer in Training (EIT) or Engineer Intern (EI) certification.

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Form A

105 pages · Version 1.1.0

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FE Chemical Form A: The knowledge-area score sheet included in the PDF
Score sheetForm A · direct PDF render

Mathematics

1 free problem · Form A: 7 of 110 questions · NCEES range: 6-9

A concentration follows ln⁡C=1.20−0.035t\ln C=1.20-0.035t, with t in minutes. The time when C=2.0 is most nearly:

  1. (A)14.5 min
  2. (B)19.8 min
  3. (C)25.7 min
  4. (D)34.3 min
Show worked solution

Answer: (A)

Solving ln⁡2=1.20−0.035t\ln2=1.20-0.035t gives t=14.5 min.

The target concentration fixes the left side of the linear logarithmic model.

0.6931=1.20−0.035t0.6931=1.20-0.035t

Isolating time gives the crossing point.

t=(1.20−0.6931)/0.035=14.5 mint=(1.20-0.6931)/0.035=14.5\ \text{min}

FE Reference Handbook — Mathematics: Logarithms

Why the other choices appear

  • (B)Dropping the 1.20 intercept leaves ln 2 = -0.035t, whose magnitude, 19.8 min, ignores where the model starts.
  • (C)Using log10 2 = 0.301 in place of ln 2 gives 25.7 min.
  • (D)Dividing the intercept alone by the decay coefficient gives 34.3 min and ignores the target concentration.

The complete practice exam contains 7 mathematics problems in Form A, with full solutions and a knowledge-area score sheet.

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Probability and Statistics

1 free problem · Form A: 4 of 110 questions · NCEES range: 4-6

A normally distributed assay has mean 50 and standard deviation 4. Using P(Z>1.5)=0.0668, the probability an assay exceeds 56 is most nearly:

  1. (A)0.0668
  2. (B)0.134
  3. (C)0.433
  4. (D)0.933
Show worked solution

Answer: (A)

The standardized value is (56-50)/4=1.5, so the requested upper-tail probability is 0.0668.

Standardization measures distance from the mean in standard deviations.

z=(56−50)/4=1.5z=(56-50)/4=1.5

The supplied upper-tail area applies directly.

P(X>56)=P(Z>1.5)=0.0668P(X>56)=P(Z>1.5)=0.0668

FE Reference Handbook — Probability: Normal Distribution

Why the other choices appear

  • (B)Doubling the one-tail probability gives the two-tail probability outside plus-or-minus 1.5.
  • (C)Subtracting the upper-tail area from one-half gives the area between mean and z=1.5.
  • (D)Using the lower cumulative probability answers X less than 56.

The complete practice exam contains 4 probability and statistics problems in Form A, with full solutions and a knowledge-area score sheet.

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Engineering Sciences

1 free problem · Form A: 5 of 110 questions · NCEES range: 4-6

A 20 kg drum is pulled horizontally with 100 N while kinetic friction is 30 N. Its acceleration is most nearly:

  1. (A)3.5 m/s²
  2. (B)5 m/s²
  3. (C)6.5 m/s²
  4. (D)70 m/s²
Show worked solution

Answer: (A)

Net force is 70 N, so acceleration is 70/20=3.5 m/s².

Collinear forces combine before applying Newton's second law.

Fnet=100−30=70 NF_{net}=100-30=70\ \text{N}

Mass converts net force to acceleration.

a=Fnet/m=70/20=3.5 m/s2a=F_{net}/m=70/20=3.5\ \text{m/s}^2

FE Reference Handbook — Engineering Sciences: Force, Mass, and Acceleration

Why the other choices appear

  • (B)Ignoring friction gives 100/20=5 m/s².
  • (C)Adding the friction to the applied force gives 130/20 = 6.5 m/s².
  • (D)Reporting net force as acceleration omits mass.

The complete practice exam contains 5 engineering sciences problems in Form A, with full solutions and a knowledge-area score sheet.

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Materials Science

1 free problem · Form A: 4 of 110 questions · NCEES range: 4-6

A fully restrained steel member is heated 60 degrees C. With E=200 GPa and thermal expansion coefficient 12e-6 per degree C, compressive thermal stress magnitude is most nearly:

  1. (A)144 MPa
  2. (B)288 MPa
  3. (C)720 MPa
  4. (D)1,440 MPa
Show worked solution

Answer: (A)

Full restraint converts free thermal strain alpha delta T into stress E alpha delta T=144 MPa compression.

The member's prevented free strain is alpha times temperature change.

ϵT=12×10−6(60)=7.2×10−4\epsilon_T=12\times10^{-6}(60)=7.2\times10^{-4}

Elastic stress balances that restrained strain.

∣σ∣=EϵT=200000(7.2×10−4)=144 MPa|\sigma|=E\epsilon_T=200000(7.2\times10^{-4})=144\ \text{MPa}

FE Reference Handbook — Materials Science: Thermal Stress

Why the other choices appear

  • (B)Using the areal coefficient 2α for a one-dimensional member doubles the stress to 288 MPa.
  • (C)720 is the restrained strain in microstrain, 12e-6 × 60, not a stress in MPa.
  • (D)Reading α as 12e-5 instead of 12e-6 gives 1,440 MPa.

The complete practice exam contains 4 materials science problems in Form A, with full solutions and a knowledge-area score sheet.

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Chemistry and Biology

1 free problem · Form A: 8 of 110 questions · NCEES range: 7-11

A buffer contains 0.20 M acetate and 0.10 M acetic acid. With pK_a=4.76, pH is most nearly:

  1. (A)4.46
  2. (B)4.76
  3. (C)5.06
  4. (D)5.36
Show worked solution

Answer: (C)

Henderson-Hasselbalch gives pH=4.76+log(2)=5.06.

Buffer pH depends on the conjugate-base to weak-acid ratio.

pH=pKa+log⁡([A−]/[HA])pH=pK_a+\log([A^-]/[HA])

The concentration ratio is two.

pH=4.76+log⁡(2)=5.061pH=4.76+\log(2)=5.061

FE Reference Handbook — Chemistry: Buffers

Why the other choices appear

  • (A)Inverting the base-to-acid ratio subtracts log 2 instead of adding it.
  • (B)Equal pH and pKa applies only when base and acid concentrations are equal.
  • (D)Squaring the 2:1 ratio, log 4 = 0.602, overstates the correction and gives 5.36.

The complete practice exam contains 8 chemistry and biology problems in Form A, with full solutions and a knowledge-area score sheet.

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Fluid Mechanics and Dynamics

1 free problem · Form A: 9 of 110 questions · NCEES range: 8-12

A liquid of density 850 kg/m³ and viscosity 0.012 Pa s flows at 1.8 m/s in a 40 mm pipe. Reynolds number is most nearly:

  1. (A)6
  2. (B)2,550
  3. (C)5,100
  4. (D)5,100,000
Show worked solution

Answer: (C)

Re=rho V D/mu=5,100.

Pipe Reynolds number compares inertial and viscous effects.

Re=ρVDμRe=\frac{\rho VD}{\mu}

The diameter is 0.040 m.

Re=850(1.8)(0.040)/0.012=5100Re=850(1.8)(0.040)/0.012=5100

FE Reference Handbook — Fluid Mechanics: Reynolds Number

Why the other choices appear

  • (A)Leaving out the density treats the dynamic viscosity as kinematic and gives 6.0.
  • (B)Using the 20 mm radius instead of the diameter halves the Reynolds number.
  • (D)Entering the diameter as 40 (millimetres) gives 5,100,000.

The complete practice exam contains 9 fluid mechanics and dynamics problems in Form A, with full solutions and a knowledge-area score sheet.

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Thermodynamics

1 free problem · Form A: 9 of 110 questions · NCEES range: 8-12

An ideal-gas mixture at 500 kPa contains 30 mol% component A. Its partial pressure is most nearly:

  1. (A)150 kPa
  2. (B)214 kPa
  3. (C)350 kPa
  4. (D)500 kPa
Show worked solution

Answer: (A)

Dalton's law gives p_A=y_A P=0.30(500)=150 kPa.

Ideal-mixture partial pressure is proportional to mole fraction.

pA=yAPp_A=y_AP

The component occupies 30% of the total moles.

pA=0.30(500)=150 kPap_A=0.30(500)=150\ \text{kPa}

FE Reference Handbook — Thermodynamics: Ideal-Gas Mixtures

Why the other choices appear

  • (B)Using the mole ratio 30/70 instead of the mole fraction gives 214 kPa.
  • (C)Using component B's 70% fraction gives B's partial pressure.
  • (D)Reporting the total pressure ignores the mixture composition.

The complete practice exam contains 9 thermodynamics problems in Form A, with full solutions and a knowledge-area score sheet.

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Material and Energy Balances

1 free problem · Form A: 12 of 110 questions · NCEES range: 10-15

A steady mixer combines 100 kg/h solution containing 10 wt% solute with 50 kg/h solution containing 30 wt% solute. Product solute mass fraction is most nearly:

  1. (A)0.1
  2. (B)0.167
  3. (C)0.2
  4. (D)0.3
Show worked solution

Answer: (B)

Solute flow is 10+15=25 kg/h in 150 kg/h product, so mass fraction is 0.1667.

Total and solute balances both apply to the nonreactive mixer.

m˙P=100+50=150 kg/h\dot m_P=100+50=150\ \text{kg/h}
m˙s=100(0.10)+50(0.30)=25 kg/h\dot m_s=100(0.10)+50(0.30)=25\ \text{kg/h}

Product composition is component flow divided by total flow.

ws=25/150=0.1667w_s=25/150=0.1667

FE Reference Handbook — Material Balances: Steady Mixing

Why the other choices appear

  • (A)Using only the dilute feed composition ignores the concentrated stream.
  • (C)Taking an unweighted average ignores unequal feed flow rates.
  • (D)Using only the concentrated feed composition ignores dilution.

The complete practice exam contains 12 material and energy balances problems in Form A, with full solutions and a knowledge-area score sheet.

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Heat Transfer

1 free problem · Form A: 9 of 110 questions · NCEES range: 8-12

A lumped solid initially at 200 degrees C cools in 25 degrees C air. Its time constant is 10 min. Temperature after 20 min is most nearly:

  1. (A)27.1 degrees C
  2. (B)48.7 degrees C
  3. (C)68.8 degrees C
  4. (D)131 degrees C
Show worked solution

Answer: (B)

The excess temperature decays as exp(-t/tau); after two time constants T=48.7 degrees C.

Lumped cooling is first order in temperature excess above ambient.

T−T∞=(Ti−T∞)e−t/τT-T_\infty=(T_i-T_\infty)e^{-t/\tau}

Here t/tau=2.

T=25+175e−2=48.7∘CT=25+175e^{-2}=48.7^\circ\text{C}

FE Reference Handbook — Heat Transfer: Lumped Transient Analysis

Why the other choices appear

  • (A)Applying the decay to 200 degrees C instead of the 175 K excess over ambient gives 27.1 degrees C.
  • (C)Treating the time constant as a half-life leaves a quarter of the excess, 68.8 degrees C.
  • (D)Inverting t/τ to 0.5 gives 131 degrees C.

The complete practice exam contains 9 heat transfer problems in Form A, with full solutions and a knowledge-area score sheet.

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Mass Transfer and Separation

1 free problem · Form A: 9 of 110 questions · NCEES range: 8-12

A solute diffuses through a stagnant liquid film 1.0 mm thick. Diffusivity is 1.0e-9 m²/s and concentration difference is 2.0 kmol/m³. Steady flux magnitude is most nearly:

  1. (A)2.0 × 10⁻⁹ kmol/(m² s)
  2. (B)2.0 × 10⁻⁶ kmol/(m² s)
  3. (C)2.0 × 10⁻³ kmol/(m² s)
  4. (D)2,000 kmol/(m² s)
Show worked solution

Answer: (B)

Fick's law gives N=D delta C/L=2.0e-6 kmol/(m² s).

A linear steady concentration profile gives constant diffusive flux.

∣NA∣=DAB∣CA1−CA2∣L|N_A|=D_{AB}\frac{|C_{A1}-C_{A2}|}{L}

The film thickness is 0.0010 m.

∣NA∣=10−9(2.0)/0.0010=2.0×10−6 kmol/(m2 s)|N_A|=10^{-9}(2.0)/0.0010=2.0\times10^{-6}\ \text{kmol/(m}^2\text{ s)}

FE Reference Handbook — Mass Transfer: Fick's First Law

Why the other choices appear

  • (A)Leaving out the film thickness gives D times delta C = 2.0 × 10⁻⁹.
  • (C)Converting 2.0 kmol/m³ to 2,000 mol/m³ but keeping kmol in the unit gives 2.0 × 10⁻³.
  • (D)Leaving out the diffusivity gives the concentration gradient, 2,000 kmol/m4.

The complete practice exam contains 9 mass transfer and separation problems in Form A, with full solutions and a knowledge-area score sheet.

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Solids Handling

1 free problem · Form A: 3 of 110 questions · NCEES range: 3-5

A powder has equal mass fractions of 100 micrometer and 400 micrometer particles of equal density and shape. Sauter mean diameter d32=1/sum(w_i/d_i) is most nearly:

  1. (A)100 micrometer
  2. (B)160 micrometer
  3. (C)250 micrometer
  4. (D)400 micrometer
Show worked solution

Answer: (B)

d32=1/(0.5/100+0.5/400)=160 micrometres.

The surface-volume mean weights inverse diameter by mass fraction for equal density.

1/d32=∑wi/di1/d_{32}=\sum w_i/d_i

The inverse mean is 0.00625 per micrometre.

d32=1/(0.005+0.00125)=160 μmd_{32}=1/(0.005+0.00125)=160\ \mu\text{m}

FE Reference Handbook — Solids Handling: Particle Size Distributions

Why the other choices appear

  • (A)Using only the fine fraction ignores coarse particles.
  • (C)Taking an arithmetic mean does not give surface-volume mean diameter.
  • (D)Using only the coarse fraction ignores the added surface from fines.

The complete practice exam contains 3 solids handling problems in Form A, with full solutions and a knowledge-area score sheet.

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Chemical Reaction Engineering

1 free problem · Form A: 8 of 110 questions · NCEES range: 7-11

When reactant concentration doubles, measured initial rate increases by a factor of four at constant temperature. Reaction order in that reactant is most nearly:

  1. (A)0.5
  2. (B)1
  3. (C)2
  4. (D)4
Show worked solution

Answer: (C)

For r proportional to C^n, 4=2^n, so n=2.

Rate ratios eliminate the constant rate coefficient.

r2/r1=(C2/C1)nr_2/r_1=(C_2/C_1)^n

The observed ratios are four and two.

4=2n4=2^n
n=2n=2

FE Reference Handbook — Reaction Engineering: Rate Laws and Order

Why the other choices appear

  • (A)Taking the square root of the rate ratio gives concentration ratio, not order.
  • (B)First order would double rate when concentration doubles.
  • (D)Using the rate factor directly as order ignores exponentiation.

The complete practice exam contains 8 chemical reaction engineering problems in Form A, with full solutions and a knowledge-area score sheet.

Compare Form A and buy a PDF · USD 29All knowledge areas

Economics

1 free problem · Form A: 4 of 110 questions · NCEES range: 4-6

A product sells for USD 50/unit, variable cost is USD 30/unit, and annual fixed cost is USD 240,000. Break-even annual production is most nearly:

  1. (A)4,800 units/yr
  2. (B)8,000 units/yr
  3. (C)12,000 units/yr
  4. (D)600,000 units/yr
Show worked solution

Answer: (C)

Contribution margin is USD 20/unit, so break-even volume is 240,000/20=12,000 units/yr.

At break-even, total contribution equals fixed cost.

QBE=F/(p−v)Q_{BE}=F/(p-v)

Selling price minus variable cost is USD 20/unit.

QBE=240000/(50−30)=12000 units/yrQ_{BE}=240000/(50-30)=12000\ \text{units/yr}

FE Reference Handbook — Economics: Break-Even Analysis

Why the other choices appear

  • (A)Dividing the fixed cost by the selling price ignores the variable cost.
  • (B)Dividing the fixed cost by the variable cost does not use the contribution margin.
  • (D)USD 600,000 is the break-even revenue, 240,000/0.40, not a production volume.

The complete practice exam contains 4 economics problems in Form A, with full solutions and a knowledge-area score sheet.

Compare Form A and buy a PDF · USD 29All knowledge areas

Process Design

1 free problem · Form A: 7 of 110 questions · NCEES range: 7-11

A continuous process requires 30 min nominal liquid residence time at 0.020 m³/s. Ignoring holdup corrections, vessel working volume is most nearly:

  1. (A)0.6 m³
  2. (B)21.6 m³
  3. (C)36 m³
  4. (D)72 m³
Show worked solution

Answer: (C)

Working volume is flow times residence time: 0.020(1,800)=36 m³.

Nominal residence time is inventory divided by volumetric throughput.

τ=V/Q\tau=V/Q

Thirty minutes equals 1,800 seconds.

V=0.020(1800)=36 m3V=0.020(1800)=36\ \text{m}^3

FE Reference Handbook — Process Design: Equipment Sizing

Why the other choices appear

  • (A)Using 30 seconds instead of 30 minutes understates the volume sixtyfold.
  • (B)Reading 30 min as 0.30 h (1,080 s) gives 21.6 m^3.
  • (D)Using 3,600 s, one hour, instead of 1,800 s doubles the volume.

The complete practice exam contains 7 process design problems in Form A, with full solutions and a knowledge-area score sheet.

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Process Control

1 free problem · Form A: 4 of 110 questions · NCEES range: 4-6

A process transfer function is G(s)=6/(4s+1)G(s)=6/(4s+1). Its time constant is:

  1. (A)1 min
  2. (B)4 min
  3. (C)6 min
  4. (D)24 min
Show worked solution

Answer: (B)

Comparing G=K/(tau s+1) gives gain K=6 and time constant tau=4 min.

The standard first-order form exposes both parameters directly.

G(s)=K/(τs+1)G(s)=K/(\tau s+1)

Coefficient comparison gives K=6 and tau=4.

K=6K=6
τ=4 min\tau=4\ \text{min}

FE Reference Handbook — Process Control: Transfer Functions

Why the other choices appear

  • (A)The denominator constant is normalized to one and is not the time constant.
  • (C)The numerator is gain, not time constant.
  • (D)Multiplying the gain by the time constant, 6(4) = 24, does not identify either parameter.

The complete practice exam contains 4 process control problems in Form A, with full solutions and a knowledge-area score sheet.

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Safety, Health, and Environment

1 free problem · Form A: 5 of 110 questions · NCEES range: 5-8

A vapor leak enters ventilation air at 2.0 kg/h while clean air flow is 1,000 kg/h. Assuming dilute mixing, vapor mass fraction is most nearly:

  1. (A)5.6 × 10⁻⁷
  2. (B)0.002
  3. (C)0.2
  4. (D)500
Show worked solution

Answer: (B)

Mixed mass fraction is 2/(1,002)=0.001996, about 0.20 wt%.

A dilute steady enclosure balance places leak mass in total exhaust flow.

wv=m˙v/(m˙air+m˙v)w_v=\dot m_v/(\dot m_{air}+\dot m_v)

Total mixed flow is 1,002 kg/h.

wv=2/1002=0.001996w_v=2/1002=0.001996

FE Reference Handbook — Safety: Ventilation and Dispersion

Why the other choices appear

  • (A)Converting only the leak to kg/s (2/3,600) before dividing by the air rate in kg/h mixes time units.
  • (C)0.2 is the vapor content in percent, not a mass fraction.
  • (D)Dividing the air flow by the leak inverts the ratio.

The complete practice exam contains 5 safety, health, and environment problems in Form A, with full solutions and a knowledge-area score sheet.

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Ethics and Professional Practice

1 free problem · Form A: 3 of 110 questions · NCEES range: 3-5

A process engineer discovers that a relief-valve calculation used the wrong reaction heat and the installed valve may be undersized. Startup is scheduled. The engineer should:

  1. (A)Document the error, notify responsible management, and withhold approval until the hazard is resolved
  2. (B)Approve startup because the valve has not yet failed
  3. (C)Delete the calculation and repeat it after startup
  4. (D)Let the equipment vendor decide without disclosing the error
Show worked solution

Answer: (A)

A credible overpressure protection deficiency must be disclosed and resolved before professional startup approval.

Reaction heat directly affects runaway relief load, making the discovered input error material to safety.

A corrected independent relief calculation can verify capacity before startup and create an auditable decision basis.

FE Reference Handbook — Ethics: Public Safety and Objective Reporting

Why the other choices appear

  • (B)Absence of a prior failure does not establish adequate relief capacity for a known scenario.
  • (C)Deleting the calculation conceals evidence and allows an unresolved public-safety risk.
  • (D)Vendor input may help, but the engineer must disclose the basis error and ensure responsible resolution.

The complete practice exam contains 3 ethics and professional practice problems in Form A, with full solutions and a knowledge-area score sheet.

Compare Form A and buy a PDF · USD 29All knowledge areas

What each download contains

Edition
First edition
Form A
105 pages · Version 1.1.0
Questions
110 original problems
Coverage
17 knowledge areas
Question type
Four-choice, single-answer
Format
Print-ready PDF, US Letter

Built against the NCEES FE Chemical specifications effective July 2020, current as of August 2026. Official exam format and appointment facts are available from NCEES. This printable form does not reproduce the Pearson VUE interface or interactive alternative item types.

Verification and corrections

Original problems, checked by a second calculation route

Every answer is reproduced with an alternate formula, a limiting case, a dimensional check, or a direct recomputation before publication. Official examination questions are confidential and are not reproduced or paraphrased.

Confirmed errors are published as versioned corrections. Buyers can re-download the corrected release at no charge. Read the full editorial method.

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105 pages · Version 1.1.0

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