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Baghouse

Environmental Engineering · FE Reference Handbook section

Environmental Engineering
0 formulas
10 exam-style examples
~45 min
All Environmental Engineering lectures

Core formulas for this FE topic

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

This section is conceptual; there are no equations to memorise.

Worked exam-style examples

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

Example 1
Series particulate control: overall collection efficiency and emission rate — Baghouse

A stack gas stream of 23 m³/s carries 19 g/m³ of particulate. It passes a cyclone at 91% efficiency followed by a fabric filter at 94.5% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=23m3/sQ = 23 m^{3}/s
  • Cin=19g/m3C_in = 19 g/m^{3}
  • η1=0.91\eta_{1} = 0.91
  • η2=0.945\eta_{2} = 0.945

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=19(1−0.91)=1.710g/m3C_{1} = 19(1 - 0.91) = 1.710 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=1.710(1−0.945)=0.0941g/m3C_{2} = 1.710(1 - 0.945) = 0.0941 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.090×0.0550=0.99505=99.505\eta = 1 - 0.090 \times 0.0550 = 0.99505 = 99.505%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.0941g/m3×23m3/s×3600s/h÷1000=7.787kg/h0.0941 g/m^{3} \times 23 m^{3}/s \times 3600 s/h \div 1000 = 7.787 kg/h
Answer:
Cout=0.0941g/m3,η=99.51C_out = 0.0941 g/m^{3}, \eta = 99.51%, emission = 7.79 kg/h

Why the other options are there

  • η = 185.5% (efficiencies added)
  • 1,573 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 2
Series particulate control: overall collection efficiency and emission rate — Baghouse (2)

A stack gas stream of 19 m³/s carries 23 g/m³ of particulate. It passes a cyclone at 75% efficiency followed by a fabric filter at 97.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=19m3/sQ = 19 m^{3}/s
  • Cin=23g/m3C_in = 23 g/m^{3}
  • η1=0.75\eta_{1} = 0.75
  • η2=0.970\eta_{2} = 0.970

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=23(1−0.75)=5.750g/m3C_{1} = 23(1 - 0.75) = 5.750 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=5.750(1−0.970)=0.1725g/m3C_{2} = 5.750(1 - 0.970) = 0.1725 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.250×0.0300=0.99250=99.250\eta = 1 - 0.250 \times 0.0300 = 0.99250 = 99.250%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.1725g/m3×19m3/s×3600s/h÷1000=11.799kg/h0.1725 g/m^{3} \times 19 m^{3}/s \times 3600 s/h \div 1000 = 11.799 kg/h
Answer:
Cout=0.1725g/m3,η=99.25C_out = 0.1725 g/m^{3}, \eta = 99.25%, emission = 11.80 kg/h

Why the other options are there

  • η = 172.0% (efficiencies added)
  • 1,573 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 3
Series particulate control: overall collection efficiency and emission rate — Baghouse (3)

A stack gas stream of 48 m³/s carries 9 g/m³ of particulate. It passes a cyclone at 85% efficiency followed by a fabric filter at 97.5% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=48m3/sQ = 48 m^{3}/s
  • Cin=9g/m3C_in = 9 g/m^{3}
  • η1=0.85\eta_{1} = 0.85
  • η2=0.975\eta_{2} = 0.975

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=9(1−0.85)=1.350g/m3C_{1} = 9(1 - 0.85) = 1.350 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=1.350(1−0.975)=0.0338g/m3C_{2} = 1.350(1 - 0.975) = 0.0338 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.150×0.0250=0.99625=99.625\eta = 1 - 0.150 \times 0.0250 = 0.99625 = 99.625%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.0338g/m3×48m3/s×3600s/h÷1000=5.832kg/h0.0338 g/m^{3} \times 48 m^{3}/s \times 3600 s/h \div 1000 = 5.832 kg/h
Answer:
Cout=0.0338g/m3,η=99.63C_out = 0.0338 g/m^{3}, \eta = 99.63%, emission = 5.83 kg/h

Why the other options are there

  • η = 182.5% (efficiencies added)
  • 1,555 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 4
Series particulate control: overall collection efficiency and emission rate — Baghouse (4)

A stack gas stream of 41 m³/s carries 17 g/m³ of particulate. It passes a cyclone at 81% efficiency followed by a fabric filter at 97.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=41m3/sQ = 41 m^{3}/s
  • Cin=17g/m3C_in = 17 g/m^{3}
  • η1=0.81\eta_{1} = 0.81
  • η2=0.970\eta_{2} = 0.970

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=17(1−0.81)=3.230g/m3C_{1} = 17(1 - 0.81) = 3.230 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=3.230(1−0.970)=0.0969g/m3C_{2} = 3.230(1 - 0.970) = 0.0969 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.190×0.0300=0.99430=99.430\eta = 1 - 0.190 \times 0.0300 = 0.99430 = 99.430%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.0969g/m3×41m3/s×3600s/h÷1000=14.302kg/h0.0969 g/m^{3} \times 41 m^{3}/s \times 3600 s/h \div 1000 = 14.302 kg/h
Answer:
Cout=0.0969g/m3,η=99.43C_out = 0.0969 g/m^{3}, \eta = 99.43%, emission = 14.30 kg/h

Why the other options are there

  • η = 178.0% (efficiencies added)
  • 2,509 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 5
Series particulate control: overall collection efficiency and emission rate — Baghouse (5)

A stack gas stream of 10 m³/s carries 16 g/m³ of particulate. It passes a cyclone at 78% efficiency followed by a fabric filter at 99.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=10m3/sQ = 10 m^{3}/s
  • Cin=16g/m3C_in = 16 g/m^{3}
  • η1=0.78\eta_{1} = 0.78
  • η2=0.990\eta_{2} = 0.990

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=16(1−0.78)=3.520g/m3C_{1} = 16(1 - 0.78) = 3.520 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=3.520(1−0.990)=0.0352g/m3C_{2} = 3.520(1 - 0.990) = 0.0352 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.220×0.0100=0.99780=99.780\eta = 1 - 0.220 \times 0.0100 = 0.99780 = 99.780%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.0352g/m3×10m3/s×3600s/h÷1000=1.267kg/h0.0352 g/m^{3} \times 10 m^{3}/s \times 3600 s/h \div 1000 = 1.267 kg/h
Answer:
Cout=0.0352g/m3,η=99.78C_out = 0.0352 g/m^{3}, \eta = 99.78%, emission = 1.27 kg/h

Why the other options are there

  • η = 177.0% (efficiencies added)
  • 576.0 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 6
Series particulate control: overall collection efficiency and emission rate — Baghouse (6)

A stack gas stream of 46 m³/s carries 22 g/m³ of particulate. It passes a cyclone at 84% efficiency followed by a fabric filter at 91.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=46m3/sQ = 46 m^{3}/s
  • Cin=22g/m3C_in = 22 g/m^{3}
  • η1=0.84\eta_{1} = 0.84
  • η2=0.910\eta_{2} = 0.910

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=22(1−0.84)=3.520g/m3C_{1} = 22(1 - 0.84) = 3.520 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=3.520(1−0.910)=0.3168g/m3C_{2} = 3.520(1 - 0.910) = 0.3168 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.160×0.0900=0.98560=98.560\eta = 1 - 0.160 \times 0.0900 = 0.98560 = 98.560%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.3168g/m3×46m3/s×3600s/h÷1000=52.462kg/h0.3168 g/m^{3} \times 46 m^{3}/s \times 3600 s/h \div 1000 = 52.462 kg/h
Answer:
Cout=0.3168g/m3,η=98.56C_out = 0.3168 g/m^{3}, \eta = 98.56%, emission = 52.46 kg/h

Why the other options are there

  • η = 175.0% (efficiencies added)
  • 3,643 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 7
Series particulate control: overall collection efficiency and emission rate — Baghouse (7)

A stack gas stream of 40 m³/s carries 26 g/m³ of particulate. It passes a cyclone at 75% efficiency followed by a fabric filter at 98.5% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=40m3/sQ = 40 m^{3}/s
  • Cin=26g/m3C_in = 26 g/m^{3}
  • η1=0.75\eta_{1} = 0.75
  • η2=0.985\eta_{2} = 0.985

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=26(1−0.75)=6.500g/m3C_{1} = 26(1 - 0.75) = 6.500 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=6.500(1−0.985)=0.0975g/m3C_{2} = 6.500(1 - 0.985) = 0.0975 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.250×0.0150=0.99625=99.625\eta = 1 - 0.250 \times 0.0150 = 0.99625 = 99.625%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.0975g/m3×40m3/s×3600s/h÷1000=14.040kg/h0.0975 g/m^{3} \times 40 m^{3}/s \times 3600 s/h \div 1000 = 14.040 kg/h
Answer:
Cout=0.0975g/m3,η=99.63C_out = 0.0975 g/m^{3}, \eta = 99.63%, emission = 14.04 kg/h

Why the other options are there

  • η = 173.5% (efficiencies added)
  • 3,744 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 8
Series particulate control: overall collection efficiency and emission rate — Baghouse (8)

A stack gas stream of 50 m³/s carries 15 g/m³ of particulate. It passes a cyclone at 85% efficiency followed by a fabric filter at 91.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=50m3/sQ = 50 m^{3}/s
  • Cin=15g/m3C_in = 15 g/m^{3}
  • η1=0.85\eta_{1} = 0.85
  • η2=0.910\eta_{2} = 0.910

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=15(1−0.85)=2.250g/m3C_{1} = 15(1 - 0.85) = 2.250 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=2.250(1−0.910)=0.2025g/m3C_{2} = 2.250(1 - 0.910) = 0.2025 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.150×0.0900=0.98650=98.650\eta = 1 - 0.150 \times 0.0900 = 0.98650 = 98.650%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.2025g/m3×50m3/s×3600s/h÷1000=36.450kg/h0.2025 g/m^{3} \times 50 m^{3}/s \times 3600 s/h \div 1000 = 36.450 kg/h
Answer:
Cout=0.2025g/m3,η=98.65C_out = 0.2025 g/m^{3}, \eta = 98.65%, emission = 36.45 kg/h

Why the other options are there

  • η = 176.0% (efficiencies added)
  • 2,700 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 9
Series particulate control: overall collection efficiency and emission rate — Baghouse (9)

A stack gas stream of 46 m³/s carries 30 g/m³ of particulate. It passes a cyclone at 86% efficiency followed by a fabric filter at 93.5% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=46m3/sQ = 46 m^{3}/s
  • Cin=30g/m3C_in = 30 g/m^{3}
  • η1=0.86\eta_{1} = 0.86
  • η2=0.935\eta_{2} = 0.935

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=30(1−0.86)=4.200g/m3C_{1} = 30(1 - 0.86) = 4.200 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=4.200(1−0.935)=0.2730g/m3C_{2} = 4.200(1 - 0.935) = 0.2730 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.140×0.0650=0.99090=99.090\eta = 1 - 0.140 \times 0.0650 = 0.99090 = 99.090%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.2730g/m3×46m3/s×3600s/h÷1000=45.209kg/h0.2730 g/m^{3} \times 46 m^{3}/s \times 3600 s/h \div 1000 = 45.209 kg/h
Answer:
Cout=0.2730g/m3,η=99.09C_out = 0.2730 g/m^{3}, \eta = 99.09%, emission = 45.21 kg/h

Why the other options are there

  • η = 179.5% (efficiencies added)
  • 4,968 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

Example 10
Series particulate control: overall collection efficiency and emission rate — Baghouse (10)

A stack gas stream of 49 m³/s carries 26 g/m³ of particulate. It passes a cyclone at 91% efficiency followed by a fabric filter at 90.0% efficiency. Compute the concentration after each device, the overall efficiency, and the emission rate in kg/h.

Given

  • Q=49m3/sQ = 49 m^{3}/s
  • Cin=26g/m3C_in = 26 g/m^{3}
  • η1=0.91\eta_{1} = 0.91
  • η2=0.900\eta_{2} = 0.900

Find

Intermediate and final concentrations, overall η and kg/h emitted

Start with the thinking

  • Efficiencies in series multiply as penetrations (1 − η), they never simply add.
  • The overall penetration is the product of the individual penetrations.

Step-by-step solution

  1. Formula

    C1=Cin(1−η1)C_{1} = C_in(1 - \eta_{1})
  2. Substituting

    C1=26(1−0.91)=2.340g/m3C_{1} = 26(1 - 0.91) = 2.340 g/m^{3}
  3. Formula

    C2=C1(1−η2)C_{2} = C_{1}(1 - \eta_{2})
  4. Substituting

    C2=2.340(1−0.900)=0.2340g/m3C_{2} = 2.340(1 - 0.900) = 0.2340 g/m^{3}
  5. Formula

    ηoverall=1−(1−η1)(1−η2)\eta_overall = 1 - (1 - \eta_{1})(1 - \eta_{2})
  6. Substituting

    η=1−0.090×0.1000=0.99100=99.100\eta = 1 - 0.090 \times 0.1000 = 0.99100 = 99.100%
  7. Formula

    emission=C2Qemission = C_{2} Q
  8. Substituting

    0.2340g/m3×49m3/s×3600s/h÷1000=41.278kg/h0.2340 g/m^{3} \times 49 m^{3}/s \times 3600 s/h \div 1000 = 41.278 kg/h
Answer:
Cout=0.2340g/m3,η=99.10C_out = 0.2340 g/m^{3}, \eta = 99.10%, emission = 41.28 kg/h

Why the other options are there

  • η = 181.0% (efficiencies added)
  • 4,586 kg/h (uncontrolled rate)

Reference: FE Reference Handbook — Environmental Engineering → Baghouse

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