Sanitary and Waste Water Engineering MCQs 2026

69 questions with detailed answers · 34 from past papers · 7 quiz batches available

📚 Civil Engineering📄 34 Past-Paper Qs✓ Free · No Login Needed
🎯 Mock Test

Read each question, think about the answer, then click Show Answer to reveal the correct option and explanation. Load 10 at a time so it stays manageable — perfect for one-topic study sessions on the bus or during a break.

Page 1 of 1Questions 1–10 of 69
  1. Q1easy

    Separate sewer system has

    1. ASingle pipe for all flows always
    2. BDistinct sanitary and storm sewers
    3. CNo storm drainage
    4. DNo sanitary lines
    💡 Explanation:

    Separate systems reduce treatment plant overload during rains

  2. Q2Past Paper · PPSC/FPSC/NTSeasy

    Standard BOD test incubation period at 20°C is

    1. A3 days
    2. B5 days
    3. C7 days
    4. D10 days
    💡 Explanation:

    BOD5 is measured over 5 days at 20°C as per standard methods used in Pakistan water quality labs

  3. Q3Past Paper · PPSC/FPSC/NTSeasy

    Typical BOD/COD ratio for untreated domestic sewage is approximately

    1. A0.4 to 0.6
    2. B0.9 to 1.0
    3. C0.1 to 0.2
    4. D0.8 to 0.9
    💡 Explanation:

    Domestic sewage is biodegradable; BOD is usually 40-60% of COD before treatment

  4. Q4easy

    Activated sludge process relies primarily on

    1. AAnaerobic bacteria in septic tank
    2. BPhysical filtration only
    3. CChemical precipitation alone
    4. DAerobic microorganisms in mixed liquor
    💡 Explanation:

    Activated sludge uses aeration to grow aerobic biomass that oxidizes organic matter

  5. Q5medium

    Mean cell residence time in activated sludge is controlled by

    1. ASludge wasting rate
    2. BPrimary clarifier depth
    3. CGrit chamber velocity
    4. DTrickling filter media size
    💡 Explanation:

    Wasting controls SRT/MCRT which affects sludge age and effluent quality

  6. Q6Past Paper · PPSC/FPSC/NTSmedium

    F/M ratio in activated sludge stands for

    1. AFlow to Mass ratio
    2. BFilament to Mixed liquor ratio
    3. CFood to Microorganism ratio
    4. DFinal to Initial BOD ratio
    💡 Explanation:

    F/M relates organic loading to biomass concentration in aeration tank

  7. Q7Past Paper · PPSC/FPSC/NTSeasy

    Typical MLSS concentration in conventional activated sludge is

    1. A50 to 100 mg/L
    2. B2000 to 4000 mg/L
    3. C10000 to 15000 mg/L
    4. D100 to 200 mg/L
    💡 Explanation:

    Mixed liquor suspended solids in conventional plants range 2000-4000 mg/L

  8. Q8Past Paper · PPSC/FPSC/NTSeasy

    Drying beds for sludge dewatering depend on

    1. AEvaporation and drainage
    2. BReverse osmosis
    3. CCentrifugal pumps only
    4. DActivated carbon adsorption
    💡 Explanation:

    Sludge is spread on sand beds for dewatering by sun and gravity

  9. Q9medium

    Belt filter press is used for

    1. AAeration of mixed liquor
    2. BMechanical sludge dewatering
    3. CGrit washing
    4. DInfluent screening
    💡 Explanation:

    Belt presses squeeze water from conditioned sludge

  10. Q10medium

    Centrifuge dewatering uses

    1. ABiological nitrification
    2. BTrickling filter recirculation
    3. CSedimentation in oxidation pond only
    4. DHigh rotational speed to separate solids
    💡 Explanation:

    Centrifugal force drives liquid-solid separation

  11. Q11medium

    Composting of sludge requires

    1. AAdequate carbon-nitrogen balance and aeration
    2. BComplete anaerobic sealed conditions always
    3. CZero moisture
    4. DSub-zero temperature
    💡 Explanation:

    Composting stabilizes biosolids for agricultural use where permitted

  12. Q12Past Paper · PPSC/FPSC/NTSmedium

    Industrial wastewater with heavy metals needs

    1. ADirect discharge to oxidation pond only
    2. BNo treatment in Pakistan
    3. CPretreatment before biological treatment
    4. DOnly dilution with storm water
    💡 Explanation:

    Toxic metals inhibit biological processes and need source control

  13. Q13easy

    Equalization tank purpose is

    1. ARemove all BOD
    2. BDampen flow and load variations
    3. CProvide final disinfection
    4. DReplace secondary clarifier
    💡 Explanation:

    Equalization balances diurnal industrial discharge peaks

  14. Q14Past Paper · PPSC/FPSC/NTSeasy

    Grease trap is installed to

    1. AIncrease BOD loading
    2. BProvide nitrification
    3. CMeasure COD
    4. DRemove fats oils and grease from kitchen waste
    💡 Explanation:

    FOG causes sewer blockages and interferes with treatment

  15. Q15Past Paper · PPSC/FPSC/NTSeasy

    Grit chamber removes

    1. ADissolved ammonia
    2. BAll organic matter
    3. CInorganic settleable particles like sand
    4. DBiogas methane
    💡 Explanation:

    Grit protects pumps and prevents abrasion in treatment units

  16. Q16Past Paper · PPSC/FPSC/NTSmedium

    Horizontal flow grit chamber design uses

    1. AControlled velocity near 0.3 m/s
    2. BVelocity 5 m/s
    3. CZero velocity always
    4. DVelocity 10 m/s
    💡 Explanation:

    At about 0.3 m/s organic matter stays suspended while grit settles

  17. Q17medium

    Aerated grit chamber uses

    1. AChlorine gas
    2. BDiffused air to separate organic matter from grit
    3. CMembrane filtration
    4. DTrickling filter media
    💡 Explanation:

    Air roll keeps organics suspended while grit settles

  18. Q18Past Paper · PPSC/FPSC/NTSeasy

    Bar screen with 25 mm spacing is classified as

    1. AFine screen
    2. BMicro screen
    3. CCoarse screen
    4. DMembrane screen
    💡 Explanation:

    Coarse screens remove large debris before pumps

  19. Q19easy

    Comminutors are used to

    1. ADigest sludge anaerobically
    2. BShred coarse solids in sewage
    3. CMeasure BOD
    4. DRemove nitrogen
    💡 Explanation:

    Comminutors reduce size of rags and debris

  20. Q20Past Paper · PPSC/FPSC/NTSmedium

    Infiltration in sewer systems refers to

    1. ASewage leaking to groundwater as standard term
    2. BRain falling on manholes only
    3. CIndustrial discharge
    4. DGroundwater entering sewer pipes
    💡 Explanation:

    Infiltration increases flow during wet weather stressing treatment plants

  21. Q21Past Paper · PPSC/FPSC/NTSmedium

    Exfiltration from sewers causes

    1. AGroundwater and soil contamination
    2. BReduced treatment cost
    3. CImproved pipe strength
    4. DHigher BOD removal in plant
    💡 Explanation:

    Leaking sewage contaminates surrounding soil and groundwater

  22. Q22Past Paper · PPSC/FPSC/NTSeasy

    I/I stands for in sewerage engineering

    1. AInfluent and Inhibition
    2. BInternal and Intermittent
    3. CInorganic and Industrial
    4. DInfiltration and Inflow
    💡 Explanation:

    I/I adds extraneous water to sanitary sewers

  23. Q23Past Paper · PPSC/FPSC/NTSmedium

    Self cleansing velocity in sewers prevents

    1. APipe corrosion only
    2. BSediment deposition in pipes
    3. CBiological treatment failure
    4. DGrit chamber overflow
    💡 Explanation:

    Minimum velocity keeps solids in suspension per sewer design codes

  24. Q24easy

    Manning formula is used in sewer design to relate

    1. ABOD and COD
    2. BSludge age and F/M
    3. CFlow velocity and pipe slope
    4. DNitrification rate
    💡 Explanation:

    Manning equation calculates flow in open channels and partially full pipes

  25. Q25medium

    Peak factor in sewage flow accounts for

    1. ADiurnal and seasonal variation
    2. BOnly pipe material
    3. COnly manhole spacing
    4. DOnly sludge density
    💡 Explanation:

    Peak flow design ensures conveyance at maximum expected flow

  26. Q26medium

    Hazen-Williams formula is also used for

    1. AWater and sewage pressure pipe flow
    2. BSludge digestion rate
    3. CBOD kinetics only
    4. DWind rose analysis
    💡 Explanation:

    HW equation estimates head loss in pressurized sewer force mains

  27. Q27Past Paper · PPSC/FPSC/NTSeasy

    Force main is required when

    1. ASewer is always gravity
    2. BNo pumping ever needed
    3. CGravity flow is not feasible
    4. DTreatment plant is uphill without lift
    💡 Explanation:

    Pumping lifts sewage where topography prevents gravity conveyance

  28. Q28easy

    Wet well in pumping station collects

    1. ATreated effluent only
    2. BSewage before pumps activate
    3. CDrinking water
    4. DSludge cake
    💡 Explanation:

    Wet wells store influent for submersible or dry well pumps

  29. Q29Past Paper · PPSC/FPSC/NTSeasy

    Chlorination of treated effluent purpose is

    1. APathogen disinfection
    2. BIncrease BOD
    3. CPromote nitrification
    4. DRemove grit
    💡 Explanation:

    Chlorine kills bacteria before discharge or reuse

  30. Q30medium

    Dechlorination may be needed to

    1. AIncrease COD
    2. BPromote algae in aeration tank
    3. CRemove grit
    4. DReduce chlorine toxicity to aquatic life
    💡 Explanation:

    Sulfur dioxide or bisulfite neutralizes residual chlorine in effluent

  31. Q31medium

    Sewer pipe minimum slope is governed by

    1. AOnly pavement CBR
    2. BOnly wind speed
    3. COnly earthquake zone
    4. DDiameter and self cleansing velocity
    💡 Explanation:

    Smaller pipes need steeper slopes to maintain self cleansing

  32. Q32easy

    Sludge digestion reduces

    1. AConcrete strength
    2. BPipe diameter
    3. CVolatile solids and pathogens
    4. DManning n value
    💡 Explanation:

    Digestion stabilizes sludge reducing odor and mass

  33. Q33easy

    Oxidation pond treatment depends on

    1. AHigh pressure pumps only
    2. BAnaerobic methanogenesis only
    3. CAlgae-bacteria symbiosis and sunlight
    4. DMembrane filtration
    💡 Explanation:

    Facultative ponds use natural oxygen from algae for aerobic bacteria

  34. Q34medium

    Detention time in facultative oxidation pond is typically

    1. A30 minutes
    2. B5 to 10 days
    3. C2 hours
    4. D1 hour
    💡 Explanation:

    Long HRT compensates for low biomass density in ponds

  35. Q35Past Paper · PPSC/FPSC/NTSeasy

    Primary treatment removes mainly

    1. ASettleable and floatable solids
    2. BDissolved nutrients completely
    3. CAll pathogens
    4. DHeavy metals completely
    💡 Explanation:

    Primary clarifiers remove suspended solids by gravity settling

  36. Q36easy

    Secondary treatment target is mainly

    1. AOnly grit and oil
    2. BTotal dissolved solids only
    3. CRadioactive isotopes
    4. DBiodegradable organic matter and BOD
    💡 Explanation:

    Biological secondary treatment reduces BOD and suspended organics

  37. Q37Past Paper · PPSC/FPSC/NTSeasy

    Tertiary treatment may include

    1. AOnly bar screens
    2. BNutrient removal and filtration
    3. CGrit channels only
    4. DRaw sewage pumping
    💡 Explanation:

    Advanced treatment adds nutrient removal, filtration, or disinfection

  38. Q38Past Paper · PPSC/FPSC/NTSmedium

    Nitrification converts

    1. ANitrate to nitrogen gas
    2. BBOD to methane
    3. CPhosphate to sludge only
    4. DAmmonia to nitrate
    💡 Explanation:

    Autotrophic nitrifiers oxidize NH3 to NO2 and NO3 aerobically

  39. Q39Past Paper · PPSC/FPSC/NTSmedium

    Denitrification requires

    1. AAnoxic conditions and organic carbon
    2. BHigh dissolved oxygen
    3. CChlorine dosing
    4. DUltraviolet light only
    💡 Explanation:

    Denitrifiers reduce nitrate to N2 under anoxic conditions

  40. Q40hard

    Biological phosphorus removal uses

    1. AOnly primary clarifiers
    2. BOnly chlorination
    3. CAlternating anaerobic-aerobic zones
    4. DOnly grit removal
    💡 Explanation:

    PAOs release P anaerobically and uptake P aerobically

  41. Q41medium

    Membrane bioreactor combines

    1. AActivated sludge with membrane filtration
    2. BTrickling filter with chlorination
    3. CSeptic tank with RO only
    4. DGrit chamber with UV
    💡 Explanation:

    MBR replaces secondary clarifier with micro/ultrafiltration membranes

  42. Q42medium

    Typical pore size classification for MBR is

    1. AGravel filtration
    2. BRapid sand 1 mm only
    3. CMicrofiltration or ultrafiltration
    4. DNo filtration
    💡 Explanation:

    MBR membranes retain biomass producing high quality effluent

  43. Q43medium

    UV disinfection mechanism is

    1. ASedimentation of viruses
    2. BDNA damage to microorganisms
    3. CChemical oxidation with chlorine
    4. DFiltration through sand
    💡 Explanation:

    UV light inactivates pathogens without chemical residual

  44. Q44Past Paper · PPSC/FPSC/NTSmedium

    Landfill disposal of dewatered sludge requires

    1. ANo regulation
    2. BDirect dumping in rivers
    3. CEnvironmental compliance and leachate control
    4. DOpen burning only
    💡 Explanation:

    Pakistan EPA guidelines restrict sludge disposal to protect environment

  45. Q45medium

    Phosphorus removal chemically uses commonly

    1. AOnly aeration
    2. BOnly grit removal
    3. COnly UV without coagulants
    4. DLime or alum coagulation
    💡 Explanation:

    Chemical precipitation with metal salts removes phosphate

  46. Q46medium

    Reclaimed wastewater for irrigation requires

    1. ANo treatment ever
    2. BAdequate treatment and pathogen control
    3. COnly grit removal
    4. DRaw sewage application
    💡 Explanation:

    Reuse standards protect public health in water-scarce Pakistan

  47. Q47Past Paper · PPSC/FPSC/NTSmedium

    Effluent discharge standards in Pakistan are set by

    1. ANEQS National Environmental Quality Standards
    2. BOnly local mason
    3. COnly WHO exclusively without local law
    4. DNo standards exist
    💡 Explanation:

    NEQS regulate pollutants in industrial and municipal effluents

  48. Q48Past Paper · PPSC/FPSC/NTSeasy

    Lagoons in Pakistan rural areas are often

    1. AMBR plants
    2. BLow cost facultative ponds
    3. CNuclear cooled basins
    4. DOnly packaged RO units
    💡 Explanation:

    Facultative lagoons suit warm climate and low maintenance needs

  49. Q49Past Paper · PPSC/FPSC/NTSmedium

    Rotating biological contactor RBC uses

    1. AStatic sand filter only
    2. BOnly chemical coagulation
    3. COnly grit channel
    4. DRotating media discs in wastewater
    💡 Explanation:

    Biofilm on rotating discs alternately contacts wastewater and air

  50. Q50medium

    Sequencing Batch Reactor SBR operates in

    1. AFill react settle decant cycle
    2. BContinuous flow only always
    3. CNo aeration ever
    4. DOnly primary treatment
    💡 Explanation:

    SBR performs all steps in single tank sequentially

  51. Q51hard

    Contact stabilization process uses

    1. AOnly oxidation pond
    2. BOnly septic tank
    3. CSmall contact tank and larger stabilization tank
    4. DOnly UASB
    💡 Explanation:

    Adsorption in contact tank and regeneration in stabilization tank

  52. Q52Past Paper · PPSC/FPSC/NTSmedium

    SRT in activated sludge is

    1. ASewer Rise Time
    2. BSludge Return Temperature
    3. CSettlement Rate Test
    4. DSolids Retention Time
    💡 Explanation:

    SRT is average time biomass remains in system affecting performance

  53. Q53hard

    ThOD theoretically represents

    1. AOxygen required for complete oxidation
    2. BOnly chlorine demand
    3. COnly nitrogen gas volume
    4. DOnly sludge volume
    💡 Explanation:

    Theoretical oxygen demand if all organics fully oxidized

  54. Q54Past Paper · PPSC/FPSC/NTSeasy

    COD measures

    1. AOnly biodegradable fraction
    2. BOnly nitrogen
    3. CTotal organic matter oxidizable chemically
    4. DOnly suspended grit
    💡 Explanation:

    COD uses strong oxidant capturing non-biodegradable organics too

  55. Q55Past Paper · PPSC/FPSC/NTSmedium

    Sludge volume index SVI indicates

    1. ABOD of influent
    2. BCOD of effluent
    3. CChlorine residual
    4. DSettleability of activated sludge
    💡 Explanation:

    High SVI suggests bulking sludge with poor settling

  56. Q56Past Paper · PPSC/FPSC/NTShard

    Sludge bulking is often caused by

    1. AExcessive grit removal
    2. BFilamentous bacteria overgrowth
    3. CToo much chlorine in influent
    4. DZero organic loading
    💡 Explanation:

    Filamentous organisms cause light fluffy sludge with high SVI

  57. Q57easy

    Primary sludge from municipal WWTP is typically

    1. ASterile and inert
    2. BLiquid with zero solids
    3. CAlready stabilized completely
    4. DHigh solids content and putrescible
    💡 Explanation:

    Primary sludge is concentrated settleable solids needing further treatment

  58. Q58easy

    Return activated sludge is recycled to

    1. AFinal effluent outlet
    2. BSludge drying beds only
    3. CPrimary clarifier underflow exclusively
    4. DAeration tank inlet
    💡 Explanation:

    RAS maintains biomass inventory in aeration tank

  59. Q59medium

    Extended aeration activated sludge typically operates at

    1. AHigh F/M and short SRT
    2. BLow F/M and long SRT
    3. CZero dissolved oxygen
    4. DNo sludge return
    💡 Explanation:

    Extended aeration has low loading and long sludge age for stable operation

  60. Q60Past Paper · PPSC/FPSC/NTSeasy

    Trickling filter media commonly used in Pakistan is

    1. ASand only
    2. BSteel plates
    3. CRock or plastic media
    4. DConcrete blocks without voids
    💡 Explanation:

    High surface area media supports biofilm growth in trickling filters

  61. Q61medium

    Hydraulic loading on trickling filter is expressed as

    1. Am³/m²/day
    2. Bkg BOD/ha/day
    3. Cm/s Manning velocity
    4. DkN/m² contact pressure
    💡 Explanation:

    Hydraulic loading rate is flow per unit plan area of filter

  62. Q62Past Paper · PPSC/FPSC/NTSmedium

    Organic loading on trickling filter is expressed as

    1. Am³/m²/day
    2. Bmg/L MLSS
    3. CkPa head loss
    4. Dkg BOD/m³/day
    💡 Explanation:

    Organic loading relates BOD applied per unit media volume

  63. Q63Past Paper · PPSC/FPSC/NTSeasy

    Anaerobic digestion produces biogas rich in

    1. AOxygen
    2. BChlorine
    3. CMethane
    4. DNitrogen gas only
    💡 Explanation:

    Methanogenic bacteria convert organics to CH4 and CO2 in anaerobic digesters

  64. Q64medium

    Optimum temperature range for mesophilic anaerobic digestion is

    1. A30 to 38°C
    2. B5 to 10°C
    3. C55 to 65°C
    4. D80 to 90°C
    💡 Explanation:

    Mesophilic digesters operate around 35°C commonly in Pakistan WWTPs

  65. Q65hard

    Two-stage anaerobic digestion separates

    1. APrimary and secondary settling
    2. BAcid formation and methane formation
    3. CNitrification and denitrification
    4. DScreening and grit removal
    💡 Explanation:

    Acidogens and methanogens have different optimal conditions

  66. Q66Past Paper · PPSC/FPSC/NTSmedium

    UASB reactor is primarily used for

    1. ADisinfection with chlorine
    2. BGrit removal
    3. CAnaerobic treatment of high-strength wastewater
    4. DStorm water detention
    💡 Explanation:

    Upflow Anaerobic Sludge Blanket treats industrial and high-strength organic waste

  67. Q67Past Paper · PPSC/FPSC/NTSeasy

    Septic tank provides

    1. APrimary sedimentation and anaerobic digestion
    2. BComplete nitrification
    3. CReverse osmosis
    4. DActivated sludge aeration
    💡 Explanation:

    Septic tanks settle solids and partial anaerobic decomposition in rural Pakistan

  68. Q68easy

    Typical detention time in septic tank is

    1. A5 minutes
    2. B7 days minimum
    3. C30 days
    4. D24 to 48 hours
    💡 Explanation:

    HRT allows settling and partial digestion of domestic waste

  69. Q69Past Paper · PPSC/FPSC/NTSmedium

    Imhoff tank combines

    1. AAeration and chlorination
    2. BSedimentation and sludge digestion
    3. CFiltration and UV
    4. DFlocculation and adsorption
    💡 Explanation:

    Imhoff cone separates digestion from supernatant in single unit