STP Load Calculator – Residential High-Rise | Step-by-Step + PDF Export

STP Load Calculator

Residential High-Rise Building • Step-by-Step Calculations • Export to PDF

Based on CPHEEO Manual, NBC 2016, CPCB/SPCB & IS 18997:2024

1. Project Inputs

STP Load Calculation Report

Residential High-Rise Building • Generated by STP Load Calculator

2. Project Summary

ParameterValue

3. Step-by-Step Calculations

4. Pollution Load

Parameter Concentration Load Calculation Load (kg/day)

5. Flow Summary

Description KLD m³/hr Remarks

6. Key Design Notes

  • Average Daily Flow (ADF) is used for biological process design and overall STP capacity.
  • Peak Flow is used only for hydraulic design of inlet works, screens, channels, pumps and pipelines.
  • Always provide 10–20% safety margin but avoid excessive over-sizing.
  • Final design must be verified by a qualified STP technology provider as per site conditions and local SPCB norms.

References: CPHEEO Manual on Sewerage & Sewage Treatment (2013) • NBC 2016 Part 9 • CPCB/SPCB Guidelines • IS 18997:2024

This is a preliminary estimation tool. Actual design shall be carried out by a competent professional.

STP Load Calculator • For educational & preliminary planning purposes only
STP Load Calculation for Residential High-Rise Building – Detailed Guide with Solved Example

STP Load Calculation for Residential High-Rise Building

Solved Example with Formulas, Design Basis & Practical Guidance

Based on CPHEEO Manual, NBC 2016, CPCB/SPCB Norms & IS 18997:2024

1. Introduction

A Sewage Treatment Plant (STP) is essential for any residential high-rise building to treat wastewater generated from toilets, kitchens, bathrooms and utility areas before reuse or safe disposal. Proper load calculation ensures the plant is neither under-designed (leading to poor performance) nor over-sized (wasting capital and operating cost).

This article presents a complete, step-by-step worked example for a typical 500-flat residential high-rise project, covering hydraulic design, pollution load, capacity selection, unit sizing and treated water reuse.

Golden Rule of STP Design:
• Average Daily Flow (ADF) is used for biological process design and overall capacity selection.
• Peak Flow is used only for hydraulic components (inlet works, screens, channels, pumps, pipes).

2. Project Details (Assumed)

ParameterValue
Type of BuildingResidential High-Rise
Number of Flats500 Nos.
Average Occupancy4 Persons / Flat
Total Population500 × 4 = 2,000 Persons
Water Supply Basis135 LPCD (Litres Per Capita per Day) – Residential
Sewage Generation80% of Water Supply (as per CPHEEO)
Design StandardsCPHEEO Manual on Sewerage & Sewage Treatment (2013), NBC 2016 Part 9, CPCB/SPCB Norms, IS 18997:2024

3. Water Demand Calculation

1 Daily Water Demand
Daily Water Demand = Population × LPCD
= 2,000 × 135
= 270,000 L/day = 270 KLD

LPCD = Litres Per Capita per Day

4. Sewage Generation (Domestic)

2 Average Sewage Flow (ADF)
Sewage Generation = 80% of Water Supply
= 270 KLD × 0.80
= 216 KLD
Average Daily Flow (ADF) = 216 KLD

This is the most important number used for process design of the biological reactor, secondary clarifier and overall plant capacity.

Reference: As per CPHEEO Manual, domestic sewage is typically taken as 80% of water supply. IS 18997:2024 also recommends 108 LPCD wastewater generation for residential buildings (which is 80% of 135 LPCD).

5. Average Sewage Flow – Hourly Conversion

3
Average Hourly Flow = 216,000 L/day ÷ 24
= 9,000 L/hour = 9.0 m³/hr

6. Peak Sewage Flow (Hydraulic Design)

Peak Factor depends on contributing population as per CPHEEO Manual:

Population (Contributing)Peak Factor (PF)
Up to 20,0003.0
20,001 – 50,0002.5
50,001 – 5,00,0002.0
Above 5,00,0001.5
4 Calculation for our project (Population = 2,000)
Peak Factor (PF) = 3.0

Peak Sewage Flow = ADF × Peak Factor
= 216 KLD × 3.0
= 648 KLD
Peak Flow = 648 KLD = 27 m³/hr = 7.5 L/sec
Important Note:
• Peak Flow (648 KLD) is used only for hydraulic design of inlet works, bar screens, grit chambers, channels, pumps and pipelines.
• STP biological process capacity is always designed on Average Daily Flow (216 KLD).

7. STP Capacity Selection

While the average sewage generation is 216 KLD, practical capacity selection considers:

  • Future load (staff, visitors, club house, commercial areas)
  • Safety margin (10–20%)
  • Possible increase in occupancy or water use
Proposed STP Capacity = 250 KLD (Preliminary Selection)

This provides approximately 15–16% extra margin over the calculated ADF of 216 KLD.

8. Pollution Load Calculation

Assumed characteristics for domestic sewage (typical values):

Parameter Unit Typical Value Load Calculation (216 KLD) Load (kg/day)
BOD mg/L 250 216,000 L/day × 250 / 1000 54.0
COD mg/L 500 216,000 × 500 / 1000 108.0
TSS mg/L 200 216,000 × 200 / 1000 43.2
Oil & Grease mg/L 20 216,000 × 20 / 1000 4.32
General Formula:
Load (kg/day) = Flow (L/day) × Concentration (mg/L) / 1000

Design of the biological reactor is primarily based on BOD Load = 54.0 kg/day.

9. Flow Summary

Description Qty (KLD) In m³/hr Remarks
Average Daily Flow (ADF) 216 9.0 For Process Design
Peak Hydraulic Flow (PF = 3.0) 648 27.0 For Inlet works, Pumps, Channels
Peak Discharge — 7.5 L/sec For Hydraulic Components
Proposed STP Capacity 250 10.4 Preliminary Selection

10. Factors to Consider Before Final STP Capacity

  • Actual water consumption pattern (metered data preferred)
  • Flat occupancy variation (weekdays vs weekends)
  • Common area usage (landscaping, clubhouse, swimming pool backwash)
  • Staff / Kitchen / Restaurant / Commercial areas (if any)
  • Future expansion (10% to 20% additional capacity)
  • Reuse requirement of treated water
  • Local SPCB norms and discharge standards
  • Quality of influent water (low / high strength sewage)
  • Availability of space and power
  • O&M strategy and skilled manpower availability
Always select STP capacity based on engineering judgement with adequate safety margin, but avoid over-sizing.

11. Design Basis Summary

ItemBasisValue / Assumption
PopulationFlats × Occupancy500 × 4 = 2,000 Persons
Water SupplyAs per Project135 LPCD (Residential)
Sewage GenerationAs per CPHEEO80% of Water Supply
Average Sewage FlowCalculation216 KLD (9.0 m³/hr)
Peak FactorCPHEEO Manual3.0 (for Pop. up to 20,000)
Peak Sewage FlowADF × PF648 KLD (27 m³/hr)
Peak DischargeConversion7.5 L/sec
Proposed STP CapacitySelection250 KLD

12. Typical STP Process Flow Diagram

A modern residential high-rise STP typically follows this treatment train:

  1. Bar Screen (Channel) – Removes large solids (rags, plastics, sticks)
  2. Grit Chamber – Removes grit, sand and small stones
  3. Equalization Tank – Balances flow & load; homogenizes sewage
  4. Biological Treatment (SBR / MBBR / MBR) – Microorganisms break down organic matter (BOD, COD, TSS reduction)
  5. Secondary Clarifier – Settles biomass (sludge); clarified water overflows
  6. Tertiary Treatment (Filter) – Removes fine suspended solids and residual organics
  7. Disinfection (UV / Chlorine) – Kills pathogenic microorganisms
  8. Treated Water Tank – Stores treated water for reuse or final disposal

Sludge Line: Secondary Clarifier → Sludge Holding Tank → (Optional Thickener) → Sludge Dewatering (Belt Filter Press) → Dry Cake / Biosolids Disposal

Typical Removal Efficiency

Parameter% Removal (Typical)
BOD90 – 95 %
COD85 – 95 %
TSS90 – 95 %
Oil & Grease80 – 90 %
Pathogens> 99 %

13. Indicative Unit Sizing (for 250 KLD STP)

Unit Design Criteria Qty / Size (Approx.) Remarks
Bar Screen Clear bar opening 20–40 mm Manual / Mech. Channel width \~450 mm
Grit Chamber Detention Time 30–45 sec Size: 1.0 m (L) × 1.0 m (W) × 2.0 m (SWD) —
Equalization Tank Detention Time 6–8 hr Volume ≈ 250 × 8/24 ≈ 83 m³ (Say 85 m³) With submersible mixers
Biological Reactor SBR: 4–6 cycles/day
MBBR: 30–40% Media
Volume: 250–300 m³ Based on technology provider
Secondary Clarifier
(if MBBR system)
Surface Loading 20–25 m³/m²/day Dia.: 8.0 m
SWD: 3.0 m
Central Drive / Rake
Tertiary Filter Filtration Rate 8–10 m³/m²/hr Dual Media Filter Sand + Gravel Filter
Disinfection Chlorine Contact Time 20–30 min Contact Tank Volume ≈ 250 × 30/(24×60) ≈ 5.2 m³ Provide baffle arrangement
Sludge Drying Bed
(if used)
Loading 30–50 kg/m² Area: 15–20 m² As per sludge quantity
Note: Actual sizing shall be as per detailed design and technology provider data.

14. Treated Water Reuse Calculation

Treated Water Available ≈ 216 KLD (Average)

Assumed Reuse Requirement:

  • Gardening / Landscaping → 120 KLD
  • Flushing (Common area) → 40 KLD
  • DG Set / Utility / Others → 20 KLD
Total Reuse = 180 KLD
Balance 36 KLD can be kept as buffer / surplus for future demand or discharge (as per norms).

15. Discharge Norms (Typical – As per CPCB / SPCB)

ParameterUnitPermissible Limit*
BODmg/L≤ 10
CODmg/L≤ 50
TSSmg/L≤ 20
Oil & Greasemg/L≤ 10
pH—6.5 – 9.0
Total ColiformMPN/100 mL< 230

* As per CPCB / SPCB norms for inland surface water discharge (may vary as per local authority).

16. Pumps & Blowers (Indicative for 250 KLD)

A) Sewage Pump (Peak Flow 27 m³/hr)

  • Duty: 27 m³/hr at 12 m head
  • Quantity: 2 Working + 1 Standby
  • Type: Submersible / Dry well pump

B) Treated Water Pump

  • Duty: 12 m³/hr at 20 m head
  • Quantity: 2 Working + 1 Standby

C) Blowers (For Aeration in SBR / MBBR)

  • Air Demand: 0.4 – 0.6 m³/min per 100 KLD
    For 250 KLD → 1.0 – 1.5 m³/min
  • Quantity: 2 Working + 1 Standby
  • Type: Roots Blower
Selection shall be as per process requirements, head losses and technology provider data.

17. O&M Considerations

  • Ensure regular cleaning of screens and grit chamber
  • Monitor DO, MLSS (if applicable), pH and sludge volume
  • Check chemical dosing system and chlorine residual regularly
  • Ensure blower, pump and mixer preventive maintenance
  • Maintain log book for operating parameters and maintenance
  • Provide skilled operator and proper training

18. Key Points to Remember

  • Average Sewage Flow (ADF) is used for STP process design.
  • Peak Flow is used for hydraulic design of inlet works, screens, channels and pumps.
  • Proper screening, equalization and aeration are essential for efficient STP performance.
  • Always provide 10–20% safety margin but avoid excessive over-sizing.
  • Final design must comply with NBC, CPHEEO, SPCB/CPCB norms and technology provider recommendations.

19. References

  • CPHEEO Manual on Sewerage and Sewage Treatment Systems (2013)
  • National Building Code (NBC) 2016 – Part 9, Section 2 – Sanitation, Drainage & STP
  • CPCB / SPCB Guidelines for STP and Treated Water Reuse
  • IS 18997:2024 – Sewage Treatment Systems – Code of Practice
Disclaimer: This calculation is for preliminary estimation and planning purposes only. Final design shall be carried out by a qualified STP technology provider / consultant considering actual site conditions, local regulations and selected treatment technology.

Prepared for educational & reference purposes based on standard Indian design practices

Yogendra Gopal Borse

Yogendra Gopal Borse

Civil Engineer | Assistant Engineer Grade-I, Maharashtra PWD

B.Tech (Civil) from VJTI Mumbai. Experienced in bridge design, road works, estimation, project monitoring and digital engineering tools. Creator of YogiPWD – practical technical resources for civil engineers.

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