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IS 8417 : 1990Criteria for design of activated sludge process (First Revision)

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Recommended Standards for Wastewater Facilities, 2021 Edition · DWA-A 131E · WEF MOP 8, 6th Edition
CurrentFrequently UsedCode of PracticeBIMEnvironmental · Environmental and Sanitation
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OverviewValues6InternationalTablesFAQ4Related

IS 8417:1990 is the Indian Standard (BIS) for criteria for design of activated sludge process (first revision). This standard provides criteria for the process design of activated sludge systems used for treating sewage and biodegradable industrial wastewater. It covers various modifications of the process, including conventional, extended aeration, and contact stabilization, detailing key design parameters like F/M ratio, sludge age, and oxygen requirements.

Specifies the criteria for the design of activated sludge process used in sewage and industrial wastewater treatment.

Overview

Status
Current
Usage level
Frequently Used
Domain
Environmental — Environmental and Sanitation
Type
Code of Practice
International equivalents
Recommended Standards for Wastewater Facilities, 2021 Edition · Great Lakes-Upper Mississippi River Board of State and Provincial Public Health and Environmental Managers (GLUMRB), USA & CanadaDWA-A 131E:2016-04 · DWA (German Association for Water, Wastewater and Waste), GermanyWEF MOP 8, 6th Edition · Water Environment Federation (WEF), USABS EN 12255-6:2002 · BSI (British Standards Institution) / CEN (European Committee for Standardization), UK/Europe
Typically used with
IS 2490IS 3306IS 2296
Also on InfraLens for IS 8417
6Key values3Tables4FAQs

BIM-relevant code. See the BIM Hub for ISO 19650, IFC, and LOD/LOIN frameworks used alongside it.

Practical Notes
! The design values provided are typical and must be adjusted based on treatability studies for specific wastewater characteristics.
! Proper design of the secondary clarifier is as crucial as the aeration tank design for achieving the desired effluent quality and ensuring good sludge settling.
! Pay close attention to sludge recirculation and wasting rates, as they directly control the sludge age (MCRT) and overall process stability.
Frequently referenced clauses
Cl. 4Design ParametersCl. 5Process DesignCl. 6Aeration SystemCl. 7Secondary Settling TankCl. 8Sludge Handling and Disposal
Pulled from IS 8417:1990. Browse the full clause & table index below in Tables & Referenced Sections.
wastewatersewageactivated sludgebiomass

International Equivalents

Similar International Standards
Recommended Standards for Wastewater Facilities, 2021 EditionGreat Lakes-Upper Mississippi River Board of State and Provincial Public Health and Environmental Managers (GLUMRB), USA & Canada
HighCurrent
Recommended Standards for Wastewater Facilities ('Ten States Standards')
Provides prescriptive design criteria for wastewater facilities, including activated sludge processes, for regulatory approval.
DWA-A 131E:2016-04DWA (German Association for Water, Wastewater and Waste), Germany
HighCurrent
Dimensioning of Single-Stage Activated Sludge Plants
Offers a detailed, calculation-based approach for sizing activated sludge systems, influential throughout Europe.
WEF MOP 8, 6th EditionWater Environment Federation (WEF), USA
HighCurrent
Design of Municipal Wastewater Treatment Plants
A comprehensive design manual of practice covering all aspects of activated sludge system design, engineering, and operation.
BS EN 12255-6:2002BSI (British Standards Institution) / CEN (European Committee for Standardization), UK/Europe
MediumCurrent
Wastewater treatment plants - Part 6: Activated sludge process
Specifies general principles and performance requirements for activated sludge processes within the EU framework.
Key Differences
≠IS 8417:1990 focuses primarily on BOD removal. Modern international standards like DWA-A 131E and WEF MOP 8 have extensive, integrated design procedures for biological nutrient removal (BNR), including nitrification, denitrification, and biological phosphorus removal, which are now standard practice globally.
≠The Indian standard heavily relies on the Food-to-Microorganism (F/M) ratio and volumetric organic loading as primary design parameters. In contrast, modern standards like DWA-A 131E and WEF MOP 8 use Sludge Retention Time (SRT) or Sludge Age as the fundamental design and control parameter, as it more directly governs effluent quality, sludge production, and the ability to achieve nitrification.
≠Secondary clarifier design in IS 8417 is based on simple surface overflow rates (SOR) and solids loading rates (SLR) from lookup tables. Modern practices, particularly in German standards, often incorporate more sophisticated models like flux theory or state-point analysis, which dynamically link clarifier performance to the settling characteristics of the sludge (e.g., Sludge Volume Index - SVI).
≠IS 8417:1990 provides only general guidelines for aeration, whereas current international standards specify detailed methods for calculating actual oxygen requirements (AOR), converting to standard oxygen requirements (SOR) using alpha, beta, and theta factors, and evaluating the Standard Oxygen Transfer Efficiency (SOTE) of aeration equipment.
Key Similarities
≈All standards are fundamentally based on the same core principles of the activated sludge process: the use of a suspended-growth microbiological culture in an aerated basin to metabolize organic pollutants, followed by solids-liquid separation.
≈Core design parameters such as BOD loading, Mixed Liquor Suspended Solids (MLSS), Hydraulic Retention Time (HRT), and secondary clarifier surface area are common to all standards, even if the target values and calculation methodologies have evolved.
≈The major process variations of activated sludge (e.g., Conventional Plug Flow, Complete Mix, Extended Aeration, Contact Stabilization) are recognized and described in both IS 8417 and its international counterparts.
≈All standards explicitly recognize the secondary clarifier as an indispensable component of the system, crucial for separating the treated wastewater from the biological mass and for thickening sludge for recirculation.
Parameter Comparison
ParameterIS ValueInternationalSource
F/M Ratio (Conventional Plant)0.2 - 0.4 kg BOD / kg MLSS.day0.2 - 0.4 lb BOD / lb MLVSS.day (functionally similar range)WEF MOP 8 / Ten States Standards
MLSS Concentration (Conventional Plant)2000 - 3500 mg/L1500 - 3000 mg/LWEF MOP 8
Secondary Clarifier SOR (Average Flow)24 - 32 m³/m².day (for plants > 4.5 MLD)≤ 32.6 m³/m².day (equivalent to 800 gpd/ft² for plants > 1 MGD)Ten States Standards
Sludge Age / SRT (Extended Aeration)20 - 30 days20 - 40 daysWEF MOP 8
Volumetric Organic Loading (Conventional Plant)0.3 - 0.6 kg BOD / m³.day0.3 - 0.7 kg BOD / m³.dayTypical US Design Practice (derived from MOP 8)
Hydraulic Retention Time (HRT) (Conventional Plant)6 - 8 hours4 - 8 hoursTen States Standards
⚠ Verify details from original standards before use

Key Values6

Quick Reference Values
F/M Ratio (Conventional Process)0.2 - 0.4 kg BOD/kg MLVSS/day
MLSS Concentration (Conventional Process)1500 - 3000 mg/l
Hydraulic Retention Time (HRT) (Conventional Process)4 - 8 hours
Sludge Age (Extended Aeration)20 - 30 days
Volumetric Loading (Extended Aeration)0.16 - 0.40 kg BOD/m³/day
Surface Overflow Rate (Secondary Clarifier)12 - 20 m³/m²/day
Key Formulas
F/M = (Q * So) / (V * X) — Food to Microorganism Ratio
θc = (V * X) / (Qw * Xr + Qe * Xe) — Sludge Age or Mean Cell Residence Time (MCRT)
Volumetric Loading = (Q * So) / V — Organic loading rate per unit volume of aeration tank

Tables & Referenced Sections

Key Tables
Table 1 - Typical Design Parameters for Activated Sludge Processes
Table 2 - Oxygen Requirements for Various Activated Sludge Treatment Processes
Table 3 - Typical Surface Overflow Rates for Secondary Settling Tanks
Key Clauses
Clause 4 - Design Parameters
Clause 5 - Process Design
Clause 6 - Aeration System
Clause 7 - Secondary Settling Tank
Clause 8 - Sludge Handling and Disposal

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Cross-Referenced Codes
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IS 3306:2018Pig Iron — Specification
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IS 2296:2001Temperature Measurement in Industry
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Frequently Asked Questions4

What is the typical F/M ratio for a conventional activated sludge plant?+
0.2 to 0.4 kg BOD per kg MLVSS per day (Table 1).
What is the recommended hydraulic retention time (HRT) for an extended aeration process?+
18 to 36 hours (Table 1).
What is a typical MLSS concentration for a conventional plant?+
1500 to 3000 mg/l (Table 1).
What is the surface overflow rate for a secondary settling tank?+
12 to 20 m³/m²/day for average flow (Table 3).

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