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IS 8413 (Part 2) : 2000Requirements for biological treatment end equipment, Part 2: Activated sludge process and its modifications

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DWA-A 281E · WEF MOP No. 8 / ASCE/WEF 52 · BS EN 12255-1
CurrentFrequently UsedSpecificationBIMEnvironmental · Public Health Engineering
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OverviewValues7InternationalTablesFAQ5Related

IS 8413:2000 (Part 2) is the Indian Standard (BIS) for requirements for biological treatment end equipment, part 2: activated sludge process and its modifications. This standard specifies the requirements for equipment used in biological wastewater treatment based on the activated sludge process (ASP) and its various modifications. It provides crucial design parameters like F/M ratio, sludge age, and loading rates for aeration tanks and secondary clarifiers, which are fundamental for designing effective sewage and industrial effluent treatment plants.

Requirements for biological treatment end equipment, Part 2: Activated sludge process and its modifications

Overview

Status
Current
Usage level
Frequently Used
Domain
Environmental — Public Health Engineering
Type
Specification
International equivalents
DWA-A 281E:2014 · DWA (German Association for Water, Wastewater and Waste), GermanyWEF MOP No. 8 / ASCE/WEF 52 · WEF (Water Environment Federation) / ASCE (American Society of Civil Engineers), USABS EN 12255-1:2002 · BSI (British Standards Institution) / CEN (European Committee for Standardization), UK/Europe
Typically used with
IS 3370IS 456IS 1172
Also on InfraLens for IS 8413
7Key values2Tables5FAQs

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

Practical Notes
! The design parameters in Table 1 are typical ranges and should be used with engineering judgment; pilot studies are recommended for large or unconventional wastewater streams.
! The performance of the entire ASP system heavily relies on the proper design and operation of the secondary clarifier, not just the aeration tank. Pay close attention to SOR and SLR values from Table 2.
! Selection of the ASP modification (e.g., conventional, extended aeration, SBR) depends on factors like influent BOD, land availability, power costs, and required effluent quality.
Frequently referenced clauses
Cl. 4Process Design ConsiderationsCl. 5.2Aeration TankCl. 5.3Secondary Clarifier (Settling Tank)Cl. 5.4Sludge Return SystemCl. 6Aeration Systems
Pulled from IS 8413:2000. Browse the full clause & table index below in Tables & Referenced Sections.
concretesteelwastewatersludge

International Equivalents

Similar International Standards
DWA-A 281E:2014DWA (German Association for Water, Wastewater and Waste), Germany
HighCurrent
Dimensioning of Trickling Filters and Rotating Biological Contactors
Directly addresses the design, dimensioning, and performance calculation of trickling filters.
WEF MOP No. 8 / ASCE/WEF 52WEF (Water Environment Federation) / ASCE (American Society of Civil Engineers), USA
HighCurrent
Design of Municipal Wastewater Treatment Plants, 5th Edition
A comprehensive manual of practice providing detailed design guidance for trickling filters within the overall context of a treatment plant.
BS EN 12255-1:2002BSI (British Standards Institution) / CEN (European Committee for Standardization), UK/Europe
LowCurrent
Wastewater treatment plants - Part 1: General construction principles
Provides general principles for all wastewater treatment plants, including trickling filters, but lacks specific design details for the equipment itself.
Key Differences
≠IS 8413 primarily provides empirical design guidelines and loading rate tables, whereas standards like DWA-A 281E and WEF MOP 8 emphasize the use of more complex, temperature-dependent kinetic models (e.g., Schulze, Eckenfelder, Velz equations) for performance prediction and sizing.
≠The Indian Standard gives very specific test requirements for conventional stone media (e.g., Los Angeles Abrasion Test, Sodium Sulphate Soundness Test). Modern international standards place less emphasis on prescriptive tests for stone and more on performance-based characteristics of synthetic media, such as specific surface area and void ratio.
≠IS 8413 provides simple recommendations for ventilation port areas (e.g., 1 m² per 25 m² of filter area). International guidance, particularly in German standards, offers more detailed analysis of ventilation, including calculations for natural draft based on air-water temperature differentials and criteria for when forced ventilation is required.
≠Recirculation in IS 8413 is determined using straightforward ratios or empirical formulae. US and German practices integrate recirculation as a key variable within their process models to more precisely control biofilm thickness, wetting rates, and overall process efficiency.
Key Similarities
≈All standards are based on the same fundamental attached-growth biological process where a microbial biofilm on a fixed medium removes organic pollutants from wastewater.
≈The core design parameters are universally recognized across all standards: organic loading (BOD/COD), hydraulic loading, media type and specific surface area, recirculation, and ventilation.
≈The fundamental construction elements are consistent, describing a filter structure, media bed, an underdrainage system for air/water flow, and a rotary distributor or fixed nozzle system for wastewater application.
≈All standards share the primary objective of designing a robust system to achieve a target effluent quality (BOD, TSS) while preventing common operational problems like media clogging, odors, and filter flies.
Parameter Comparison
ParameterIS ValueInternationalSource
Organic Loading (High-Rate, Rock Media)0.8 to 3.2 kg BOD/m³/day0.4 to 2.4 kg BOD/m³/dayWEF MOP No. 8
Hydraulic Loading (Low-Rate)1.1 to 4.4 m³/m²/day1.0 to 4.0 m³/m²/dayWEF MOP No. 8
Media Depth (Conventional/Rock Media)1.5 to 3.0 m2.0 to 6.0 m (for single stage)DWA-A 281E
Media Size (Conventional/Rock Media)25 to 100 mm25 to 100 mmWEF MOP No. 8
Underdrain Channel SlopeNot less than 1 in 100 (1%)Typically 1% to 2%WEF MOP No. 8
Rotary Distributor SpeedOne revolution in 1 to 10 minutes0.3 to 2 rpm (one revolution in 0.5 to 3.3 minutes)WEF MOP No. 8
Minimum Wetting RateNot explicitly specified as a numerical rate.Recommended > 0.4 L/(m²·s) to ensure full wetting.DWA-A 281E
⚠ Verify details from original standards before use

Key Values7

Quick Reference Values
F/M Ratio for Conventional ASP0.2 - 0.4 kg BOD/kg MLVSS/day
MLSS for Conventional ASP1500 - 3000 mg/l
Hydraulic Retention Time for Extended Aeration18 - 36 h
Sludge Age for Extended Aeration20 - 30 days
Surface Overflow Rate for Secondary Clarifier (Avg Flow)12 - 20 m³/m²/day
Solids Loading Rate for Secondary Clarifier40 - 120 kg/m²/day
Minimum Freeboard in Aeration Tank0.6 m
Key Formulas
F/M Ratio = (Q × S₀) / (V × Xᵥ) — Food to Microorganism Ratio
Sludge Age (SRT) = (V × X) / (Qw × Xw + Qe × Xe) — Solids Retention Time
Surface Overflow Rate (SOR) = Q / A — Clarifier Sizing
Solids Loading Rate (SLR) = (Q + Qr) × X / A — Clarifier Sizing

Tables & Referenced Sections

Key Tables
Table 1 - Design Parameters for Activated Sludge Process and its Modifications
Table 2 - Design Parameters for Secondary Settling Tank
Key Clauses
Clause 4 - Process Design Considerations
Clause 5.2 - Aeration Tank
Clause 5.3 - Secondary Clarifier (Settling Tank)
Clause 5.4 - Sludge Return System
Clause 6 - Aeration Systems

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Frequently Asked Questions5

What is the typical F/M ratio for an Extended Aeration plant?+
0.05 to 0.15 kg BOD per kg MLVSS per day, as per Table 1.
What is the recommended surface overflow rate (SOR) for a secondary clarifier at average flow?+
12 to 20 m³/m²/day, as per Table 2.
What should be the minimum freeboard in an aeration tank?+
A minimum of 0.6 m should be provided above the top water level (Clause 5.2.3).
What are the typical MLSS concentrations for a conventional activated sludge process?+
1500 to 3000 mg/l, as per Table 1.
What is the typical sludge age (SRT) for a conventional ASP?+
5 to 15 days, as per Table 1.

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