NMCG STP Standards: What Changed and Why
The National Mission for Clean Ganga (NMCG) operates under the Ministry of Jal Shakti as the implementing authority for the Namami Gange programme. Launched in 2014 with a budget outlay of ₹20,000 crore, Namami Gange identified inadequate sewage treatment as the dominant source of Ganga pollution — accounting for approximately 75–80% of total organic load entering the river. Legacy STPs built in the 1970s–90s were designed to CPCB's general inland water standard of BOD ≤30 mg/L, TSS ≤100 mg/L — standards that proved inadequate to protect the river's designated use as bathing water.
In 2017, NMCG issued revised STP performance standards for all towns in the Ganga basin, prescribing:
- BOD ≤10 mg/L — one-third of the old 30 mg/L standard; requires tertiary-quality biological treatment
- TSS ≤20 mg/L — requires either secondary clarifier with tertiary polishing or MBR
- Fecal coliform ≤230 MPN/100 mL — requires active disinfection (UV or chlorination), not just adequate BOD removal
- TN ≤10 mg/L and TP ≤1 mg/L — for larger STPs (≥50 MLD) in designated stretches, addressing eutrophication of the river system
These standards were set to achieve "bathing quality" water (Class B under CPCB classification, BOD <3 mg/L in river) at key ghats — Haridwar, Allahabad, Varanasi, and Kolkata. The jump from 30 mg/L to 10 mg/L is technically significant: it moves the requirement from conventional secondary treatment to advanced secondary or secondary-plus-tertiary treatment.
The NGT has repeatedly directed states to comply with NMCG standards through a series of orders from 2018–2024, setting progressive deadlines and imposing environmental compensation on defaulting ULBs and state agencies. The Supreme Court has also intervened directly in Ganga cleaning, giving the programme constitutional backing.
Towns and Rivers Covered Under NMCG
The NMCG mandate applies to all urban local bodies (ULBs) — municipal corporations, municipalities, and town panchayats — in the five Ganga basin states that drain to the Ganga main stem or its principal tributaries. The designated tributaries include the Yamuna, Ramganga, Ghaghra (Saryu), Gandak, Kosi, Son, Damodar, and Hooghly.
Priority Towns
NMCG classified 97 towns on the main Ganga stem as Priority-1 (direct discharge to river) and an additional 200+ towns on major tributaries as Priority-2. Priority-1 towns were expected to have functional, NMCG-compliant STPs by 2020 — a deadline extended multiple times.
The largest cities — Kanpur (Class I, population 3+ million), Prayagraj, Varanasi, Patna, and Kolkata — have the largest STP capacity gaps and the most visible NGT monitoring. Kanpur's Jajmau STP complex and the CETP serving tanneries are specifically named in NGT orders.
Tributary Standards
For towns discharging to tributaries rather than the main stem, some states have implemented transitional standards (BOD ≤20 mg/L for smaller Class II towns) pending infrastructure development, but the prescribed NMCG standard of BOD ≤10 mg/L remains the target for all Ganga basin STPs.
Industrial Estates in Ganga Basin
CETPs in the Ganga basin are also subject to NMCG standards for their discharge. This is particularly relevant for Kanpur leather CETPs and UP agro-processing clusters discharging to Ganga tributaries.
Technology Requirements to Meet BOD <10 mg/L
Meeting BOD ≤10 mg/L reliably requires a step-change in treatment approach. The conventional activated sludge process (ASP) with secondary clarifier can achieve this on paper — at very long SRT (15–20 days) and with consistent plant operation — but struggles in municipal practice due to:
- Monsoon dilution: influent BOD drops 3–5× during rain events (I/I — inflow and infiltration from leaking sewers), which disrupts biological equilibrium
- Sludge settleability: bulking events in conventional clarifiers produce high TSS effluent even when BOD removal is adequate
- Operating staff capability: Indian ULBs face chronic shortfalls in trained operators; technologies requiring more precise control increase failure risk
Technologies that reliably achieve BOD ≤10 mg/L in municipal wastewater:
- MBR (Membrane Bioreactor): Achieves BOD ≤5 mg/L and TSS ≤2 mg/L by definition (complete membrane filtration). Also meets fecal coliform standard without separate disinfection in most cases. Capital cost 30–50% higher than MBBR; membrane replacement cost at year 8–10 is a lifecycle consideration. Best for space-constrained urban sites and where treated water reuse is planned.
- MBBR + Tertiary Disc Filter: MBBR's high biomass density (8,000–12,000 mg/L VSS-equivalent in carrier biofilm) enables BOD removal to ≤15 mg/L in secondary; tertiary polishing filter brings this to ≤10 mg/L. Disc filters (rotating cloth media filters) are compact, low-energy, and well-suited to NMCG retrofit projects.
- SBR (Sequencing Batch Reactor): SBR with extended react phase achieves BOD ≤10 mg/L with good decant design. SBR is particularly effective for variable flows and is widely used in Ganga basin STP projects. NMCG's design guidelines have standardised SBR as a preferred technology for new STPs.
- UASB + MBBR (for larger flows): For STPs ≥10 MLD, UASB pre-treatment followed by MBBR polishing is a cost-effective approach used by several NMCG projects in Bihar and UP. UASB removes 60–70% of BOD anaerobically (with biogas recovery), reducing the load on the aerobic MBBR stage.
MBBR Retrofit: The Most Practical Upgrade Path
For the large installed base of ASP STPs in the Ganga basin — most built in the 1980s–2000s under NRCP and JNNURM — MBBR retrofit is the most practical and cost-effective upgrade path. The retrofit involves:
Phase 1 — Media installation: Carrier media is added to existing aeration tanks (no civil reconstruction required). Coarse-bubble diffusers are replaced with fine-bubble disc diffusers. Media retention screens are installed at tank outlets. Blower capacity may need to be increased by 15–25% for fine-bubble systems.
Phase 2 — Tertiary stage: A compact disc filter or rapid sand filter is installed downstream of the existing secondary clarifier. The clarifier is retained for sludge settlement; the tertiary filter handles solids polishing.
Phase 3 — Disinfection upgrade: UV disinfection system sized for peak flow is added to meet fecal coliform ≤230 MPN/100 mL. UV dose of 40–60 mJ/cm² is adequate for municipal STP effluent at the NMCG TSS standard.
The primary advantage of MBBR retrofit is that it increases both treatment quality (BOD 30 → 10 mg/L) and treatment capacity (2–3× hydraulic capacity) from the same civil infrastructure. Many Ganga basin STPs are also capacity-constrained — receiving more flow than design capacity — making the dual benefit particularly valuable. The MBBR for municipal STP guide covers design parameters for retrofit projects in detail.
Typical MBBR retrofit costs for existing ASP STPs of 10–50 MLD capacity range from ₹2–4 crore per MLD, significantly less than new-build STP costs of ₹5–8 crore per MLD.
Nitrogen and Phosphorus Removal Requirements
For STPs ≥50 MLD in designated Ganga tributaries, NMCG requires TN ≤10 mg/L and TP ≤1 mg/L. These nutrient removal standards are aimed at preventing eutrophication of the Ganga system and protecting Farakka Barrage reservoir water quality.
Biological Nitrogen Removal
Achieving TN ≤10 mg/L from typical municipal sewage (TKN 40–60 mg/L inlet) requires both nitrification and denitrification. The process sequence is: anoxic zone (denitrification, 30% of aeration volume) → aerobic zone (nitrification) → anoxic polishing zone. Internal recycle ratio of 3–4× is needed to achieve 70–80% total nitrogen removal. MBBR can be configured for simultaneous nitrification– denitrification (SND) in alternating zones, reducing reactor volume requirement by 20–25%. See thebiological nitrogen removal guide for detailed design parameters.
Phosphorus Removal
Biological phosphorus removal (Bio-P, or EBPR — Enhanced Biological Phosphorus Removal) requires an anaerobic zone upstream of the anoxic zone to enrich polyphosphate-accumulating organisms (PAOs). Bio-P can achieve TP removal to 1–2 mg/L. For more stringent requirements (TP ≤1 mg/L), chemical precipitation using alum (aluminium sulphate) or ferric chloride as a polishing step is added after secondary treatment. Chemical dosing costs approximately ₹8–15 per m³ of sewage treated.
Monitoring, Reporting, and ICCC Connectivity
NMCG has established an Integrated Command and Control Centre (ICCC) at Haridwar that aggregates real-time telemetry from STPs across the Ganga basin. STPs funded under Namami Gange are required to connect to the ICCC system and transmit:
- Influent flow (m³/hour)
- Treated effluent flow (m³/hour)
- Online BOD or TOC proxy (UV-Vis analyser or TOC analyser)
- TSS (online turbidity transducer with correlation to actual TSS)
- pH
- Dissolved oxygen in aeration tank (proxy for process health)
The ICCC generates automated alerts when STP outlets exceed standards for more than 2 consecutive hours. Alerts trigger field inspection by state SPCB. NMCG also publishes monthly STP performance reports by state and town, creating public accountability.
In addition to ICCC connectivity, NMCG requires: quarterly NABL-laboratory sampling of treated effluent; annual third-party performance audit submitted to both SPCB and NMCG; monthly operator logbook submission.
NMCG Funding and Project Implementation
NMCG provides 100% central funding for sewage infrastructure projects (STP construction, sewer network, and pump stations) for states that enter into NMCG agreements under the National Ganga Plan. Project implementation follows a hybrid annuity model (HAM) or EPC model depending on size:
- HAM (Hybrid Annuity Model): Used for STPs ≥20 MLD. The private developer constructs and operates for 15 years; NMCG pays 40% during construction and the balance as annuity against performance. This model transfers O&M risk to the private operator — creating a strong incentive to meet BOD ≤10 mg/L continuously.
- EPC with O&M contract: Used for smaller STPs. Public agency (NMCG/state JV) contracts construction on EPC basis, followed by a 5–10-year O&M contract. O&M payments are performance-linked to ICCC data.
For local bodies operating existing STPs outside Namami Gange funding — particularly for upgrades to meet NMCG standards — state AMRUT (Atal Mission for Rejuvenation and Urban Transformation) funds can be accessed. AMRUT 2.0 includes sewage treatment as a priority component.
If your municipality or engineering consultancy is planning an STP upgrade or new STP to meet NMCG standards, contact Spans Envirotech for a feasibility study and technology selection. We offer MBBR retrofit design, full EPC, and post-commissioning AMC services for municipal STPs across India. Our municipal sector page covers our project portfolio.
