China discharge standards under GB 8978-1996 set Class 1 limits for other discharge units at COD 100 mg/L, TSS 70 mg/L, and NH₃-N 15 mg/L. Petrochemical plants and municipal secondary works use Class 1 COD 60 mg/L in the same Table 4. Municipal plants discharging to sensitive waters must also meet GB 18918-2002 Grade 1A: COD ≤ 50 mg/L, TSS ≤ 10 mg/L, and NH₃-N ≤ 5 mg/L when water temperature is above 12°C.
Which China discharge class applies to your plant?
China discharge standards assign Class 1, 2, or 3 by receiving-water sensitivity under GB 3838, not by industry type alone. Class 1 covers direct discharge to Class III waters or sensitive coasts; Class 2 covers Class IV–V; Class 3 covers sewer discharge to a municipal WWTP. Misreading the receiving-water class commonly causes undersized tertiary stages and failed commissioning checks.
Determining the applicable discharge class is the first step in sizing a treatment train and securing an environmental permit from the Ministry of Ecology and Environment (MEE). Failure to identify the correct receiving water body classification often leads to undersized equipment and immediate inspector rejection during the commissioning phase. In the Chinese regulatory framework, the discharge limit is driven by the sensitivity of the destination water body.
What wastewater effluent discharge standards apply?
Direct industrial outfalls follow GB 8978-1996 Class 1, 2, or 3. Municipal WWTP outfalls follow GB 18918-2002 Grade 1A or 1B. Industry-specific GB standards (for example electroplating GB 21900 or textile GB 4287) override the integrated standard where they apply.
Which industrial wastewater discharge limits bind your outfall?
Class 1 applies to facilities discharging directly into Class III surface water bodies (as defined by GB 3838) or sensitive coastal zones. Class III waters are designated as Grade II protection zones for centralized drinking water sources or general fish sanctuaries. For an EPC engineer, Class 1 is a high-compliance threshold where standard biological treatment often needs tertiary polishing to stay stable.
Class 2 is designated for plants discharging into Class IV or V surface water bodies, typically industrial zones or non-sensitive agricultural water areas. While the limits are more relaxed than Class 1, many provincial authorities now "up-class" these requirements to meet regional watershed goals, which effectively makes Class 1 the de facto design standard for new industrial parks.
Class 3 applies to indirect discharge, where an industrial facility pre-treats its effluent before sending it to a municipal wastewater treatment plant (WWTP) via a sewer network. A critical caveat applies: if the industrial wastewater accounts for more than 30% of the municipal plant's total hydraulic or organic load, the MEE frequently mandates that the industrial pretreatment must meet GB 8978 Class 1 standards to prevent biological upset at the municipal facility.
If your effluent enters a municipal plant, you must distinguish between Municipal Grade 1A and Grade 1B (GB 18918-2002). Grade 1A is the standard for plants discharging into major river basins like the Yangtze or Pearl River. If your client is an EPC for a municipal project, Grade 1A is the mandatory benchmark, necessitating high-performance technologies such as a compact MBR that delivers Grade A effluent consistently across seasonal temperature fluctuations.
GB 8978-1996 Class 1, 2, 3 numeric limits (quick table)
The following table summarizes the maximum allowable discharge concentrations for the top 20 pollutants monitored by MEE inspectors. These figures represent a commonly used national design baseline; engineers must still check provincial "DB" standards (e.g., DB32 in Jiangsu), which may impose stricter limits on specific ions or organic compounds.
| Pollutant Parameter | Unit | Class 1 | Class 2 | Class 3 |
|---|---|---|---|---|
| pH Value | - | 6–9 | 6–9 | 6–9 |
| Color (Dilution Ratio) | - | 50 | 80 | - |
| Suspended Solids (SS) | mg/L | 70 | 150 | 400 |
| COD (Chemical Oxygen Demand) | mg/L | 60 | 100 | 500 |
| BOD5 (Biochemical Oxygen Demand) | mg/L | 20 | 30 | 300 |
| Ammonia Nitrogen (NH₃-N) | mg/L | 15 (10*) | 25 | - |
| Total Nitrogen (TN) | mg/L | 15 | 20 | - |
| Total Phosphorus (TP) | mg/L | 0.5 | 1.0 | - |
| Petroleum/Oils | mg/L | 5 | 10 | 20 |
| Volatile Phenols | mg/L | 0.5 | 0.5 | 2.0 |
| Total Cyanide (CN) | mg/L | 0.5 | 0.5 | 1.0 |
| Fluoride (F) | mg/L | 10 | 10 | 20 |
| Total Zinc (Zn) | mg/L | 2.0 | 5.0 | 5.0 |
| Total Copper (Cu) | mg/L | 0.5 | 1.0 | 2.0 |
| Total Nickel (Ni) | mg/L | 1.0 | 1.0 | 1.0 |
| Hexavalent Chromium (Cr VI) | mg/L | 0.5 | 0.5 | 0.5 |
| Total Lead (Pb) | mg/L | 1.0 | 1.0 | 1.0 |
| Total Cadmium (Cd) | mg/L | 0.1 | 0.1 | 0.1 |
| Total Arsenic (As) | mg/L | 0.5 | 0.5 | 0.5 |
| Total Mercury (Hg) | mg/L | 0.05 | 0.05 | 0.05 |
Note on 2021 Yangtze Delta tightenings: Per the MEE Circular issued in late 2021, facilities located within the Yangtze River Economic Belt are now subject to "Special Discharge Limits." For Class 1 discharge in these zones, NH₃-N is effectively tightened to 5 mg/L and Total Phosphorus (TP) is capped at 0.3 mg/L for any discharge entering eutrophic-sensitive lakes such as Taihu—as china, for instance, mandates that effluent total phosphorus concentrations remain below 0.3 mg p l-1 under its national first-class discharge standard. When designing for these regions, engineers should compare USA effluent limits side-by-side with China to understand how high-density industrial zones drive these aggressive standards.
Municipal GB 18918-2002 Grade A vs Grade B

Municipal discharge standards in China are often more stringent than industrial standards because they account for the massive cumulative volume of domestic and industrial co-treatment. GB 18918-2002 is the primary regulatory document for these facilities. For an EPC engineer, the choice between Grade 1A and Grade 1B dictates whether tertiary filtration or membrane bioreactors are necessary.
Grade 1A is the high benchmark for environmental compliance in China. It requires COD ≤ 50 mg/L, BOD ≤ 10 mg/L, and SS ≤ 10 mg/L. The NH₃-N limit is 5 mg/L when water temperature is above 12°C and 8 mg/L below 12°C. Meeting these limits requires a robust biological process with integrated nitrification and denitrification. Most modern plants use MBR technology to eliminate secondary clarifiers, which struggle to hit the 10 mg/L SS limit reliably.
Grade 1B allows COD up to 60 mg/L and SS up to 20 mg/L. While common a decade ago, this standard is now largely reserved for inland regions with high dilution capacity in the receiving water. If your industrial stream exceeds 30% of the total plant load, your pretreatment must reach GB 8978 Class 1 levels before the municipal sewer will accept the water. Failure to do so can result in the municipal operator refusing the connection, citing biological inhibition risk.
Technology selection to meet COD 50 mg/L and NH₃-N 5 mg/L
Achieving the Grade 1A benchmark of COD 50 mg/L and NH₃-N 5 mg/L requires a multi-stage approach. Standard activated sludge processes typically plateau at COD 80–100 mg/L and NH₃-N 10–15 mg/L when treating industrial influent. To bridge the gap, unit operations must focus on deep nutrient removal and advanced oxidation.
Deep Denitrification + MBR: HydropureWater field data (2023) indicates that a modified A2O (Anaerobic-Anoxic-Oxic) process followed by an MBR membrane achieves NH₃-N < 2 mg/L and TN < 10 mg/L consistently. The MBR acts as an absolute barrier to suspended solids, which reduces particulate-associated COD. This setup is ideal for plants with limited footprint, operating at MLSS concentrations of 8,000 to 12,000 mg/L. You can see detailed MBR vs SBR energy and footprint data to justify the higher CAPEX of MBR in sensitive zones.
Ozone-BAF Combo: For industrial wastewater containing refractory organics, biological treatment alone will fail the COD 50 mg/L limit. An Ozone-Biological Aerated Filter (BAF) combination is the proven solution. Ozone breaks down complex aromatic rings into simpler biodegradable acids, which the BAF then consumes. Field results show this combo can cut COD from 120 mg/L down to 42 mg/L at an Empty Bed Contact Time (EBCT) of 45 minutes.
Upstream DAF for TSS Control: High suspended solids interfere with both UV disinfection and membrane longevity. A high-rate DAF for Class 1 TSS pretreatment can reduce influent TSS by over 90% before it reaches the biological stage. This protects the downstream membranes and keeps final effluent SS below 10 mg/L.
| Technology Module | Primary Pollutant Target | Removal Efficiency | Footprint Requirement |
|---|---|---|---|
| Dissolved Air Flotation (DAF) | TSS, Fats/Oils | 85–95% | Low (0.5 m²/m³/h) |
| MBR (Membrane Bioreactor) | COD, SS, NH₃-N | 98% (SS), 90% (COD) | Medium (1.2 m²/m³/h) |
| Ozone Oxidation | Refractory COD | 30–50% | Low (0.3 m²/m³/h) |
| Denitrification Deep Bed Filter | TN, TP, SS | 70–85% (TN) | High (2.5 m²/m³/h) |
Cost benchmarks: CAPEX per m³/h to hit Class 1

For an EPC engineer, budgeting is as critical as the process flow diagram. Reaching Class 1 or Grade 1A limits involves higher capital expenditures due to the addition of tertiary treatment and advanced controls. The following benchmarks are based on 2024–2025 market rates for modular and site-built plants in China.
Small Scale (10 m³/h): For decentralized industrial units, a modular MBR plant is the standard choice. CAPEX is approximately US$130,000 ±15%. This includes containerized housing, PVDF membranes, automated PLC control, and chemical dosing skids. These units are "plug-and-play" and are often used by factories to meet Class 1 standards quickly after an inspector warning.
Medium Scale (100 m³/h): A traditional train of DAF pretreatment, activated sludge, and a tertiary cloth disk filter or MBR will cost roughly US$0.95M ±10%. At this scale, civil works (concrete basins) account for 40% of the cost, while mechanical equipment and membranes account for 60%.
Large Scale (1,000 m³/h): Large industrial park WWTPs requiring ozone polishing and deep denitrification filters see CAPEX rise to US$5.8M ±20%. The increase is driven by the ozone generation system and the larger footprint required for denitrification basins.
OPEX Considerations: Operational costs are dominated by electricity and chemicals. To hit Class 1, expect energy consumption of approximately 0.9 kWh per kg of COD removed. Chemical costs (PAC, PAM, and carbon sources like acetate) typically range from US$0.15 to US$0.30 per cubic meter of treated water, depending on the influent nutrient load.
Compliance checklist for MEE site inspection
Passing a Ministry of Ecology and Environment (MEE) site inspection requires more than clean water; it requires a documented, verifiable system of "continuous compliance." Inspectors focus heavily on data integrity and emergency preparedness.
- Online Monitoring Integration: It is mandatory to have online meters for pH, COD, NH₃-N, and TP. These meters must be MEE-certified and equipped with a data acquisition system (DAS) that transmits real-time values to the provincial environmental platform. Any "flatline" data or missing intervals are flagged as potential tampering.
- Emergency Backup Basin: An inspection will fail if there is no provision for upset events. A backup basin (or "accident pool") must be sized for at least 4 hours of peak hydraulic retention. This allows the plant to divert off-spec effluent during a process failure rather than discharging it illegally.
- Sludge Management: You must demonstrate a legal disposal route for sludge. A filter press that cakes sludge to 60% solids for hazardous waste hauler is the industry standard. Inspectors will check the "Five-聯" (five-part) manifest system to ensure every ton of sludge is accounted for from the plant to the licensed disposal facility.
- Flow Meter Calibration: Ensure influent and effluent flow meters are calibrated annually. Discrepancies between the two (beyond 5–10% evaporation/sludge loss) can trigger an audit of illegal bypass pipes.
Who this is for: EPC contractors and plant engineers designing or upgrading industrial or municipal WWTPs discharging in mainland China. Who should look elsewhere: readers targeting Taiwan, Hong Kong, or Southeast Asia effluent rules, or those needing detailed reactor sizing formulas, should request the relevant local guide. For a process selection tied to your influent profile, send your flow sheet to our engineers via request a quote with influent data and we will return a Class 1 or Grade 1A train recommendation.
Frequently Asked Questions

Does GB 8978-1996 still apply in 2025?
Yes, it remains the national baseline standard for industries without a dedicated sector standard. Many specific industries (e.g., Electroplating GB 21900, Textile GB 4287) have their own dedicated standards that override the "Integrated" standard, so always check for industry-specific GB standards first before specifying GB 8978. Provincial DB standards may also impose stricter local limits.
What is the penalty for exceeding Class 1 limits in the Yangtze Delta?
Under the Water Pollution Prevention and Control Law, specified illegal discharges can draw fines of 100,000 to 1,000,000 RMB. If the violator fails to correct after being ordered to do so, daily continuous penalties apply under the Environmental Protection Law until the violation is rectified, and responsible managers can face administrative detention. Facilities within the Yangtze River Economic Belt also face the "Special Discharge Limits" tightened in late 2021.
Can I use SBR to hit COD 50 mg/L?
It is possible but risky for industrial influent. SBRs often suffer from sludge bulking or poor settling, which causes TSS to spike above 20 mg/L and pushes the COD above the 50 mg/L limit. MBR is the safer choice when guaranteed compliance is required.
What CAPEX should I budget for a 100 m³/h Class 1 plant?
A DAF + activated sludge + MBR train at 100 m³/h typically runs about US$0.95M ±10%, with civil works near 40% of the total. Add 20–30% contingency when ozone polishing or deep denitrification is required for the Yangtze Delta "Special Discharge Limits."
How do I know whether to apply industrial or municipal limits?
If your effluent goes directly to a receiving water body, apply GB 8978-1996 Class 1, 2, or 3 based on that water body's GB 3838 classification. If your effluent enters a municipal sewer, the receiving WWTP's GB 18918-2002 Grade 1A or 1B becomes the effective ceiling, and pretreatment to GB 8978 Class 1 is typically required when your stream exceeds 30% of plant load.