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STEEL INDUSTRY ETP CASE STUDY

How a 3600 KLD Steel Plant Eliminated 99.5% Cyanide & 99.2% Phenol

Industry: Steel Manufacturing (Coke Oven Effluent, HR/CR Plates, Galvanised Sheets, Pipes)


Plant Location: Eastern India  |  Plant Capacity: 3,600 m³/day (3.6 MLD)


Core Tech: Aeration Tanks, Anoxic Tanks, MBR & RO Recycling

99.5%

Cyanide Degradation (6.5 → 0.031 mg/L)

99.2%

Phenol Reduction (250 → 2.0 mg/L)

94.3%

Thiocyanate Degradation (350 → 20 mg/L)

Aerobic and Nutrient Removal Bioculture Combo for Toxic Coke Oven Effluent

BactaServe Aerobic & Nutrient Removal

Specialised Strains for Toxic Coke Oven Effluent

This pharmaceutical wastewater treatment case study explains how a 30 KLD Oral Cephalosporin API manufacturing plant commissioned its Up-flow Anaerobic Sludge Blanket Reactor (UASBR) in just 25 days using BactaServe Anaerobic. The project achieved 85 to 90% COD reduction, maintained a stable VFA to alkalinity ratio of 0.18, and established healthy granular sludge formation without using conventional seed sludge.

1. Background & Technical Challenge

Plant Overview

Coke production in integrated steel facilities generates highly toxic, refractory wastewater containing cyanides, thiocyanates, phenols, and heavy nitrogen loads. A major steel manufacturer in Eastern India operates a 3,600 m³/day (3.6 MLD) state-of-the-art ETP. To enable complete Reverse Osmosis (RO) recycling, the wastewater must undergo total biological breakdown of organic and inorganic toxins before reaching MBR and RO membranes.

The Technical Challenge & Risk

  • High Chemical Toxicity: Raw baseline of 6.5 ppm Cyanide (CN), 350 ppm Thiocyanate (SCN), and 250 ppm Phenol.

  • Ammonia Spikes: Degradation of thiocyanates releases additional free ammonia (NH₃-N), pushing total nitrogen up to 400 ppm.

  • Low BOD:COD Ratio: Organic carbon availability for biological denitrification was severely constrained.

  • Membrane Fouling Risk: Incomplete toxic breakdown rapidly fouls downstream MBR and RO units, triggering severe operational downtime.

2. Treatment Process Flow Diagram

Treatment process flow diagram of the steel plant effluent treatment plant showing the wastewater treatment process and key treatment units.

3. Specialised Solution: BactaServe Anaerobic

Steel plant effluent treatment plant where BactaServe™ Aerobic was implemented.

Project Site

Ready to Solve Complex Effluent Toxicity Issues?

Let our bio-engineers analyze your coke oven or chemical effluent parameters to design a tailored strain-selection and dosing protocol.

Step 1: Share your inlet COD, BOD, and flow parameters.

Step 2: Our bio-engineers analyze your process flow diagram.

Step 3: Receive a custom BactaServe dosing protocol with performance guidance.

Download Product Brochure

Frequently Asked Questions

Q1: How do you remove cyanide and phenol from steel plant wastewater biologically?

Q2: What bacteria degrade thiocyanate in industrial wastewater?

Q3: How does bio-augmentation protect MBR and RO membranes in steel plant ETPs?

Q4: Why does ammonia increase during thiocyanate degradation in wastewater?

Q5: How long does it take to achieve 99% phenol removal in an industrial ETP?

Q6: What is the dosing schedule for BactaServe in a 3.6 MLD steel plant ETP?

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