+91 93211 61989kshitij@kkenviro.in
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Pharmaceutical Effluent Treatment Plant (Pharma ETP)

Solvents, high COD, toxic and biorefractory compounds, antibiotics that inhibit biology, batch-wise discharges — pharma effluent needs segregation, stripping, robust biology and often ZLD. We have designed for API, intermediate and formulation plants.

The effluent and the norms

API and intermediate plants generate concentrated mother liquors (COD 20,000–100,000 mg/L) alongside dilute wash water; solvents (methanol, toluene, DCM), high ammonia, sulphates and salts are common; formulation plants are milder but carry surfactants and actives. Norms include COD, BOD, TDS, ammoniacal nitrogen and, increasingly, antibiotic-residue expectations; many API units are under ZLD directions.

Treatment train we design

  1. Stream segregationHigh-COD/high-TDS mother liquors separated from dilute streams at source — the single most important design decision.
  2. Pre-treatment of concentratesSolvent stripping/recovery, ammonia stripping, MEE for high-TDS liquors, incineration or TSDF for residues.
  3. Physico-chemicalNeutralisation, coagulation, Fenton/ozone for toxicity reduction where biology would be inhibited.
  4. BiologicalAnaerobic (UASB/anaerobic filter) for high-COD streams followed by aerobic MBBR/MBR with long SRT; nitrification–denitrification for ammonia.
  5. Tertiary and reusePSF/ACF, UF + RO for 70–80 % reuse to cooling and utilities.
  6. ZLDRO reject to MEE/MVR + crystalliser/ATFD; condensate reused.

Where we apply it

API and bulk-drug plants
Hyderabad, Vizag, Ankleshwar, Tarapur, Taloja clusters.
Formulation and OSD plants
Milder effluent, GMP-documented plants.
Biotech and fermentation
High-BOD spent broth, anaerobic-first design.
R&D and pilot plants
Small, highly variable streams; batch treatment.

How KK Enviro Engineers delivers

Sampling plan and inlet characterisation → process design (PFD, P&ID, sizing, BOQ) → supply, erection and commissioning → biological stabilisation → handover with O&M manual and training → AMC if you want us to stay. We also audit and upgrade plants built by others.

Frequently asked questions

Why does biology fail in pharma ETPs?

Toxic shock from un-segregated concentrates, solvents and antibiotics. Segregation, pre-treatment of concentrates and a buffer/equalisation stage protect the biomass; MBR with long sludge age tolerates variability better.

Do we need ZLD?

If your consent says so, yes. Otherwise a good reuse train (UF+RO) with reject to CETP is often the economical choice; we compare both on lifecycle cost.

Can you handle solvent-bearing streams?

Yes — stripping and recovery are designed upstream of biology; recovered solvent has value and the ETP is protected.

Send your effluent data

Flow, inlet analysis and required outlet — we reply with a scheme and budget range within one working day.