Adhāra Viveka

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Plastic Pyrolysis

Emission Control System

A three-stage emission control system — cyclone, wet scrubber, and bag filter — treats furnace flue gas in series, with each stage targeting a different pollutant size and type before the cleaned gas exits through the chimney stack.

Left-to-right process flow diagram of a three-stage emission control system showing furnace flue gas entering a cyclone separator on the left that removes coarse particles, then a wet scrubber in the centre removing acid gases and fine particles through water spray contact, then a bag filter on the right capturing fine PM2.5 and PM10 particles, then an induced draft fan, then a chimney stack at far right, with pollutant type labels at each stage removal point
Left-to-right process flow diagram of a three-stage emission control system showing furnace flue gas entering a cyclone separator on the left that removes coarse particles, then a wet scrubber in the centre removing acid gases and fine particles through water spray contact, then a bag filter on the right capturing fine PM2.5 and PM10 particles, then an induced draft fan, then a chimney stack at far right, with pollutant type labels at each stage removal point
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How to read this sketch

This is a left-to-right process flow. Flue gas flows from left to right, becoming cleaner at each stage. Read as follows:

  • Each stage box: One treatment unit with its symbol and removal target labelled.
  • Downward arrows (at cyclone and scrubber): Collected pollutant streams (ash from cyclone, effluent from scrubber) exit downward for disposal or treatment.
  • Temperature labels: 350°C at flue gas inlet, dropping to ~70°C after scrubber (saturation temperature). Below 120°C required before bag filter.
  • Caption: 'Three stages, three different pollutants — each box handles what the previous one couldn't.'

About this sketch

Furnace flue gas from a plastic pyrolysis plant contains three categories of pollutants: coarse fly ash and char particles, water-soluble acid gases (HCl from PVC contamination, SO₂ from sulphur in plastic additives), and fine particulate matter (PM10, PM2.5). No single piece of equipment removes all three effectively — which is why the emission control system uses three different technologies in series, each doing what the others cannot.

Stage 1 — Cyclone separator: Hot flue gas (350°C or above) enters the cyclone tangentially, spinning at high velocity. Centrifugal force pushes heavier particles (above 10–20 microns — coarse fly ash, char fines) to the cyclone wall and down into the collection hopper. Clean gas exits the cyclone top. The cyclone is a purely mechanical device with no consumables — the only maintenance is periodic ash hopper emptying. It handles 70–90% of the total particulate mass load but cannot remove fine PM2.5 particles.

Stage 2 — Wet scrubber: Gas from the cyclone enters the scrubber where it contacts a water or alkaline solution spray. Fine particles (2–10 micron range) are captured by the water droplets. More importantly, water-soluble acid gases (HCl, SO₂) dissolve into the scrubber liquid, which is collected at the bottom as a slightly acidic or alkaline effluent. This effluent must be neutralised and treated before discharge or recycling. The scrubber reduces gas temperature to near its saturation point (50–70°C), which also helps the downstream bag filter work within its temperature limit.

Stage 3 — Bag filter (fabric filter): Fine particles (0.5–5 microns — the PM2.5 and PM10 range that both the cyclone and scrubber miss) are captured on the fabric bags as gas passes through them. Bags are periodically cleaned by pulse-jet or mechanical shaking. Bag filter performance is typically PM below 30 mg/Nm³ at the outlet, meeting CPCB norms. The ID fan after the bag filter maintains negative pressure throughout the train.

Key insights

  • The cyclone, scrubber, and bag filter each target a different pollutant type — no single stage can do all three jobs, which is why all three are needed in series.
  • The wet scrubber is specifically needed when PVC-contaminated feedstock is processed — it is the only stage that removes HCl gas from the flue stream.
  • Gas must be cooled below 120°C (by the scrubber stage) before entering the bag filter — temperatures above this damage the glass fibre or PTFE bag filter fabric.
  • CPCB norms require particulate matter at the stack to be below 50 mg/Nm³ — the three-stage system typically achieves 20–30 mg/Nm³, providing a compliance margin.
  • Scrubber effluent (acidic water with absorbed HCl and SO₂) cannot be discharged to drains without neutralisation — this effluent must be pH-adjusted and treated before disposal.

Frequently asked questions

Does the wet scrubber need a permit for its effluent discharge?

Yes — scrubber effluent is a liquid waste containing absorbed pollutants (HCl, SO₂, fine particulates). It requires treatment before discharge. In a zero-liquid-discharge (ZLD) setup, the scrubber liquid is recirculated with periodic bleed and neutralisation. If discharged to a municipal drain or body of water, it requires a consent under the Water (Prevention and Control of Pollution) Act with applicable effluent standards met.

What is the difference between a wet scrubber and a dry scrubber?

A wet scrubber uses liquid (water or alkaline solution) to absorb and remove pollutants — effective for acid gases and fine particles but generates liquid effluent requiring treatment. A dry scrubber injects dry alkaline powder (lime, sodium bicarbonate) into the gas stream to react with acid gases, generating dry powder for disposal. Dry scrubbers avoid liquid effluent but are less effective for particle removal and have higher consumable costs.
Last updated: Jun 11, 2026 License
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