Welcome to Chongqing XinXie Environmental Protection Equipment Co., Ltd.! 📧 923369385@qq.com  |  WhatsApp: +86 186 2313 6759
TURNKEY PROJECT · NON-FERROUS MELTING

120 t Scrap Copper Melting Furnace
Waste Gas Treatment — Nuomake, Chongqing

A two-train, 160,000 m³/h exhaust system for the 120 t scrap copper melting furnace at Nuomake (Chongqing) Automotive Components: a cooling box and 1,300-bag PTFE pulse baghouse on the 120,000 m³/h furnace-area train, and a wet electrostatic precipitator, multi-stage filter and honeycomb activated carbon train for the 40,000 m³/h furnace-interior stream — engineered for tar fume, VOCs, benzo[a]pyrene and fine metallic dust at 110–160 °C.

Project Overview

One Furnace, Two Streams, 160,000 m³/h

Melting scrap copper releases a difficult mixture: fine metallic dust and sticky tar/asphalt fume, VOCs and benzo[a]pyrene, plus SO₂ and NOₓ — continuously, at 110–160 °C and up to 60% humidity. After on-site survey and calculation, we split the sources into two independently optimized treatment units:

  • ▪
    Train 1 — furnace exterior area, 120,000 m³/h — large area capture hoods connected through the renovated existing duct network, into a cooling/dust-settling box and a 13.5 m-wide pulse baghouse
  • ▪
    Train 2 — furnace interior, 40,000 m³/h — sealed enclosure collection at the charging and slag-skimming ports, into a wet electrostatic precipitator, G4/F7/F9 multi-stage filter and honeycomb activated carbon adsorber
  • ▪
    18 m/s duct transport velocity sized to keep sticky particulate from settling in the header runs
  • ▪
    Code-compliant sampling ports and platforms on both stacks, designed to HJ 75-2017 / GB/T 16157-1996 for third-party monitoring from day one

Key committed values, written into the design documents:

ParameterCommitted Value
Total system airflow160,000 m³/h (120,000 + 40,000)
Baghouse filtration velocity0.8 m/min (1,300 × Ø133 × 3,500 mm PTFE bags)
Particulate removal (baghouse)≥ 99.9%, outlet ≤ 10 mg/m³
WESP dust/mist removal≥ 95%, inlet ≤ 300 → outlet ≤ 30 mg/m³
Activated carbon residence time≥ 0.5 s (6,000 honeycomb blocks, > 700 m²/g)
Stack targetsPM ≤ 10 · SO₂ ≤ 80 · NOₓ ≤ 100 mg/m³
Design gas temperature110–160 °C continuous, humidity ≤ 60%
System Design

Two Trains, Each Matched to Its Pollution Load

Sticky tar fume and high-temperature metallic dust destroy ordinary filters and blind electrostatic fields — so every stage exists for a reason, in the right order.

1 · Cooling & Settling Box

Train 1 first passes a 4,000 × 2,500 × 3,800 mm galvanized cooling box (ΔP ≤ 1,000 Pa, inlet/outlet ≤ 15 m/s): it knocks out coarse dust and trims the 110–160 °C flue gas before the filters — protecting everything downstream.

2 · 120,000 m³/h Pulse Baghouse

A 13,550 × 5,110 × 8,660 mm multi-compartment pulse-jet baghouse with 1,300 PTFE membrane bags (Ø133 × 3,500 mm) rated for continuous duty at 160 °C and short excursions to 300 °C. ≥ 99.9% particulate removal at 0.8 m/min — PTFE's non-stick surface sheds sticky fume and resists SO₂/NOₓ corrosion.

3 · Wet Electrostatic Precipitator

Train 2's BWD360-40000 WESP (264 conductive tubes Ø360 × 6,000 mm, 80 kV / 900 mA) captures what dry systems cannot: sticky tar fume, acid mist, aerosols and sub-micron metal particles, with continuous water-film flushing — no rapping, no re-entrainment, ≥ 95% removal.

4 · G4/F7/F9 Multi-Stage Filter

A modular dry filter (12.6 m² media, ≤ 1.25 m/s) polishes residual dust, oil mist and polymerized matter before the carbon bed — with online differential-pressure transmitters on each stage so filter change-outs are scheduled by data, not by guesswork.

5 · Honeycomb Activated Carbon

6,000 honeycomb carbon blocks (100 × 100 × 100 mm, 1,600 cells, surface area > 700 m²/g) adsorb VOCs and benzo[a]pyrene at ≤ 1.2 m/s with ≥ 0.5 s residence — finishing the furnace-interior stream to a smoke-free, odor-controlled discharge.

6 · Stacks, Ports & Platforms

Sampling ports ≥ 80 mm bore positioned per the 6D/3D straight-run rule, platforms ≥ 1.5 m² with 1.2 m guardrails, 200 kg/m² load rating and 100 mm toe boards — every detail of HJ 75-2017 and GB/T 16157-1996 built in, not bolted on.

More Than Equipment

Designed Against the Book, Verified at the Stack

The whole system was engineered and documented to pass design review and emission monitoring the first time:

  • ✓
    Standards-based design — GB 16297-1996 (integrated emission), GB 37822-2019 (fugitive VOCs), DB51/2377-2017 (stationary-source VOCs), GB 14554-1993 (odor), GB 50019-2015 (industrial ventilation)
  • ✓
    Non-ferrous melting limits — PM ≤ 10 mg/m³, SO₂ ≤ 80 mg/m³, NOₓ ≤ 100 mg/m³ at the stack, monitored at the discharge outlets
  • ✓
    Electrical & safety engineering — HV power supply interlocked with WESP access doors, lightning protection and grounding, per GB 50254 / GB 50054
  • ✓
    WESP long-run design — automatic interval flushing of tubes and electrodes, anti-corona-blocking wide-spacing logic, and critical-spark power control for stable high-voltage operation
  • ✓
    Existing infrastructure reused — the furnace-area duct network was renovated and tied in rather than rebuilt, cutting project cost
  • ✓
    O&M handover — commissioning, operator training, and a consumables schedule covering filter stages and carbon blocks
On-Site Photos

Installed, Insulated and Monitored — at the Nuomake Plant, Chongqing

April–May 2023: the elevated multi-compartment baghouse on the plant facade, pulse valves and blow pipes on the roof platform, the cooling and filtration equipment row, and our crew on scheduled maintenance.

Melting, casting or smelting non-ferrous metal?

Hot, sticky, tar-laden furnace gas needs cooling, high-temperature filtration and wet electrostatic polishing — in the right order. Send us your furnace data for a written proposal within 24 hours.

Discuss Your Project