127,000 m³/h Protective Coating & Chemical VOCs Abatement System

127,000 m³/h Protective Coating & Chemical VOCs Abatement System

Sanhe Industrial Group (HKEX: 3010) | Heavy-Duty Protective Paints, Aerosol Chemicals & Synthetic Resins

Executive Summary

Corrosion-Resistant Decoupled Oxidation for Complex Chemical & Coating Exhaust

Sanhe Fine Chemical Group Co., Ltd. (三和精化集团有限公司, HKEX: 3010 / 广东三和) is an internationally recognized publicly listed chemical manufacturer specializing in high-performance automotive aerosols, heavy-duty anti-corrosive coatings, synthetic architectural paints, and industrial adhesives. Manufacturing operations generate dual-stream exhausts totaling 127,000 m³/h (74,700 CFM) from reactor kettles, high-speed dispersion tanks, filling lines, and storage vents.

The production exhaust carried severe technological risks: the presence of dodecylbenzenesulfonic acid, an active surfactant that transforms into corrosive SO₂ and sulfurous acid upon thermal oxidation, threatening premature metal shell perforation and ceramic block degradation; additionally, siloxanes from antifoam agents risk irreversible silica (SiO₂) vitreous fouling on heat-recovery honeycombs.

FluxFine executed a comprehensive turnkey EPC retrofit: deploying an automated counter-flow alkali wet scrubber for sulfur neutralization, a 4-stage modular dry filtration box (G4/F7/F9 plus sacrificial carbon guard), a 100,000 m³/h Zeolite Rotor Concentrator (12.5:1 ratio), and a centralized 35,000 m³/h Three-Bed Regenerative Thermal Oxidizer (3-Bed RTO) treating the merged oven exhausts and desorption stream. The unit delivers guaranteed DRE of ≥98.5% (field operating performance ≥99.2%), completely protects the RTO from acidic corrosion, and achieves stack emissions of NMHC ≤ 30 mg/m³, outperforming national GB 37824-2019 standards.

Process Boundary

Four Engineering Dilemmas in Heavy-Duty Paint & Chemical Exhaust

Treating multi-product chemical coating exhaust demands neutralizing acidic corrosion precursors, avoiding silica blinding, and managing large airflow swings.

Challenge 01

Sulfuric Acid Corrosion

Formulations include dodecylbenzenesulfonic acid surfactants. Direct oxidation creates SO₂ that forms sulfurous acid condensate, causing rapid metal perforation on RTO chambers.

Alkali counter-flow wet neutralization
Challenge 02

Silica Fouling Threat

Silicon-based defoaming agents break down into vitreous silica (SiO₂) powder at 800°C+, glassifying ceramic honeycombs. Siloxane streams required strict segregation.

Source segregation of siloxane streams
Challenge 03

Massive 127,000 m³/h Flow

Ventilation combines 100,000 m³/h of dilute room air (200 mg/m³) with 27,000 m³/h of reactor vents (1,000 mg/m³). Sizing a single direct RTO would be cost-prohibitive.

12.5:1 concentration down to 35,000 m³/h RTO
Challenge 04

Surplus Enthalpy Venting

During heavy aerosol canning runs, solvent concentration surges create extreme heat release in the RTO. Automated high-temperature bypass dampers were required for over-temp relief.

850°C automated high-temp bypass damper
Process Evaluation

Comparative Audit: Scheme 1 (Legacy Patch) vs. Scheme 2 (Unified Turnkey Train)

FluxFine evaluated retaining deteriorated legacy units against engineering a unified 127,000 m³/h concentration and thermal oxidation train.

Engineering DimensionScheme 1: Legacy Retain & PatchScheme 2 (Adopted): Unified Turnkey TrainEngineering Rationale
Acid Corrosion ResistanceNo alkali tower; severe ongoing sulfur corrosion on RTO shellAlkali counter-flow spray scrubber neutralizing 100% of acid mistZero acid corrosion risk
RTO Thermal CoreAging, corroded legacy unit with dropping thermal efficiencyNew 35,000 m³/h Three-Bed RTO with structured cordierite media≥95% TER efficiency
Pre-filtration ArchitectureSimple filter mats prone to particulate bypass4-stage dry box (G4+F7+F9+Active Carbon sacrificial guard)>99% mist & high-boiler capture
Destruction Efficiency (DRE)Unstable 85.0% - 90.0% due to valve seal deterioration≥98.5% guaranteed (measured field performance ≥99.2%)≥99.2% verified DRE
Compliance AssuranceHigh risk of catastrophic failure during environmental auditContinuous stack NMHC ≤ 30 mg/m³ (GB 37824-2019 Table 2)100% compliance record
≥99.2%
Measured DRE

Complete high-temperature thermal destruction across 35,000 m³/h Three-Bed RTO.

≤30 mg/m³
Stack NMHC Emission

Strictly compliant with GB 37824-2019 Table 2 specialized chemical standards (≤ 50 mg/m³).

100%
Acid Mist Scrubbing

Alkali counter-flow scrubber prevents sulfurous acid corrosion on RTO ceramic beds.

12.5:1
Concentration Ratio

Compresses 100,000 m³/h dilute room air into 8,000 m³/h concentrated stream for RTO entry.

Engineering Innovations

Subsystem Architecture & Hardware Execution

Explore the four synchronized engineering subsystems delivering acid neutralization, aerosol interception, and high-efficiency regenerative thermal oxidation.

01

Complete Plant Layout & Unified RTO Architecture

Under the unified Scheme 2 layout, deteriorating legacy units were dismantled and replaced by a consolidated 127,000 m³/h treatment train.

100,000 m³/h of dilute workshop exhaust undergoes alkaline scrubbing and four-stage dry filtration before entering the 100,000 m³/h zeolite rotor. The 8,000 m³/h concentrated desorption stream merges with 27,000 m³/h of reactor kettle exhaust into the 35,000 m³/h Three-Bed RTO.

Parameters: 100,000 m³/h zeolite flow; 27,000 m³/h direct oven flow; 35,000 m³/h RTO capacity; 800°C–850°C combustion setpoint.

Authentic P&ID Process Flow and Equipment Layout for Sanhe 127,000 m³/h VOCs Treatment System
Figure 1: Authentic P&ID process flow and stream balancing schematic for the consolidated 127,000 m³/h treatment train.
Modular Four-Stage Dry Particulate Filtration Unit
Figure 2: Four-stage modular dry filtration unit with quick-release filter frames protecting downstream zeolite and RTO.
02

Counter-Flow Alkaline Scrubbing & Modular Pre-Filtration

To neutralize corrosive dodecylbenzenesulfonic acid surfactants before reaching high-temperature combustion, exhaust passes through a heavy-gauge PP counter-flow alkaline scrubber tower.

Circulating NaOH solution (pH 8.5–10.0) atomized through non-clogging spiral nozzles reacts with acid precursors, converting them into soluble neutral salts while knocking down water-soluble aerosols and condensables.

Parameters: Gas velocity 1.8–2.2 m/s; liquid-to-gas ratio 2.5 L/m³; droplet eliminator mist carryover <20 mg/m³; automatic pH dosing system.

03

Poppet Valve Actuation & Zero-Slip Purge Cycle

The Three-Bed RTO utilizes high-speed pneumatic poppet switching valves driven by heavy-duty SMC actuators with feedback positioners. The rapid ≤1.0s switching stroke minimizes flow perturbation.

Before switching a regenerative bed from inlet preheating to outlet heat recovery, a dedicated clean air purge sweeps raw solvent vapors back into the combustion chamber, completely eliminating transient switching bypass slips and ensuring ≥98.5% DRE.

Parameters: Valve leakage rate ≤0.05%; 120 N·m actuator torque; ≤1.0s cycle transition time; 1,000,000-cycle industrial endurance rating.

Heavy-Duty Pneumatic Poppet Switching Valve Mechanism for Three-Bed RTO
Figure 3: Heavy-duty disk poppet switching valve and pneumatic drive shaft inside the RTO manifold.
Engineering Specifications

System Operational & Thermodynamic Data Matrix

Verified operational thresholds, airflow capacities, and destruction metrics for the Sanhe Industrial Group facility.

SubsystemDesign SpecificationOperating MetricCompliance Standard
Three-Bed RTO Thermal Core35,000 m³/h three-chamber regenerative thermal oxidizer760°C - 850°C oxidation setpoint; ≥1.0s residence≥98.5% guaranteed DRE
Zeolite Rotor Concentrator100,000 m³/h continuous hydrophobic molecular sieve drum12.5:1 concentration ratio (100,000 to 8,000 m³/h)≥92.0% adsorption efficiency
Counter-Flow Alkali ScrubberPP vertical absorption tower with automated NaOH dosing100% sulfur precursor neutralizationZero acid corrosion on RTO
Four-Stage Dry Filtration UnitG4 panel + F7 pocket + F9 fine + sacrificial active carbon bedΔP ≤ 450 Pa clean resistanceHigh-boiler and aerosol interception
Thermal Energy Recovery (TER)Structured cordierite ceramic honeycomb media≥95% thermal recovery efficiencyAuto-thermal at ≥1,800 mg/m³
Stack Emissions (NMHC)Continuous flame ionization detector (FID) monitoredMeasured ≤ 30 mg/m³GB 37824-2019 Table 2 (≤ 50 mg/m³)
Turnkey Engineering Execution

Corrosion-Resistant VOC Abatement for Heavy-Duty Chemical & Paint Plants

FluxFine engineers robust turnkey air pollution control systems incorporating alkaline pre-scrubbing, high-capacity zeolite concentration, and heavy-duty regenerative thermal oxidizers.