Editorial Technical Reference

Demister/Mist Eliminator

This page explains how Demister/Mist Eliminator is classified within Chemical Manufacturing. Technical values and manufacturer relationships are research references; confirm the current specification and supplier evidence for each order.

Technical Definition & Core Assembly

A device used to remove liquid droplets or mist from gas streams in industrial processes.

Demister/Mist Eliminator in a manufacturing environment
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Product Specifications

Technical details and manufacturing context for Demister/Mist Eliminator

Definition
A demister, also known as a mist eliminator, is a component used in gas cleaning systems to separate entrained liquid droplets from gas streams. It operates through impingement, centrifugal force, or filtration mechanisms, ensuring that the gas output is clean and preventing downstream equipment from damage caused by liquid carryover. This product is typically installed in vessels such as scrubbers, knock-out drums, or evaporators, where it captures droplets that would otherwise contaminate the gas or corrode piping and compressors. The demister is available in various configurations, including mesh pads, vane packs, and cyclonic separators, each suited to specific process conditions. The choice of material—stainless steel, polypropylene, or fiberglass—depends on the chemical compatibility and temperature requirements of the application. Key parameters to consider when selecting a demister include operating pressure, temperature, gas flow rate, removal efficiency, pressure drop, mist load, vessel diameter, material grade, and weight. For instance, the operating pressure range is 1.0–1.6 MPa, with a note that The operating temperature range is -40 to 120°C, above which material degradation may occur. Gas flow rates can vary from 1000 to 50000 m³/h, with higher flows requiring larger vessels. Removal efficiency is typically 99–99.9% for droplets larger than 5 μm. Pressure drop is low, between 0.1 and 0.5 kPa, but higher drops reduce efficiency. Mist load should be kept between 0.1 and 10 g/m³, as exceeding 10 g/m³ may cause flooding. Vessel diameter ranges from 300 to 3000 mm, with custom sizes available. Material grades include SS304 and SS316L, conforming to ASTM A240, for corrosion resistance. Weight ranges from 50 to 500 kg, depending on size and material. These values are reference ranges and must be verified for the specific model and application with the legal manufacturer or supplier. The demister is a critical component in chemical manufacturing, ensuring process reliability and product quality.
Working Principle
The demister operates by forcing gas streams containing liquid droplets through a mesh pad, vane pack, or cyclonic separator. As the gas flows through, droplets collide with the surfaces, coalesce into larger droplets, and then drain away by gravity. The clean gas passes through and exits the vessel. The mechanism relies on inertial impaction, where droplets, due to their higher density, deviate from the gas streamlines and impact the collecting surfaces. The efficiency of droplet removal depends on factors such as droplet size, gas velocity, and the geometry of the demister. For fine droplets, a mesh pad with high surface area is effective, while for larger droplets, vane packs or cyclones may be used. The pressure drop across the demister is minimal, ensuring energy efficiency. Proper design and selection are essential to achieve the desired removal efficiency without causing flooding or excessive pressure loss.
Common Materials
Stainless Steel, Polypropylene, Fiberglass
Technical Parameters
ParameterTypical rangeNotes & selection driver
Operating Pressure1.0–1.6 MPa
Operating Temperature-40–120 °CAbove 120°C material degradation may occur
Gas Flow Rate1000–50000 m³/hHigher flow requires larger vessel
Removal Efficiency99–99.9 %For droplets >5 μm
Pressure Drop0.1–0.5 kPaHigher drop reduces efficiency
Mist Load0.1–10 g/m³Above 10 g/m³ may cause flooding
Vessel Diameter300–3000 mmCustom sizes available
Material GradeSS304/SS316LCorrosion resistanceASTM A240
Weight50–500 kgDepends on size and material

Ranges are indicative industry figures for RFQ preparation, not a supplier commitment. Confirm every value and standard with the legal manufacturer before ordering.

Components / BOM
  • Mesh Pad Part
    Primary separation surface where droplets coalesce
    Material: stainless steel
  • Support Grid Part
    Structural framework holding mesh pads in place
    Material: carbon steel
  • Drainage System
    Channels collected liquid away from gas stream
    Material: stainless steel
  • Vane Pack Optional
    Separates larger droplets by zig-zag impaction instead of by mesh, on vane-type units.

Application & selection

Application Fit & Sizing Matrix

Operational Limits
pressure: Up to 100 bar (standard), higher with reinforced designs
flow rate: 0.5 to 50 m/s gas velocity (optimal range)
temperature: -40°C to 400°C (typical), up to 600°C with special materials
slurry concentration: Up to 10% solids by weight (standard), higher with specialized designs
Media Compatibility
✓ Natural gas processing (amine contactors) ✓ Chemical reactor off-gas streams ✓ Compressed air systems
Unsuitable: High-viscosity liquid entrainment (>500 cP)
Sizing Data Required
  • Gas flow rate (actual m³/h)
  • Droplet size distribution (microns)
  • Required separation efficiency (%)

Risk, maintenance & compliance

Reliability & Engineering Risk Analysis

Failure Mode & Root Cause
Plugging/Fouling
Cause: Accumulation of solids, polymers, or viscous materials in the mesh or vanes, often due to inadequate upstream filtration, process upsets, or chemical reactions within the mist stream.
Structural Damage/Blowout
Cause: Mechanical failure of the mesh, pads, or support structure due to excessive pressure drop (ΔP), liquid overloading, corrosion, or fatigue from cyclic operation or vibration.
Maintenance Indicators
  • Sustained high differential pressure (ΔP) across the demister, exceeding design limits.
  • Visible liquid carryover or excessive mist in the outlet stream, indicating reduced separation efficiency.
Engineering Tips
  • Implement regular monitoring of differential pressure (ΔP) and trend analysis to detect fouling early and schedule cleaning before efficiency drops critically.
  • Specify and install appropriate upstream devices (e.g., inlet baffles, pre-filters) to remove large droplets and particulates, reducing the load on the demister and minimizing plugging and erosion.

Indicative industry ranges for design and RFQ preparation. Confirm the exact figures and applicable standard with the manufacturer before specifying.

Compliance & Manufacturing Standards

Applicable Standards
ISO 14644-1:2015 (Cleanrooms and associated controlled environments) ANSI/ASME B31.3 (Process Piping) DIN EN 13445-3 (Unfired pressure vessels - Part 3: Design)

Quoted from the published standard.

Manufacturing Precision
  • Mesh wire diameter: +/-0.01mm
  • Support grid flatness: 0.5mm per meter
Quality Inspection
  • Pressure drop test (air/water flow)
  • Material composition verification (PMI - Positive Material Identification)
Technical documentation
Request current drawings, revision history, and a signed specification sheet.
Manufacturing capability
Verify equipment lists, process limits, capacity, and representative production evidence.
Inspection readiness
Confirm test methods, calibrated equipment, sampling plans, and traceable reports.
Supplier transparency
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Manufacturers of Demister/Mist Eliminator

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Frequently Asked Questions

What is the typical removal efficiency of a demister?

The removal efficiency is typically 99–99.9% for droplets larger than 5 μm. However, the actual efficiency depends on the specific design, operating conditions, and droplet size distribution. Always verify the efficiency for your application with the manufacturer.

What materials are available for demisters?

Common materials include stainless steel (SS304, SS316L), polypropylene, and fiberglass. The choice depends on chemical compatibility, temperature, and corrosion resistance requirements. Material grades conform to standards like ASTM A240 for stainless steel.

How does operating pressure affect demister performance?

The operating pressure range is 1.0–1.6 MPa. It is important to ensure the demister is designed for the actual pressure conditions in your system.

What maintenance signals indicate a demister needs attention?

Signs of fouling or blockage include increased pressure drop, reduced gas flow, or decreased removal efficiency. Regular inspection and cleaning may be required, especially if the mist load exceeds 10 g/m³, which can cause flooding. Always follow the manufacturer's maintenance guidelines.

Related equipment

Applied To / Applications

This component is essential for the following industrial systems and equipment:

Data Basis

Editorial classification, named public sources where available, and source-reviewed manufacturer records.

Preliminary Technical Classification
This page supports structured research, RFQ preparation, and supplier evaluation. It does not replace buyer-led supplier qualification, standards review, or technical approval.

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