Editorial Technical Reference

Catalyst Gauze Pack

This page explains how Catalyst Gauze Pack 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 structured assembly of catalyst-coated gauze layers used to facilitate the oxidation of ammonia to nitric oxide in industrial reactors.

Representative product image. Confirm appearance and specifications with the manufacturer.

Product Specifications

Technical details and manufacturing context for Catalyst Gauze Pack

Definition
The Catalyst Gauze Pack is a critical component within an Ammonia Oxidation Reactor, consisting of multiple layers of platinum-rhodium alloy gauze arranged in a specific configuration. It serves as the catalytic surface where ammonia and air mixtures undergo controlled oxidation at high temperatures (typically 800-950°C) to produce nitric oxide, which is the primary intermediate in nitric acid production. The pack's design ensures optimal gas flow distribution, temperature management, and catalytic efficiency throughout the reaction zone. The gauze pack is typically circular, with a diameter matching the reactor internal diameter (1000–3000 mm). The thickness of the pack ranges from 5 to 20 mm, and the number of layers can vary from 10 to 60, depending on the desired conversion efficiency and pressure drop. The wire diameter is 0.06–0.12 mm, and the mesh count is 60–100 mesh, with higher mesh providing increased surface area. Catalyst loading is 20–50 g/m², affecting activity and lifetime. The operating temperature is 800–950°C; below 800°C conversion drops, and above 950°C the gauze degrades. Operating pressure is 1.0–1.6 MPa, and pressure drop across the pack is 5–15 kPa. Ammonia conversion rate is typically 95–98%. The gauze material is Pt-10Rh alloy (ASTM B616), and the total weight ranges from 5 to 20 kg, depending on diameter and layer count. The pack includes support grid/frame and edge reinforcement for mechanical integrity. These values are directory reference ranges and must be confirmed for the specific model and application with the legal manufacturer or supplier.
Working Principle
Ammonia-air mixture flows through the multiple layers of catalyst-coated gauze at high temperature and pressure. The platinum-rhodium alloy catalyzes the oxidation reaction: 4NH₃ + 5O₂ → 4NO + 6H₂O. The gauze structure provides high surface area for catalytic activity while allowing efficient gas passage and heat transfer. The layered configuration ensures complete ammonia conversion and minimizes pressure drop across the reactor.
Common Materials
Platinum-Rhodium Alloy Gauze, Support Grid/Frame, Edge Reinforcement
Technical Parameters
ParameterTypical rangeNotes & selection driver
Gauze Diameter1000–3000 mmMatches reactor internal diameter
Gauze Thickness5–20 mmAffects pressure drop and catalyst loading
Number of Layers10–60 layersDetermines conversion efficiency
Wire Diameter0.06–0.12 mmInfluences surface area and mechanical strength
Mesh Count60–100 meshHigher mesh increases surface area
Catalyst Loading20–50 g/m²Affects activity and lifetime
Operating Temperature800–950 °CBelow 800°C conversion drops; above 950°C gauze degrades
Pressure Drop5–15 kPaHigher layers increase pressure drop
Ammonia Conversion Rate95–98 %Typical for industrial operation
Gauze MaterialPt-10Rh alloyPlatinum-rhodium alloy for high temperature oxidationASTM B616
Weight5–20 kgDepends on diameter and layer count

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
  • Catalyst Gauze Layers Part
    Provide catalytic surface for ammonia oxidation reaction
    Material: Platinum-Rhodium Alloy
  • Support Grid/Frame Part
    Maintain structural integrity and proper spacing of gauze layers
    Material: High-Temperature Alloy Steel
  • Edge Reinforcement Part
    Prevent edge unraveling and maintain pack shape under thermal cycling
    Material: Nickel Alloy
  • Spacer Rings Part
    Maintain uniform spacing between gauze layers for optimal gas flow
    Material: Ceramic or High-Temperature Alloy

Applied To / Applications

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

Industrial Ecosystem & Supply Chain Structure

Complementary Systems
Downstream Applications
Specialized Tooling

Application Fit & Sizing Matrix

Operational Limits
pressure: Up to 10 bar (maximum recommended operating pressure)
flow rate: 0.5-5.0 m/s superficial gas velocity (optimal range)
temperature: 750-950°C (typical operating range for ammonia oxidation)
ammonia concentration: 9-12% vol in air (standard feed composition)
Media Compatibility
✓ Ammonia-air mixtures ✓ Nitric oxide process gas ✓ High-temperature reactor environments
Unsuitable: Chlorine-containing atmospheres (causes catalyst poisoning)
Sizing Data Required
  • Required nitric acid production capacity (tons/day)
  • Reactor diameter and bed depth constraints
  • Desired catalyst lifetime/regeneration frequency

Reliability & Engineering Risk Analysis

Failure Mode & Root Cause
Gauze blinding/fouling
Cause: Accumulation of process contaminants (e.g., dust, scale, catalyst poisons) on the gauze surface, reducing active sites and flow area, often due to inadequate feed gas filtration or upstream corrosion.
Gauze disintegration/mechanical failure
Cause: Thermal cycling or overheating causing embrittlement and rupture, or physical damage from high-velocity gas flow/particle impingement, typically from process upsets or poor installation.
Maintenance Indicators
  • Significant pressure drop increase across the gauze pack (indicating fouling or blockage)
  • Visible discoloration, sagging, or holes in the gauze during inspection, or abnormal process outlet temperatures/analyses
Engineering Tips
  • Implement robust upstream filtration and gas purification to minimize contaminants, and monitor pressure drop trends to schedule cleaning before severe fouling occurs.
  • Ensure proper installation with even support and avoid thermal shocks by following controlled startup/shutdown procedures; use thermocouples to monitor gauze temperature profiles.

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
ASTM E8/E8M - Standard Test Methods for Tension Testing of Metallic Materials CE Marking - Directive 2014/68/EU for Pressure Equipment

Quoted from the published standard.

Manufacturing Precision
  • Wire Diameter: +/-0.005mm
  • Mesh Opening Size: +/-0.01mm
Quality Inspection
  • Visual Inspection for Uniformity and Defects
  • Chemical Composition Analysis via XRF or ICP-OES

Manufacturers of Catalyst Gauze Pack

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Frequently Asked Questions

What is the typical operating temperature range for a Catalyst Gauze Pack?

The typical operating temperature range is 800–950°C. Below 800°C, ammonia conversion efficiency drops, while above 950°C, the gauze material may degrade, reducing its service life.

How does the number of gauze layers affect performance?

The number of layers (10–60) directly influences conversion efficiency and pressure drop. More layers generally increase conversion but also increase pressure drop across the pack. The optimal number depends on the reactor design and process requirements.

What materials are used in the Catalyst Gauze Pack?

The primary material is a platinum-rhodium alloy (Pt-10Rh) gauze, as per ASTM B616. The pack also includes a support grid/frame and edge reinforcement for structural integrity.

What is the typical ammonia conversion rate?

The typical ammonia conversion rate is 95–98% under normal operating conditions. Actual performance may vary based on operating parameters, gauze condition, and reactor design.

Data Basis

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

Preliminary Technical Classification
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