Editorial Technical Reference

Selective Catalytic Reduction (SCR) Catalyst

This page explains how Selective Catalytic Reduction (SCR) Catalyst is classified within Motor Vehicle Manufacturing. Technical values and manufacturer relationships are research references; confirm the current specification and supplier evidence for each order.

Technical Definition & Core Assembly

A catalytic component that converts nitrogen oxides (NOx) into nitrogen and water using a reductant like ammonia or urea.

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Product Specifications

Technical details and manufacturing context for Selective Catalytic Reduction (SCR) Catalyst

Definition
The Selective Catalytic Reduction (SCR) Catalyst is a component used in the exhaust aftertreatment systems of diesel and lean-burn engines. Its primary function is to reduce nitrogen oxides (NOx) in exhaust gas to harmless nitrogen (N₂) and water (H₂O) through a chemical reaction with a reductant, typically ammonia derived from a urea solution (AdBlue/DEF). This process is essential for meeting stringent emissions regulations. The catalyst is typically a honeycomb or substrate structure coated with active materials such as vanadium pentoxide (V₂O₅) on a titanium dioxide (TiO₂) substrate, or copper-zeolite or iron-zeolite formulations. During operation, a urea-water solution is injected into the exhaust stream upstream of the catalyst. The solution decomposes into ammonia (NH₃), which then reacts with NOx on the catalyst's active sites, selectively reducing it to nitrogen and water vapor. The catalyst operates effectively within a temperature range of 250–450°C; below 250°C, conversion efficiency drops, and above 450°C, the catalyst may sinter. Space velocity typically ranges from 10,000 to 60,000 h⁻¹, with higher values reducing NOx conversion. At optimal conditions, NOx conversion efficiency can reach 90–98%. The NH₃/NOx ratio should be maintained between 0.8 and 1.2, with a stoichiometric ratio of 1.0; higher ratios may cause ammonia slip. The catalyst is available in various sizes, with diameters typically 150–300 mm and lengths 300–600 mm, and can be customized. Cell density ranges from 200 to 400 cpsi, and wall thickness from 0.15 to 0.30 mm. Pressure drop is typically 1–5 kPa at rated flow, and excessive pressure drop can affect engine performance. The catalyst has a sulfur tolerance of ≤50 ppm, as higher sulfur levels deactivate the catalyst. Mechanical strength is ≥1.5 MPa, and weight ranges from 5 to 20 kg depending on size and substrate material. For specific applications, verify model-specific values and standards with the legal manufacturer or supplier.
Working Principle
Exhaust gas containing NOx passes over the catalyst surface. A urea-water solution is injected upstream, decomposing into ammonia (NH₃). On the catalyst's active sites, ammonia reacts with NOx in a selective catalytic reduction reaction, forming nitrogen and water vapor. Common catalyst formulations include vanadium-based or zeolite-based materials.
Common Materials
Vanadium Pentoxide (V₂O₅) on Titanium Dioxide (TiO₂) substrate, Copper-Zeolite or Iron-Zeolite
Technical Parameters
ParameterTypical rangeNotes & selection driver
Operating Temperature250–450 °CBelow 250°C, conversion efficiency drops; above 450°C, catalyst may sinter.
Space Velocity10000–60000 h⁻¹Higher space velocity reduces NOx conversion.
NOx Conversion Efficiency90–98 %At optimal temperature and NH3/NOx ratio.
NH3/NOx Ratio0.8–1.2Stoichiometric ratio is 1.0; higher ratio may cause NH3 slip.
Dimensions (Diameter)150–300 mmCustom sizes available.
Dimensions (Length)300–600 mmCustom sizes available.
Cell Density200–400 cpsiHigher cell density increases surface area but may increase pressure drop.
Wall Thickness0.15–0.30 mmThinner walls reduce pressure drop.
Pressure Drop1–5 kPaAt rated flow; excessive pressure drop affects engine performance.
Sulfur Tolerance≤50 ppmHigher sulfur deactivates catalyst.
Mechanical Strength≥1.5 MPaResistance to crushing and vibration.
Weight5–20 kgDepends on size and substrate 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
  • Catalyst Substrate
    Provides a high-surface-area ceramic or metallic honeycomb structure to support the active catalytic coating.
    Material: Cordierite ceramic or metallic alloy (e.g., FeCrAl)
  • Washcoat Part
    A porous layer applied to the substrate to increase surface area and anchor the active catalytic material.
    Material: Alumina (Al₂O₃), Titanium Dioxide (TiO₂)
  • Active Catalytic Material Part
    The chemical compound that catalyzes the SCR reaction between NOx and ammonia.
    Material: Vanadium Pentoxide (V₂O₅), Copper-Zeolite (Cu-Zeolite)
  • Catalyst Canning / Housing
    Metal shell that contains and protects the catalyst brick, ensuring proper gas flow and mechanical integrity.
    Material: Stainless steel

Industry Taxonomies & Aliases

Commonly used trade names and technical identifiers for Selective Catalytic Reduction (SCR) Catalyst.

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 (typical 1-5 bar)
flow rate: 0.5-50 m/s gas velocity
temperature: 250-450°C (optimal 300-400°C)
space velocity: 5000-30000 h⁻¹ (typical 15000-25000 h⁻¹)
ammonia to nox ratio: 0.8-1.2 (optimal 1.0)
Media Compatibility
✓ Diesel exhaust gases ✓ Natural gas turbine exhaust ✓ Coal-fired boiler flue gas
Unsuitable: High sulfur content (>50 ppm) or halogen-containing environments
Sizing Data Required
  • NOx concentration at inlet (ppm)
  • Total exhaust gas flow rate (Nm³/h)
  • Required NOx removal efficiency (%)

Reliability & Engineering Risk Analysis

Failure Mode & Root Cause
Catalyst poisoning
Cause: Contamination from sulfur, phosphorus, or heavy metals in the flue gas, which adsorb onto active sites and reduce NOx conversion efficiency.
Thermal degradation
Cause: Exposure to temperatures above the catalyst's design limit, often due to improper burner operation or system malfunctions, leading to sintering and loss of surface area.
Maintenance Indicators
  • Visible ammonia slip (white plume) from the stack, indicating poor NOx conversion and potential catalyst deactivation.
  • Abnormally high pressure drop across the SCR reactor, suggesting catalyst blockage or physical damage.
Engineering Tips
  • Implement strict fuel quality control and upstream gas conditioning to minimize contaminants like sulfur and particulates before the SCR unit.
  • Install and maintain precise temperature monitoring and control systems to prevent thermal excursions and ensure optimal operating temperature windows.

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 D5758-01(2019) - Standard Guide for Characterization of Spent Selective Catalytic Reduction (SCR) Catalysts CE Marking - EU Directive 2007/46/EC (for vehicle emissions systems)

Quoted from the published standard.

Manufacturing Precision
  • Cell Density: +/- 5 cells/cm²
  • Wall Thickness: +/- 0.05 mm
Quality Inspection
  • X-ray Fluorescence (XRF) Analysis for active metal content
  • Pressure Drop Test for flow uniformity

Manufacturers of Selective Catalytic Reduction (SCR) Catalyst

Manufacturer profiles associated with Selective Catalytic Reduction (SCR) Catalyst.

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Frequently Asked Questions

What is the operating temperature range for this SCR catalyst?

The typical operating temperature range is 250–450°C. Below 250°C, conversion efficiency drops, and above 450°C, the catalyst may sinter. Always verify the exact range for your specific application with the manufacturer.

What reductant is used with this catalyst?

The reductant is typically ammonia derived from a urea solution (AdBlue/DEF). The solution is injected upstream of the catalyst and decomposes into ammonia, which reacts with NOx.

What is the expected NOx conversion efficiency?

At optimal temperature and NH3/NOx ratio, the NOx conversion efficiency is typically 90–98%. Actual efficiency depends on operating conditions and system design.

What are the common catalyst formulations?

Common formulations include vanadium pentoxide (V₂O₅) on a titanium dioxide (TiO₂) substrate, and copper-zeolite or iron-zeolite materials. The choice depends on the application and operating conditions.

Data Basis

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

Preliminary Technical Classification
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