Ion-Exchanged Synthetic Phyllosilicate SCR Catalyst

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Solution Overview

Problem

Current SCR catalysts, particularly Cu-CHA zeolite catalysts, are expensive and have limitations in ammonia retention at high exhaust temperatures, leading to environmental and health concerns due to ammonia desorption, and there is a need for a cost-effective alternative that can efficiently reduce NOx emissions.

Innovation Solution

Ion-exchanged synthetic phyllosilicates, such as those synthesized via hydrothermal methods and pillared with metal cations like Cu and Fe, are used as catalysts to facilitate the reaction between ammonia and NOx gases, providing a cost-effective and efficient alternative to traditional zeolite-based SCR systems.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If Cu-CHA zeolite catalysts are used for SCR, then NOx conversion efficiency is improved, but system cost increases significantly

Engineering Contradiction:
ImproveNOx conversion efficiencyVSAvoidsystem cost
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent replaces expensive Cu-CHA zeolite catalysts with a less expensive Cu-exchanged natural mica catalyst. While natural mica has lower inherent catalytic activity, the patent compensates through optimized ion exchange processes and catalyst formulation, achieving acceptable NOx conversion at reduced cost.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent modifies the catalyst composition by controlling copper ion exchange levels and incorporating promoters to enhance the activity of the cheaper natural mica substrate, thereby improving NOx conversion efficiency without relying on expensive zeolite structures.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If SCR catalyst retains ammonia during low temperature cycles, then NOx conversion is improved, but ammonia desorbs at high temperatures causing environmental concerns

Engineering Contradiction:
ImproveNOx conversion rateVSAvoidammonia desorption
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent incorporates an AMOx catalyst upstream of the SCR catalyst to oxidize excess ammonia into nitrogen and water vapor before it reaches the SCR catalyst. This converts the harmful effect of ammonia overdose into a beneficial outcome, preventing ammonia slip while maintaining high NOx conversion efficiency.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The AMOx catalyst acts as an intermediary component that processes excess ammonia before it can cause environmental harm. By placing this intermediate treatment stage in the exhaust stream, the system manages ammonia retention and release dynamics effectively.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If ammonia is overdosed to increase NOx conversion rates, then SCR performance is improved, but risk of ammonia exiting exhaust system increases

Engineering Contradiction:
ImproveNOx conversion rateVSAvoidammonia slip
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The AMOx catalyst converts excess ammonia (which would otherwise be harmful) into harmless nitrogen and water vapor through oxidation. This allows the system to use higher ammonia dosing rates to maximize NOx conversion while the AMOx catalyst prevents ammonia slip by destroying the excess ammonia.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The use of ion-exchanged synthetic phyllosilicates effectively reduces NOx emissions by stabilizing metal cations, enhancing surface area, and maintaining ammonia retention, thus addressing the limitations of traditional SCR systems while reducing costs.

Implementation Method 1

exchanging a cation present in the synthesized phyllosilicate with one or more metal cations (e.g., including, but not limited to, cations of one or more metals selected from the group consisting of Cu, Fe, Co, Ni, La, Ce, Mn, V, Ag, Ti, and Zr), forming an ion-exchanged, synthesized phyllosilicate

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

Ion-exchanged synthetic phyllosilicates, such as those synthesized via hydrothermal methods and pillared with metal cations like Cu and Fe, are used as catalysts to facilitate the reaction between ammonia and NOx gases

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

Normally, the SCR catalyst can retain the ammonia during low temperature cycles. However, an increase in exhaust temperature can cause ammonia to desorb from the SCR catalyst and exit the exhaust system to the atmosphere

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS10792616B2Ion exchanged synthetic phyllosilicate as SCR catalyst
Publication Date: 2020.10.06 BASF MOBILE EMISSIONS CATALYSTS LLC
  • US10792616B2 patent drawing
  • US10792616B2 patent drawing
  • US10792616B2 patent drawing

AI summary

The present disclosure is directed to SCR catalysts, methods for their manufacture, and methods of treating emissions in an exhaust stream with them. The SCR catalysts are produced from pillaring and ion exchanging synthetic phyllosilicates, particularly hydrothermally synthesized phyllosilicates.