Zn/Al Catalyst Pore Volume Retention

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Solution Overview

Problem

Existing water gas shift catalysts face challenges during startup under steam condensing conditions, leading to leaching of alkali metal compounds and loss of catalytic activity, and require dedicated guard materials to mitigate halogen poisoning, limiting their mechanical strength and number of start-ups.

Innovation Solution

A Zn/Al-based catalyst with a mixture of zinc aluminum spinel and alkali metals like potassium, having a specific pore volume and density, allowing retention of alkali metal compounds within the catalyst pores and maintaining mechanical strength, thus preventing significant loss of activity during steam condensation and halogen exposure.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If steam is used to heat the HTS reactor during startup, then heating efficiency is improved and dedicated nitrogen loops are eliminated, but alkali metal compounds are leached from the catalyst causing loss of catalytic activity

Engineering Contradiction:
Improveheating efficiencyVSAvoidalkali metal compounds
Core Design Contradiction:
Use of energy by moving objectVSLoss of substance

Solution Approach 1:

The catalyst employs a porous support structure with controlled pore size distribution that physically confines alkali metal compounds within the pores. The pore dimensions are specifically designed to retain the alkali metals during steam condensation while still allowing reactant and product molecules to diffuse freely, thus preventing leaching during steam heating startup

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The catalyst uses a composite structure combining metal oxide active phases with a porous support material. This composite design provides both the catalytic functionality and the structural framework that retains alkali metal promoters during steam exposure, resolving the contradiction between steam heating efficiency and alkali metal retention

Inventive Principle:
Principle #40Composite materials

2Reliability

If guard materials are added to mitigate halogen poisoning, then catalyst protection is improved, but device complexity and pressure drop increase

Engineering Contradiction:
Improvecatalyst protectionVSAvoidreactor structure
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The invention extracts and eliminates the need for separate guard materials by incorporating halogen resistance directly into the main catalyst formulation. The catalyst composition includes components specifically designed to withstand halogen exposure, thereby removing the requirement for additional protective beds or guard materials

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The catalyst is designed with multi-functionality, simultaneously providing water-gas shift activity, halogen resistance, and alkali metal retention. This universal design consolidates multiple functions into a single catalyst material, eliminating the need for separate guard materials and reducing reactor complexity

Inventive Principle:
Principle #6Universality (Multi-functionality)

3Productivity

If the number of start-ups is increased, then catalyst utilization is improved, but mechanical strength degradation and activity loss occur

Engineering Contradiction:
Improvecatalyst utilizationVSAvoidmechanical strength
Core Design Contradiction:
ProductivityVSStrength

Solution Approach 1:

The catalyst undergoes preliminary stabilization treatment during manufacturing that strengthens its mechanical structure before service. This pre-treatment creates a more robust catalyst formulation that can withstand repeated thermal cycling and mechanical stress from multiple start-ups without significant strength degradation or activity loss

Inventive Principle:
Principle #10Preliminary action

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 catalyst maintains high mechanical strength and catalytic activity through the alkali-buffer effect, enabling over 100 start-ups without substantial activity loss, eliminating the need for dedicated nitrogen loops and reducing halogen poisoning, while being environmentally friendly by avoiding chromium and iron.

Implementation Method 1

allowing retention of alkali metal compounds within the catalyst pores

Methodology Applied
Scientific EffectPhysical containment in pores: Physical Containment

Implementation Method 2

heating up the reactor and the HTS catalyst inside it... While the reactor temperature is below the dew point of water, condensation will take place inside the reactor

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

heats up the reactor and the HTS catalyst inside it

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 4

Water gas shift is a well-known method for increasing the hydrogen content of a synthesis gas... Water gas shift enables increasing the hydrogen yield and decreasing the carbon monoxide content of the synthesis gas according to the equilibrium reaction: CO+H2O═CO2+H2

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20240001341A1Improved water gas shift catalyst
Publication Date: 2024.01.04 HALDOR TOPSOE AS
  • US20240001341A1 patent drawing
  • US20240001341A1 patent drawing
  • US20240001341A1 patent drawing

AI summary

The present disclosure relates to an improved water gas shift catalyst, in particular an improved high temperature shift catalyst and process using the catalyst. The water gas shift catalyst includes Zn, Al, optionally Cu, and an alkali metal or alkali metal compound, wherein the content of alkali metal, preferably K, is in the range 1-6 wt %, such as 1-5 wt % or 2.5-5 wt % based on the weight of oxidized catalyst, and wherein the water gas shift catalyst has a pore volume, as determined by mercury intrusion, of 240 ml/kg or higher, such as 250 ml/kg or higher. A process for enriching a synthesis gas in hydrogen by contacting the synthesis gas in a water gas shift reactor with the water gas shift catalyst.