Selective FCC Gasoline Hydrodesulfurization Catalyst

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Solution Overview

Problem

Current hydrotreatment processes for gasoline desulfurization face challenges in maintaining low sulfur content while minimizing the hydrogenation of olefins, leading to a significant drop in octane number due to non-selective catalysts.

Innovation Solution

A hydrotreatment catalyst comprising metals from group VIB and group VIII, supported on an alumina with a high gamma alumina content and specific surface area, optimized through heat treatment and impregnation processes to enhance selectivity and activity in hydrodesulfurization without severe reduction in octane number.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional hydrotreatment catalysts are used to achieve deep hydrodesulfurization, then sulfur content is reduced, but octane number drops significantly due to non-selective olefin hydrogenation

Engineering Contradiction:
Improvesulfur content reductionVSAvoidoctane number
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent changes the physical and chemical parameters of the alumina support, specifically controlling the gamma alumina content (60-95 wt%) and specific surface area (60-100 m2/g), to optimize the catalyst's selectivity. This allows deep hydrodesulfurization while preserving olefins and maintaining high octane numbers

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates a composite catalyst system combining Group VIB metals (Mo, W) with Group VIII metals (Co, Ni) on a specially formulated alumina support. This composite structure synergistically enhances both hydrodesulfurization activity and selectivity, resolving the contradiction between sulfur removal and octane preservation

Inventive Principle:
Principle #40Composite materials

2Reliability

If catalyst selectivity is increased to preserve olefins and maintain octane number, then hydrodesulfurization activity may be reduced

Engineering Contradiction:
Improveoctane numberVSAvoidhydrodesulfurization rate
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent optimizes metal loading parameters (Group VIB: 3-35 wt%, Group VIII: 0.1-10 wt%) and support properties (gamma alumina content, specific surface area) to achieve a balance where the catalyst maintains high hydrodesulfurization activity while being selective enough to preserve olefins and maintain octane number

Inventive Principle:
Principle #35Parameter changes

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 achieves deep hydrodesulfurization with improved selectivity, maintaining high octane numbers by effectively reducing sulfur content while limiting olefin hydrogenation, thus producing gasoline that meets stringent sulfur specifications.

Implementation Method 1

heat treatment of an alumina precursor so as to obtain a support having a gamma alumina content of between 60% and 95% wt.

Methodology Applied
Scientific EffectPhase transformation: Phase Change

Implementation Method 2

at least one component of a metal of group VIB, at least one component of a metal of group VIII, and optionally phosphorus are brought into contact with said support

Methodology Applied
Scientific EffectImpregnation: Adsorption

Implementation Method 3

A hydrotreatment catalyst comprising at least one metal from group VIB, at least one metal from group VIII and an alumina support

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP3498370B1Catalyst for selective fcc gasoline hydrodesulphurisation
Publication Date: 2021.08.04 IFP ENERGIES NOUVELLES
  • EP3498370B1 patent drawingFigure 1~2
  • EP3498370B1 patent drawing
  • EP3498370B1 patent drawing

AI summary

The present invention relates to a hydrotreating catalyst comprising at least one metal from group VIB, at least one metal from group VIII and an alumina support having a gamma alumina content greater than 50% by weight and less than 100% by weight relative to the weight of the support, said support having a specific surface area between 25 and 150 m2/g.