Hydrotreating Catalyst Activation via Acid-Organic Additive Treatment

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Solution Overview

Problem

Current hydrotreating catalyst activation processes are insufficient in achieving high activity levels, especially in fresh calcined catalysts with significant crystalline fractions, and do not effectively maintain additive presence during the activation process.

Innovation Solution

A process involving the use of an acid and an organic additive with specific boiling and solubility properties is applied to hydrotreating catalysts, incorporating the additive through impregnation and aging steps to reduce the crystalline fraction and enhance catalyst activity, suitable for both fresh and used catalysts.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional activation processes are used on fresh calcined catalysts, then the catalyst can be activated, but the significant crystalline fraction results in insufficient activity levels

Engineering Contradiction:
Improvecatalyst activityVSAvoidcrystalline fraction
Core Design Contradiction:
ReliabilityVSStability of the object's composition

Solution Approach 1:

The invention changes the chemical environment parameters by introducing specific organic additives (carboxylic acids, phenols, or their salts) during activation. These additives interact with the crystalline metal oxides on the catalyst surface, dissolving or transforming them into more active amorphous forms. The controlled chemical parameters (additive concentration, pH, temperature) enable conversion of the stable but inactive crystalline phase into an active form without compromising catalyst structure.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Organic additives serve as intermediaries between the crystalline metal oxide phase and the desired active catalyst state. These additives (carboxylic acids, phenols, or their salts) act as chelating agents that bind to metal ions in the crystalline structure, facilitating their transformation into active dispersed phases. The intermediary compounds enable the transition from stable crystalline form to active amorphous form by providing a chemical pathway for transformation.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If drying conditions are applied to remove solvent, then the catalyst can be processed, but the additive may be lost reducing catalyst performance

Engineering Contradiction:
Improvecatalyst activityVSAvoidadditive retention
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The invention optimizes drying parameters (temperature, time, atmosphere) to remove solvent while preserving the thermally sensitive organic additives. By controlling the drying temperature to remain below the decomposition temperature of the additives and using gentle removal conditions, the process achieves solvent elimination without significant additive loss, maintaining catalyst activity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The catalyst structure is prepared in advance to accommodate and retain the organic additives. The porous support structure and metal oxide phases are pre-treated to create binding sites that anchor the additives before drying. This preliminary structuring ensures that during subsequent drying and processing steps, the additives remain retained in the catalyst pores rather than being washed or evaporated away.

Inventive Principle:
Principle #10Preliminary action

3Duration of action of stationary object

If used catalysts are regenerated, then they can be reused, but their activity decreases compared to fresh catalysts

Engineering Contradiction:
Improvecatalyst lifespanVSAvoidcatalyst activity
Core Design Contradiction:
Duration of action of stationary objectVSReliability

Solution Approach 1:

The invention recovers activity in regenerated catalysts by applying the organic additive treatment specifically tailored to restore the active phase. Used catalysts that have lost activity due to crystallization or deactivation are treated with carboxylic acids, phenols, or their salts during activation, which re-dissolve crystalline phases and regenerate the active amorphous metal oxide phases, recovering near-fresh catalyst performance and extending catalyst lifespan.

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The invention converts the harmful effect of crystallization (which causes deactivation) into a beneficial recovery process. The same crystalline phases that cause deactivation during use become the target for recovery treatment. By applying organic additives during regeneration, the crystalline deposits are chemically transformed back into active phases, turning the deactivation mechanism into a recoverable state and extending catalyst life.

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

This process significantly improves catalyst activity by maintaining at least 50% of the additive within the catalyst, achieving comparable performance to fresh catalysts and extending the lifespan of used catalysts, while reducing energy consumption and increasing cycle length.

Implementation Method 1

incorporating the additive through impregnation and aging steps

Methodology Applied
Scientific EffectImpregnation: Absorption (physical)

Implementation Method 2

drying under such conditions that at least 50 wt % of the additive (relative to the total original amount of additive) is maintained in the catalyst

Methodology Applied
Scientific EffectDrying: Evaporation

Data Source

PatentUS7956000B2Process for activating a hydrotreating catalyst
Publication Date: 2011.06.07 NIPPON KETJEN CO LTD

AI summary

The invention pertains to a process for activating an hydrotreating catalyst comprising a Group VIB metal oxide and a Group VIII metal oxide which process comprises contacting the catalyst with an acid and an organic additive which has a boiling point in the range of 80-500° C. and a solubility in water of at least 5 grams per liter (20° C., atmospheric pressure), optionally followed by drying under such conditions that at least 50% of the additive is maintained in the catalyst. The hydrotreating catalyst may be a fresh hydrotreating catalyst or a used hydrotreating catalyst which has been regenerated.