White Oil Catalytic Hydrogenation Yield Optimization

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Solution Overview

Problem

Existing processes for producing white oils result in by-products such as cracking products, leading to reduced yields and increased costs, particularly due to the involvement of high sulfur amounts.

Innovation Solution

A process involving catalytic hydrogenation of a base oil feedstock at specific temperature, pressure, and liquid hourly space velocity conditions, with a sulfur content of less than 5 ppm, to produce white oils with an initial boiling point of at least 250°C and reduced aromatic content.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional hydrofining processes are used to produce white oils, then the aromatic content is reduced, but cracking by-products are formed leading to reduced yield

Engineering Contradiction:
Improvearomatic contentVSAvoidyield
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The invention changes the operating parameters of the hydrogenation process, specifically using temperatures of 200-400°C and pressures of 30-160 bar with modified catalyst systems, to achieve aromatic removal without the cracking reactions that occur in conventional processes

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention introduces a specific catalyst system acting as an intermediary that facilitates selective hydrogenation of aromatic compounds while preventing cracking reactions. The catalyst enables the desired chemical transformation without causing unwanted side reactions

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If high sulfur amounts are involved in the process, then the refining capability is enhanced, but the cost increases and environmental impact worsens

Engineering Contradiction:
Improverefining capabilityVSAvoidcost
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The invention uses base oil feedstocks with low sulfur content (less than 5 ppm) that can be processed through a single hydrogenation step without requiring extensive pre-treatment or sulfur-tolerant catalysts, thereby reducing overall process cost and complexity

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

Solution Approach 2:

The invention modifies the feedstock specification parameter (sulfur content < 5 ppm) and adjusts process parameters (temperature, pressure, catalyst type) to achieve effective refining without requiring high sulfur inputs, thus reducing cost and environmental burden

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 process achieves higher yields and reduced costs by minimizing by-product formation, specifically cracking products, while maintaining the purity and stability requirements of white oils, as defined by pharmacopeial standards.

Implementation Method 1

a step of catalytically hydrogenating a base oil feedstock

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

a step of catalytically hydrogenating a base oil feedstock

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Data Source

PatentUS12269999B2Process for the production of white oils
Publication Date: 2025.04.08 TOTALENERGIES ONETECH
  • US12269999B2 patent drawing
  • US12269999B2 patent drawing

AI summary

The invention is a process for producing a white oil having an initial boiling point of at least 250° C., the process comprising a step of catalytically hydrogenating a base oil feedstock at a temperature of from 120 to 210° C., at a pressure of from 30 to 160 bars and a liquid hourly space velocity of 0.2 to 5 hr−1, the base oil feedstock comprising less than 5 ppm by weight of sulphur.