Oxidative Desulfurization of Diesel Using Cage Catalyst

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Solution Overview

Problem

Current oxidative desulfurization processes for hydrocarbon mixtures, such as diesel oil, face limitations in selectivity and scalability due to the use of biphasic reaction systems, which hinder their effectiveness in large-scale commercial applications.

Innovation Solution

The process involves using a cage structure catalyst and a co-catalyst with an aqueous oxidizing agent to oxidize sulfur species in hydrocarbon mixtures, followed by solvent extraction and subsequent steps like solvent stripping and polishing to achieve high selectivity and efficiency in sulfur removal.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If biphasic reaction systems are used for oxidative desulfurization, then sulfur removal capability is achieved, but selectivity and scalability are limited

Engineering Contradiction:
Improvesulfur removal capabilityVSAvoidselectivity
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

A phase transfer catalyst is introduced as an intermediary substance to facilitate the reaction between the aqueous oxidizing agent and organosulfur compounds in the hydrocarbon phase. The phase transfer catalyst mediates mass transfer across the liquid-liquid interface, enabling selective oxidation of sulfur compounds while maintaining biphasic system advantages.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent modifies reaction parameters including oxidizing agent concentration, phase transfer catalyst dosage, temperature, and contact time to optimize both sulfur removal efficiency and selectivity. By carefully controlling these parameters, the process achieves high selectivity for sulfur compounds over hydrocarbon components.

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If biphasic reaction systems are used for oxidative desulfurization, then sulfur removal capability is achieved, but scalability to large-scale commercial applications is hindered

Engineering Contradiction:
Improvesulfur removal capabilityVSAvoidscalability
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The phase transfer catalyst serves as a scalable intermediary that facilitates rapid mass transfer and reaction kinetics. This mediator enables the process to be scaled from laboratory to commercial dimensions by maintaining efficient interfacial reaction rates throughout the larger reactor volume.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent optimizes reaction conditions including temperature, oxidizing agent dosage, and phase ratio to enable scalable operation. These parameter adjustments ensure that reaction efficiency and sulfur removal capability are maintained across different scales of operation.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If oxidized sulfur compounds are removed by solvent extraction, then sulfur content is reduced to below 10 ppm, but process complexity increases

Engineering Contradiction:
Improvesulfur content reductionVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent employs liquid-liquid extraction to separate oxidized sulfur compounds from the hydrocarbon phase. A selective solvent extracts the polar oxidized sulfur species (sulfones, sulfoxides) from the non-polar hydrocarbon phase, achieving sulfur content reduction to below 10 ppm through selective phase separation.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The process utilizes phase separation between immiscible liquid phases to remove sulfur compounds. The oxidized sulfur compounds preferentially partition into the aqueous or solvent phase, which is then separated from the hydrocarbon phase, achieving high purity fuel without complex separation equipment.

Inventive Principle:
Principle #36Phase transitions

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 approach effectively reduces sulfur content in diesel oil to below 10 ppm, utilizing catalysts like polyoxometalates and porphyrins, and solvent extraction with polar solvents like acetonitrile and methanol, ensuring high selectivity and recyclability of solvents, thereby enhancing the desulfurization process.

Implementation Method 1

treating a hydrocarbon mixture with an aqueous oxidizing agent in the presence of a cage structure catalyst and a co-catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

oxidative conversion of organosulfur compounds in liquid hydrocarbon mixtures

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

selectively removing the oxidized compounds by solvent extraction

Methodology Applied
Scientific EffectSolvent extraction: Liquid-Liquid Extraction

Data Source

PatentUS8715489B2Process for oxidative conversion of organosulfur compounds in liquid hydrocarbon mixtures
Publication Date: 2014.05.06 SAUDI ARABIAN OIL CO
  • US8715489B2 patent drawing
  • US8715489B2 patent drawing
  • US8715489B2 patent drawing

AI summary

The process for the desulfurization of a sulfur-containing hydrocarbon mixture, such as a full-range, hydrotreated diesel oil, is accomplished with an aqueous oxidizing agent in the presence of a catalyst and a co-catalyst, and thereafter selectively removing the oxidized compounds by solvent extraction. Optionally, the foregoing steps are followed by solvent stripping and recovery, and a final polishing step.