Integrated Desulfurization via Mild Hydrotreating and Oxidation

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Solution Overview

Problem

Existing hydroprocessing facilities struggle to meet stringent sulfur and nitrogen reduction standards in hydrocarbon fuels due to the difficulty in upgrading existing hydrotreating reactors to operate at higher temperature and pressure conditions required for ultra-low sulfur production, making conventional desulfurization methods costly and inefficient.

Innovation Solution

An integrated process combining mild hydrotreating with an oxidation reaction zone to separate and remove labile and refractory sulfur and nitrogen compounds, where hydrotreating converts easily removable compounds, and oxidation targets harder-to-remove aromatic compounds, followed by extraction and adsorption of oxidized products.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If existing hydrotreating reactors are upgraded to operate at higher temperature and pressure conditions to achieve ultra-low sulfur production, then sulfur content in fuel is reduced to meet stringent specifications, but capital investment and operational costs increase substantially

Engineering Contradiction:
Improvesulfur content reductionVSAvoidreactor upgrade complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The desulfurization process is segmented into two distinct stages: mild hydrotreating at existing reactor conditions to remove labile sulfur compounds, followed by oxidation treatment specifically targeted at refractory aromatic sulfur compounds. This segmentation allows each stage to be optimized independently, avoiding the need to upgrade existing reactors to harsh conditions while achieving ultra-low sulfur levels in the final product

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention changes the operational parameters from conventional harsh hydrotreating conditions (high temperature and pressure) to mild hydrotreating conditions (lower temperature and pressure), followed by oxidation at controlled conditions. This parameter change enables the use of existing reactor infrastructure without substantial upgrades while achieving the required sulfur reduction to ultra-low levels

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If conventional harsh oxidation conditions are used to remove refractory sulfur compounds, then sulfur content is reduced effectively, but fuel quality deteriorates due to harmful side reactions

Engineering Contradiction:
Improvesulfur content reductionVSAvoidfuel quality degradation
Core Design Contradiction:
Manufacturing precisionVSObject-affected harmful factors

Solution Approach 1:

The oxidation step is conducted under controlled mild conditions with specific oxidizing agents and catalysts, rather than using conventional harsh oxidation conditions. This parameter control achieves effective removal of refractory sulfur compounds while minimizing harmful side reactions that would degrade fuel quality, such as excessive ring opening or formation of unwanted byproducts

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

A catalyst is introduced as an intermediary to facilitate the oxidation of refractory sulfur compounds under milder conditions. The catalyst enables the oxidation reaction to proceed selectively at lower temperatures and with controlled oxidizing agents, reducing the formation of harmful side products while effectively removing sulfur from the fuel

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If new high pressure hydrotreating units are constructed to meet ultra-low sulfur specifications, then sulfur content in fuel is reduced to required levels, but capital investment increases substantially

Engineering Contradiction:
Improvesulfur content reductionVSAvoidnew facility construction
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The process segments sulfur removal into mild hydrotreating (using existing infrastructure) followed by oxidation treatment (can be implemented as a separate, smaller unit). This avoids the need to construct new high-pressure hydrotreating facilities while achieving the same ultra-low sulfur output, substantially reducing capital investment requirements

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The mild hydrotreating step performs preliminary removal of labile sulfur compounds before the oxidation step targets refractory compounds. This preliminary action reduces the overall burden on any single processing unit, enabling the use of existing facilities rather than requiring new high-capacity units

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

This approach allows for cost-effective and efficient reduction of sulfur and nitrogen levels in hydrocarbon fuels, minimizing capital and operational costs by optimizing existing equipment and avoiding harsh oxidation conditions that can harm fuel quality.

Implementation Method 1

contacting the hydrocarbon stream with a hydrotreating catalyst in a hydrotreating reaction zone under mild conditions

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 2

the aromatic-rich fraction is contacted with an oxidizing agent to convert the refractory organosulfur and organonitrogen compounds

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

the oxidized organosulfur and organonitrogen compounds are removed in a separation zone

Methodology Applied
Scientific EffectExtraction: Liquid-Liquid Extraction

Implementation Method 4

followed by extraction and adsorption of oxidized products

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS8741127B2Integrated desulfurization and denitrification process including mild hydrotreating and oxidation of aromatic-rich hydrotreated products
Publication Date: 2014.06.03 SAUDI ARABIAN OIL CO
  • US8741127B2 patent drawing
  • US8741127B2 patent drawing
  • US8741127B2 patent drawing

AI summary

Reduction of sulfur-containing and nitrogen-containing compounds from hydrocarbon feeds is achieved by first contacting the entire feed with a hydrotreating catalyst in a hydrotreating reaction zone operating under mild conditions to convert the labile organosulfur and organonitrogen compounds. An extraction zone downstream of the hydrotreating reaction zone separates an aromatic-rich fraction that contains a substantial amount of the remaining refractory organosulfur and organonitrogen compounds. The aromatic-lean fraction is substantially free of organosulfur and organonitrogen compounds, since the non-aromatic organosulfur and organonitrogen compounds were the labile organosulfur and organonitrogen compounds which were initially removed by mild hydrotreating. The aromatic-rich fraction is oxidized to convert the refractory organosulfur and organonitrogen compounds to oxidized sulfur-containing and nitrogen-containing hydrocarbon compounds. These oxidized organosulfur and organonitrogen compounds are subsequently removed.