Reactive Chromatography for Hydrocarbon Separation

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Solution Overview

Problem

Current petroleum refining processes rely heavily on thermal distillation, which is energy-intensive and inefficient, separating crude oil based on boiling points rather than molecular class and size, leading to unoptimized processing and inappropriate disposition of molecules.

Innovation Solution

A system and method using reactive chromatography, specifically deasphalted crude oil treated with a catalytic active substrate followed by simulated moving bed chromatography, to separate hydrocarbons into saturate and aromatics fractions, reducing energy consumption and improving separation efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Measurement precision

If thermal distillation is used to separate crude oil fractions, then separation based on boiling point ranges is achieved, but energy consumption is excessive and molecular class separation is not optimized

Engineering Contradiction:
Improveseparation precisionVSAvoidenergy consumption
Core Design Contradiction:
Measurement precisionVSUse of energy by moving object

Solution Approach 1:

The patent replaces the thermal distillation system with a chromatographic separation system that uses adsorption mechanisms instead of thermal phase change. The chromatography column with stationary phase separates hydrocarbons based on molecular class and size through adsorption-desorption processes, eliminating the need for high-temperature heating and condensation cycles while achieving superior separation precision.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent changes the separation parameter from boiling point (thermal property) to molecular class and size (structural property). By using chromatographic media with specific pore sizes and surface chemistries, the system separates molecules based on their structural characteristics rather than volatility, enabling more efficient routing to downstream processes.

Inventive Principle:
Principle #35Parameter changes

2Measurement precision

If distillation separates based on boiling points, then product cuts are obtained, but molecules are not separated by molecular class leading to unoptimized processing

Engineering Contradiction:
Improveseparation precisionVSAvoidprocessing efficiency
Core Design Contradiction:
Measurement precisionVSProductivity

Solution Approach 1:

The patent replaces thermal distillation with chromatographic separation that directly separates molecules by class (paraffins, aromatics, naphthenes) and size. The stationary phase in the chromatography column selectively adsorbs different molecular classes based on their chemical structure and size, producing purified streams that are immediately suitable for downstream conversion processes without requiring additional separation steps.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If conventional distillation and conversion processes are used, then hydrocarbon processing is achieved, but heteroatom species are distributed to multiple processes requiring additional hydroprocessing units

Engineering Contradiction:
Improveprocessing efficiencyVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent extracts and removes heteroatom species (sulfur, nitrogen, oxygen compounds) from the crude oil feed stream before the chromatographic separation step. This pre-treatment ensures that heteroatoms are concentrated in a separate stream and do not contaminate the hydrocarbon fractions, eliminating the need for multiple downstream hydroprocessing units and simplifying the overall process flow.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent performs heteroatom removal as a preliminary action before molecular class separation. By treating the crude oil with hydroprocessing catalysts or adsorbents in advance, the feed stream is cleaned of catalyst poisons and impurities, allowing the chromatographic separation to proceed efficiently without requiring additional treatment steps downstream.

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 enables more efficient separation of crude oil fractions based on molecular class and size, reducing energy consumption and enhancing the quality and yield of refined products by removing heteroatom species and metal-containing asphaltenes, thus optimizing downstream processing.

Implementation Method 1

passing a deasphalted oil stream through a reactor containing an active substrate, wherein the catalytic active substrate adsorbs heteroatom species from the deasphalted oil stream

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

chromatographically separating with a simulated moving bed apparatus or a true moving bed apparatus the pretreated hydrocarbon feed stream into a saturate fraction and an aromatics fraction

Methodology Applied
Scientific EffectChromatography: Chromatography

Data Source

PatentUS11377605B2Molecular separations process
Publication Date: 2022.07.05 EXXONMOBIL TECHNOLOGY & ENGINEERING CO
  • US11377605B2 patent drawing
  • US11377605B2 patent drawing
  • US11377605B2 patent drawing

AI summary

A molecular separation method can include: passing a deasphalted oil stream through a reactor containing an active substrate, wherein the catalytic active substrate adsorbs heteroatom species from the deasphalted oil stream and produces a pretreated hydrocarbon feed stream essentially free of 4+ ring aromatic molecules (ARC 4+ species), metal species, and heteroatom species; and chromatographically separating with a simulated moving bed apparatus or a true moving bed apparatus (SMB/TMB) the pretreated hydrocarbon feed stream into a saturate fraction and an aromatics fraction.