Solvent Clean-Up Zone with Co-Displacement Agent

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Solution Overview

Problem

Existing solvent regeneration techniques in extractive distillation and liquid-liquid extraction processes for aromatics recovery are inadequate for removing heavy hydrocarbons and polymeric sludge, leading to solvent contamination and equipment plugging due to the accumulation of high-boiling-point components.

Innovation Solution

A co-displacement agent is introduced to enhance the capability of a displacement agent in removing heavy hydrocarbons and polymeric materials from the solvent by using a solvent clean-up zone with a counter-current extraction system, where a light hydrocarbon-rich stream is used to 'squeeze out' heavies from the solvent phase into a hydrocarbon phase, reducing the need for high-temperature thermal regenerators.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional thermal solvent regenerator is used to remove heavy hydrocarbons, then heavy HCs with boiling points lower than solvent can be removed, but heavy polymeric materials with boiling points higher than solvent cannot be removed and accumulate in the solvent loop

Engineering Contradiction:
Improvesolvent purityVSAvoidpolymer accumulation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent extracts polymeric materials from the solvent loop by introducing a displacement agent that selectively displaces polymeric materials from the solvent phase into a separate hydrocarbon phase. This allows polymeric materials to be removed from the solvent circulation system without requiring thermal degradation, thereby preventing equipment plugging and maintaining solvent purity.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent introduces a displacement agent as an intermediary substance that facilitates the removal of polymeric materials. The displacement agent interacts with both the solvent phase containing polymeric materials and the hydrocarbon phase, enabling the transfer and separation of polymeric materials from the solvent loop through counter-current extraction.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If thermal regenerator operates at high temperature to strip heavy hydrocarbons, then more heavy HCs can be removed from solvent, but solvent selectivity and solvency are significantly changed

Engineering Contradiction:
Improveheavy HC removal efficiencyVSAvoidsolvent properties
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The patent replaces the thermal field (high temperature) with a mass transfer field using a displacement agent. Instead of using thermal energy to strip heavy hydrocarbons, the system uses a displacement agent that selectively interacts with heavy hydrocarbons and polymeric materials, transferring them from the solvent phase to the hydrocarbon phase through counter-current extraction, thereby maintaining solvent properties while improving removal efficiency.

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

3Reliability

If solvent circulation time is increased to improve separation, then more heavy components can be removed, but polymeric materials accumulate and plug equipment

Engineering Contradiction:
Improveseparation efficiencyVSAvoidequipment operability
Core Design Contradiction:
ReliabilityVSDuration of action of stationary object

Solution Approach 1:

The patent continuously extracts polymeric materials from the solvent circulation system by introducing a displacement agent that selectively displaces polymeric materials into the hydrocarbon phase. This continuous removal prevents polymeric material accumulation and equipment plugging, allowing the solvent loop to operate indefinitely without maintenance interruptions.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent establishes a continuous counter-current extraction process where the displacement agent continuously contacts the solvent phase to displace polymeric materials into the hydrocarbon phase. This continuous action ensures that polymeric materials are constantly removed from the solvent loop, maintaining equipment operability and preventing accumulation over extended circulation times.

Inventive Principle:
Principle #20Continuity of useful action

4Reliability

If water wash method is used to remove heavy hydrocarbons, then heavy HCs and PMs can be removed from solvent stream, but much water is required and process water distribution becomes difficult to balance

Engineering Contradiction:
Improveheavy component removalVSAvoidwater consumption
Core Design Contradiction:
ReliabilityVSQuantity of substance

Solution Approach 1:

The patent extracts heavy hydrocarbons and polymeric materials from the solvent stream using a displacement agent that selectively displaces these components into the hydrocarbon phase. This method eliminates the need for large quantities of water, as the displacement agent directly interacts with the heavy components to transfer them from the solvent phase to the hydrocarbon phase through counter-current extraction.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent introduces a displacement agent as an intermediary that facilitates the removal of heavy hydrocarbons and polymeric materials without requiring water. The displacement agent serves as a mediator that transfers heavy components from the solvent phase to the hydrocarbon phase, eliminating the need for water-based washing and simplifying process water distribution.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 method effectively recovers a solvent substantially free of heavy hydrocarbons and polymeric sludge, reducing the loading requirements of thermal regenerators and maintaining solvent selectivity, thereby preventing equipment plugging and improving process operability.

Implementation Method 1

a light hydrocarbon-rich stream is used to 'squeeze out' heavies from the solvent phase into a hydrocarbon phase

Methodology Applied
Scientific EffectCounter-current extraction: Liquid-Liquid Extraction

Implementation Method 2

a co-displacement agent is used to enhance the capability of a primary displacement agent

Methodology Applied
Scientific EffectDisplacement: Displacement

Data Source

PatentUS8663461B2Extraction process with novel solvent regeneration methods
Publication Date: 2014.03.04 AMT INTERNATIONAL INC
  • US8663461B2 patent drawing
  • US8663461B2 patent drawing
  • US8663461B2 patent drawing

AI summary

Solvent regeneration to recover a polar hydrocarbon (HC) selective solvent substantially free of hydrocarbons (HCs) and other impurities from a solvent-rich stream containing selective solvent, heavy HCs, and polymeric materials (PMs) generated from reactions among thermally decomposed or oxidized solvent, heavy HCs, and additives is provided. A combination of displacement agent and associated co-displacement agent squeezes out the heavy HCs and PMs from the extractive solvent within a solvent clean-up zone. Simultaneously, a filter equipped with a magnetic field is positioned in a lean solvent circulation line to remove paramagnetic contaminants. The presence of the co-displacement agent significantly enhances the capability of the displacement agent in removing the heavy HCs and PMs from the extractive solvent. As a result, the solvent regeneration system operates under milder conditions and minimizes or eliminates the need for including a high temperature, energy intensive and difficult-to-operate thermal solvent regenerator.