Ionic Liquid Recovery via Hydrocarbon Fractionation

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Solution Overview

Problem

Existing methods for recovering entrained ionic liquids from hydrocarbon conversion processes are costly and inefficient, particularly due to the need for coalescing materials and limited control over separation processes.

Innovation Solution

A method that increases the ionic liquid volume fraction in the hydrocarbon phase by fractionating and separating the hydrocarbon stream, allowing for coalescence of ionic liquid droplets without the use of coalescing materials, utilizing gravity separation and additional separation zones to recover the ionic liquid.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If conventional liquid-liquid phase separation by gravity is used, then the separation process is simple, but small droplets of ionic liquid remain entrained in the immiscible phase

Engineering Contradiction:
Improveseparation process simplicityVSAvoidionic liquid entrainment
Core Design Contradiction:
Ease of operationVSLoss of substance

Solution Approach 1:

The patent applies preliminary action by performing fractionation of the hydrocarbon phase before final ionic liquid recovery. The hydrocarbon phase is fractionated into at least two fractions, with the lighter fraction containing the entrained ionic liquid droplets. This preliminary separation concentrates the ionic liquid in a specific fraction, making subsequent recovery more effective and reducing overall entrainment losses.

Inventive Principle:
Principle #10Preliminary action

2Loss of substance

If coalescing material is used to recover entrained ionic liquids, then ionic liquid recovery efficiency is improved, but process cost and device complexity increase

Engineering Contradiction:
Improveionic liquid recovery efficiencyVSAvoidcoalescing material requirement
Core Design Contradiction:
Loss of substanceVSDevice complexity

Solution Approach 1:

The patent extracts the ionic liquid recovery function from the traditional coalescing material approach. Instead of using external coalescing materials, the method utilizes the inherent fractionation process to separate and concentrate ionic liquid droplets in the lighter hydrocarbon fraction, followed by gravity separation. This eliminates the need for additional coalescing materials and associated equipment complexity.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The system performs self-service by using the existing fractionation process to achieve ionic liquid concentration and separation. The fractionation process itself, combined with gravity separation, provides the coalescing function without requiring external coalescing materials. The process leverages its own operational steps to achieve recovery, reducing external dependencies.

Inventive Principle:
Principle #25Self-service

3Loss of substance

If additional ionic liquid is added to increase volume fraction, then ionic liquid recovery is improved, but process cost increases

Engineering Contradiction:
Improveionic liquid recoveryVSAvoidionic liquid volume
Core Design Contradiction:
Loss of substanceVSQuantity of substance

Solution Approach 1:

The patent introduces the lighter hydrocarbon fraction as an intermediary medium. This fraction acts as a mediator that naturally concentrates ionic liquid droplets through the fractionation process. By directing the lighter fraction to a separate gravity separation zone, the system achieves ionic liquid concentration without adding more ionic liquid, using instead the intermediary hydrocarbon fraction as the concentration vehicle.

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 entrained ionic liquids with higher efficiency and reduced costs by leveraging existing process conditions, enhancing collision frequency and coalescence of droplets, and allowing for their separation through gravity or other methods.

Implementation Method 1

separating the process stream comprising a mixture of hydrocarbons and ionic liquid into an ionic liquid phase and a hydrocarbon phase in a gravity separation zone

Methodology Applied
Scientific EffectGravity separation: Gravitation

Implementation Method 2

flashing at least a portion of the process stream comprising a mixture of hydrocarbons and ionic liquid into a vapor phase comprising a first portion of at least one first hydrocarbon and a liquid phase comprising a second portion of the at least one first hydrocarbon

Methodology Applied
Scientific EffectFlashing: Flash Evaporation

Implementation Method 3

coalescing ionic liquid droplets onto a coalescing material, coalescing the small droplets into larger droplets

Methodology Applied
Scientific EffectCoalescence: Coagulation

Data Source

PatentUS9522859B2Methods for recovering ionic liquid fines from a process stream
Publication Date: 2016.12.20 UOP LLC
  • US9522859B2 patent drawing
  • US9522859B2 patent drawing
  • US9522859B2 patent drawing

AI summary

Methods of recovering droplets of ionic liquid catalyst from a process stream are described. The volume fraction of ionic liquid in the hydrocarbon is increased to cause the ionic liquid droplets to coalesce. One method incorporates various combinations of gravity separation zone(s) and fractionation zones. Another method involves using a combination of a flash vessel and a fractionation zone, as well as an optional gravity separation zone.