Sulfolane Recovery Column Vacuum via Liquid-Jet Ejector

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Solution Overview

Problem

Current methods for recovering aromatic hydrocarbons from mixtures with non-aromatic hydrocarbons are inefficient in terms of cost and capital investment, and result in fugitive emissions, while existing solvent recovery processes struggle to maintain extraction efficiency and achieve a hydrocarbon-free solvent.

Innovation Solution

A method involving a solvent-recovery column with a heat source and a liquid-jet ejector to maintain sub-atmospheric pressure, allowing for the separation of polar hydrocarbons from non-polar hydrocarbons, using a solvent like sulfolane, which is recycled and reused, and includes a system for condensing and recycling the solvent to minimize hydrocarbon emissions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional solvent recovery processes are used, then aromatic hydrocarbons can be recovered, but utility costs and capital investment are high

Engineering Contradiction:
Improvearomatic hydrocarbon recoveryVSAvoidutility cost
Core Design Contradiction:
ProductivityVSUse of energy by stationary object

Solution Approach 1:

The patent operates the solvent recovery column at sub-atmospheric pressure (reduced pressure) instead of conventional atmospheric or elevated pressure. This parameter change lowers the boiling point of components, enabling separation at lower temperatures and reducing energy consumption for heating and compression while maintaining effective aromatic hydrocarbon recovery

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a liquid-jet ejector as an intermediary device to create and maintain sub-atmospheric pressure in the condenser and receiver system. The ejector uses a motive fluid (steam or process fluid) to generate vacuum, eliminating the need for conventional high-energy vacuum pumps and reducing utility costs

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If conventional solvent recovery processes are used, then aromatic hydrocarbons can be recovered, but capital investment is high

Engineering Contradiction:
Improvearomatic hydrocarbon recoveryVSAvoidcapital investment
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The liquid-jet ejector serves as a simpler, more cost-effective intermediary device compared to conventional vacuum pump systems. It uses readily available motive fluid to create vacuum, reducing capital investment in vacuum generation equipment while enabling effective solvent recovery operation

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent extracts the vacuum generation function from complex, expensive vacuum pump systems and replaces it with the simpler liquid-jet ejector mechanism. This extraction of the essential function (creating sub-atmospheric pressure) through a simpler means reduces capital investment while maintaining productivity

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If conventional pressure operation is used, then solvent recovery can proceed, but hydrocarbon emissions occur

Engineering Contradiction:
Improvesolvent recoveryVSAvoidhydrocarbon emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent creates a sub-atmospheric pressure (vacuum) environment in the condenser and receiver, which acts as an inert condition that prevents hydrocarbon vapors from escaping to the atmosphere. The vacuum system captures and condenses hydrocarbon vapors that would otherwise be emitted, converting a harmful emission process into a controlled recovery process

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

Solution Approach 2:

The patent utilizes phase transition (condensation) of hydrocarbon vapors in the condenser operating at sub-atmospheric pressure. The vacuum condition enhances condensation efficiency by lowering the partial pressure of hydrocarbons, promoting their transition from vapor to liquid phase for collection and recycling rather than emission

Inventive Principle:
Principle #36Phase transitions

4Ease of operation

If solvent is recycled without sub-atmospheric pressure, then process is simpler, but extraction efficiency decreases

Engineering Contradiction:
Improveprocess simplicityVSAvoidextraction efficiency
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The patent changes the pressure parameter to sub-atmospheric levels, which improves extraction efficiency by enhancing the separation between solvent and hydrocarbons. The reduced pressure lowers the boiling point and reduces solvent vapor pressure, improving the clarity and efficiency of phase separation while maintaining relatively simple operation through the ejector-based vacuum system

Inventive Principle:
Principle #35Parameter changes

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 enhances the recovery of aromatic hydrocarbons by reducing utility and capital costs, minimizing environmental emissions, and maintaining extraction efficiency through the effective separation and recycling of solvents, specifically achieving a hydrocarbon-free solvent stream.

Implementation Method 1

maintaining the sub-atmospheric pressure by connection of the receiver to a liquid-jet ejector, ejecting ejector fluid to a receptacle and recycling fluid from the receptacle to the liquid-jet ejector

Methodology Applied
Scientific EffectLiquid-jet ejector effect: Jet

Implementation Method 2

introducing the mixture into a solvent-recovery column having a heat source connected to a bottom portion of the column

Methodology Applied
Scientific EffectThermal heating: Heating

Implementation Method 3

removing a polar-hydrocarbon-rich overhead stream from the top section of the column and condensing the overhead stream into a receiver operating at a sub-atmospheric pressure

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS8747622B2Aromatics-recovery process
Publication Date: 2014.06.10 UOP LLC
  • US8747622B2 patent drawing
  • US8747622B2 patent drawing
  • US8747622B2 patent drawing

AI summary

The present invention comprises a process for recovery of sulfolane used in a solvent-extraction or extractive-distillation process. A recovery column for the sulfolane solvent comprises a liquid-jet ejector for maintaining the needed vacuum conditions, preferably using water as the liquid.