Liquid component separations

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Solution Overview

Problem

Liquid-liquid separation processes, such as distillation, are often energy intensive and complex, requiring large and expensive equipment with high operational costs.

Innovation Solution

A method involving a process liquid stream expansion to vaporize and freeze components, followed by direct-contact heat exchange to further separate the components without heat transfer through the expansion device, allowing energy recovery and efficient separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If distillation is used for liquid-liquid separation, then separation can be achieved, but energy consumption increases and equipment complexity increases

Engineering Contradiction:
Improveseparation effectivenessVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent applies phase transitions by expanding the liquid mixture through an expansion device, causing components to vaporize or freeze based on their phase behavior at reduced pressure. This eliminates the need for continuous heating in distillation, dramatically reducing energy consumption while achieving effective separation through differential phase changes.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention changes the pressure parameter abruptly through an expansion device, transitioning the system from liquid phase to vapor-solid equilibrium. This parameter change enables separation based on differential phase behavior rather than differential volatility requiring continuous heating, thus reducing energy consumption while maintaining separation effectiveness.

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If distillation towers are used for liquid-liquid separation, then separation can be achieved, but equipment size and cost increase

Engineering Contradiction:
Improveseparation effectivenessVSAvoidequipment size and complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent uses phase transitions during expansion to achieve separation in a single stage rather than requiring multi-stage distillation towers. The expansion device followed by a heat exchanger replaces complex distillation equipment with simpler components, reducing equipment size and cost while maintaining separation effectiveness.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention segments the separation process into two distinct stages: (1) expansion and freezing of the heavier component, and (2) condensation and desublimation in the heat exchanger. This segmentation allows each stage to be performed in simple, compact equipment rather than requiring a large, complex distillation tower.

Inventive Principle:
Principle #1Segmentation

3Manufacturing precision

If conventional liquid-liquid separation processes are used, then separation can be achieved, but operational costs increase

Engineering Contradiction:
Improveseparation effectivenessVSAvoidoperational costs
Core Design Contradiction:
Manufacturing precisionVSLoss of energy

Solution Approach 1:

The patent utilizes phase transitions during expansion and condensation to achieve separation without continuous energy input. The expansion device causes spontaneous vaporization and freezing, and the heat exchanger recovers latent heat during condensation and desublimation, minimizing energy loss and reducing operational costs while maintaining effective separation.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention implements thermal feedback by using the heat released during condensation and desublimation in the heat exchanger to pre-cool the incoming liquid mixture. This feedback mechanism recovers energy that would otherwise be lost, reducing operational costs while maintaining separation effectiveness.

Inventive Principle:
Principle #23Feedback

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 simple, thermodynamically efficient separation of liquid components, reducing energy consumption and operational costs while recovering energy from decompression.

Implementation Method 1

The process liquid stream is expanded across the expansion device such that the first component and a first portion of the second component vaporize

Methodology Applied
Scientific EffectVaporization: Evaporation

Implementation Method 2

a second portion of the second component freezes to form a first solid product stream

Methodology Applied
Scientific EffectFreezing: Freezing

Implementation Method 3

The first portion of the second component desublimates into the contact liquid stream as a second solid product stream

Methodology Applied
Scientific EffectDesublimation: Sublimation

Data Source

PatentUS12152835B2Liquid component separations
Publication Date: 2024.11.26 U S BANK TRUST CO NAT ASSOC
  • US12152835B2 patent drawing
  • US12152835B2 patent drawing
  • US12152835B2 patent drawing

AI summary

A method and a system for separating components is disclosed. A process liquid stream, containing a first component and a second component, is passed into an expansion device. The process liquid stream is expanded such that the first component and a first portion of the second component vaporize to form a process vapor stream and a second portion of the second component freezes to form a first solid product stream. The first solid product stream passes out of the expansion device. The process vapor stream passes into a direct-contact heat exchanger against a contact liquid stream. The first portion of the second component desublimates into the contact liquid stream as a second solid product stream. The contact liquid stream and the second solid product stream leave the direct-contact heat exchanger as a slurry stream. The process vapor stream leaves the direct-contact heat exchanger as a stripped process vapor stream.