Multistage Fischer-Tropsch Gas-Liquid Separation to Prevent Wax Deposition

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Solution Overview

Problem

The Fischer-Tropsch process produces a mixture of liquid and gaseous hydrocarbon products and water vapor, which requires cooling to separate wax products from lighter hydrocarbons. However, cooling can cause wax products to solidify and deposit on apparatus components, leading to blockages and inefficiencies.

Innovation Solution

A method involving multiple vapour-liquid separators and coolers arranged in series is used to separate hydrocarbon products and water vapor. This method includes pre-cooling the product stream, separating it into multiple cuts, and cooling each gas stream to condense hydrocarbons and water vapor, thereby preventing wax deposition.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If the product stream is cooled to separate wax products from lighter hydrocarbons, then the separation efficiency is improved, but wax deposits block the apparatus components

Engineering Contradiction:
Improveseparation efficiencyVSAvoidwax deposits
Core Design Contradiction:
Manufacturing precisionVSObject-affected harmful factors

Solution Approach 1:

The cooling and separation process is divided into multiple stages with three vapour-liquid separators arranged in series. Each separator operates at progressively lower temperatures, with the first separator removing wax at higher temperature, the second separator removing heavier hydrocarbons at intermediate temperature, and the third separator removing lighter hydrocarbons at lower temperature. This segmentation prevents wax deposition in downstream components while achieving complete separation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The first vapour-liquid separator performs preliminary removal of wax products from the product stream before the cooled mixture proceeds to subsequent separators. By removing wax early in the process at relatively higher temperatures, the apparatus prevents wax deposition in downstream coolers and separators, eliminating the need for shutdowns and maintenance.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If parallel condensers are used to prevent wax deposits, then continuous operation is maintained, but equipment complexity and cost increase

Engineering Contradiction:
Improvecontinuous operationVSAvoidequipment complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

Instead of using parallel condensers where only one operates at a time, the invention merges multiple vapour-liquid separators into a series configuration. All three separators operate simultaneously in sequence, with each handling a specific fraction of the hydrocarbon mixture. This eliminates idle equipment while achieving continuous operation and complete separation.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The series configuration of three vapour-liquid separators enables continuous separation of all hydrocarbon fractions simultaneously. The product stream flows continuously through all three separators in sequence, with each separator continuously removing its designated fraction. This eliminates the intermittent operation required by parallel condenser systems, maintaining continuous useful action throughout the apparatus.

Inventive Principle:
Principle #20Continuity of useful 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

The method allows for continuous operation and reduces the risk of wax deposits in separators and coolers, maintaining equipment efficiency and reducing maintenance costs. It enables multistage separation and cooling, allowing for controlled separation of hydrocarbon cuts at optimal temperatures.

Implementation Method 1

a first vapour-liquid separator inside which the product stream is separated into a first liquid comprising a first cut of the hydrocarbon products and a first gas stream comprising gaseous hydrocarbon products and water vapour

Methodology Applied
Scientific EffectPhase separation: Phase Change

Implementation Method 2

feeding the first gas stream through a first cooler to apply cooling to the first gas stream to condense a portion of the gaseous hydrocarbon products and water vapour

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

feeding the second liquid and the third liquid into a single decanter inside which the second liquid and the third liquid are separated into liquid hydrocarbon products and water

Methodology Applied
Scientific EffectDensity separation: Density Gradient

Data Source

PatentUS20250115533A1Apparatus and method for gas-liquid separation of a fischer-tropsch reactor outlet stream
Publication Date: 2025.04.10 JOHNSON MATTHEY DAVY TECHNOLOGIES LTD
  • US20250115533A1 patent drawing
  • US20250115533A1 patent drawing

AI summary

Gas-liquid separation comprising a) feeding a product stream comprising a mixture of liquid and gaseous hydrocarbon products and water vapour; b) collecting the first liquid at a liquid outlet of the first vapour-liquid separator; c) discharging the first gas stream from a gas outlet of the first vapour-liquid separator; d) feeding the first cooled mixture from the first cooler into a second vapour-liquid separator; e) collecting the second liquid at a liquid outlet of the second vapour-liquid separator; f) discharging the second gas stream from a gas outlet of the second vapour-liquid separator; g) feeding the second gas stream from the gas outlet of the second vapour-liquid separator through a second cooler; h) feeding the second cooled mixture from the second cooler into a third vapour-liquid separator; i) collecting the third liquid at a liquid outlet; and j) discharging the third gas stream from a gas outlet.