Fisher-Tropsch Distillation Segmentation for Energy Reduction

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Solution Overview

Problem

The existing methods for hydrocarbon compound distillation in Fisher-Tropsch synthesis reactions require excessive heating, leading to increased energy costs and inefficiencies in separating naphtha, middle distillate, and wax fractions.

Innovation Solution

Separate fractional distillation of heavy and light hydrocarbon compounds, using a heavy hydrocarbon fractionator and a light hydrocarbon fractionator respectively, to minimize heating requirements and efficiently recover hydrocarbons equivalent to naphtha, with specific temperature and pressure settings to prevent condensation and optimize energy use.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If light hydrocarbon compounds and heavy hydrocarbon compounds are mixed and fractionally distilled together in a single fractionator, then the separation process is simplified, but excessive heating is required leading to increased energy costs

Engineering Contradiction:
Improvedistillation process complexityVSAvoidheating energy consumption
Core Design Contradiction:
Device complexityVSUse of energy by moving object

Solution Approach 1:

The patent divides the distillation process into two separate fractionators: a light hydrocarbon fractionator for processing light hydrocarbon compounds and a heavy hydrocarbon fractionator for processing heavy hydrocarbon compounds. This segmentation allows each fractionator to operate at optimized temperature levels, avoiding the excessive heating that would occur if all hydrocarbons were distilled together in a single unit.

Inventive Principle:
Principle #1Segmentation

2Productivity

If light hydrocarbon compounds are heated to high temperatures for fractional distillation, then separation efficiency is improved, but energy costs increase significantly

Engineering Contradiction:
Improveseparation efficiencyVSAvoidheating energy loss
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

By separating the distillation of light and heavy hydrocarbons into different fractionators, the patent enables light hydrocarbons to be distilled at lower temperatures appropriate to their boiling points, while heavy hydrocarbons are distilled at higher temperatures in a separate unit. This eliminates the energy waste of heating light hydrocarbons to the high temperatures required for heavy hydrocarbon distillation.

Inventive Principle:
Principle #1Segmentation

3Loss of energy

If separate fractionators are used for light and heavy hydrocarbon compounds, then energy consumption is reduced, but device complexity increases

Engineering Contradiction:
Improveheating energy lossVSAvoidfractionation system complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The patent implements segmentation by using separate fractionators for light and heavy hydrocarbons. While this increases the number of units, each fractionator is simpler in design and operation compared to a single complex fractionator handling all hydrocarbon ranges. The segmentation allows for optimized, simpler processing in each unit.

Inventive Principle:
Principle #1Segmentation

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 reduces energy costs and enhances the efficient recovery of naphtha and other hydrocarbon fractions by minimizing unnecessary heating and optimizing distillation conditions.

Implementation Method 1

fractionally distilling heavy hydrocarbon compounds synthesized as a liquid in the Fisher-Tropsch synthesis reaction into a first middle distillate and a wax fraction

Methodology Applied
Scientific EffectFractional distillation: Distillation

Implementation Method 2

fractionally distilling light hydrocarbon compounds synthesized as a gas in the Fisher-Tropsch synthesis reaction into a second middle distillate and a light gas fraction

Methodology Applied
Scientific EffectFractional distillation: Distillation

Implementation Method 3

the light hydrocarbon compounds discharged as a gas from the synthesis reactor are cooled down and liquefied by a heat exchanger

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Data Source

PatentEP2402419B1Method for upgrading hydrocarbon compound and apparatus for separating hydrocarbon compounds by distillation
Publication Date: 2016.06.22 JAPAN PETROLEUM EXPLORATION CO LTD
  • EP2402419B1 patent drawingFigure 1
  • EP2402419B1 patent drawingFigure 2
  • EP2402419B1 patent drawingFigure 3

AI summary

There is provided a method for upgrading hydrocarbon compounds, in which hydrocarbon compounds synthesized in a Fisher-Tropsch synthesis reaction are fractionally distillated, and the fractionally distillated hydrocarbon compounds are hydrotreated to produce liquid fuel products. The method includes fractionally distilling heavy hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a liquid into a first middle distillate and a wax fraction, and fractionally distilling light hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a gas into a second middle distillate and a light gas fraction.