Pyrolysis Unit Aromatics Production via RWGS Fermentation Recycling

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Solution Overview

Problem

Current aromatic complexes in the petrochemical industry are unable to efficiently produce biobased aromatics and fail to upgrade carbon in the form of CO and CO2 by-products into high-value compounds, relying predominantly on oil or natural gas feedstocks.

Innovation Solution

Incorporating a reverse water gas shift (RWGS) unit to convert CO2 into CO, followed by a fermentation process to produce ethanol, which is then recycled to the pyrolysis unit to enhance the production of aromatic compounds, allowing for the conversion of CO and CO2 by-products into additional aromatic and paraffin compounds.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If aromatic complexes use conventional pyrolysis processes, then aromatic compounds are produced, but CO and CO2 by-products are generated without being upgraded

Engineering Contradiction:
Improvearomatic compounds productionVSAvoidCO and CO2 by-products
Core Design Contradiction:
Quantity of substanceVSLoss of substance

Solution Approach 1:

The invention converts the harmful CO and CO2 by-products from pyrolysis into valuable aromatic compounds through a multi-step process: RWGS conversion of CO2 to CO, fermentation of CO to ethanol, and pyrolysis of ethanol to aromatics. This transforms waste carbon into high-value products, resolving the contradiction between aromatic production and carbon loss.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

Instead of discarding CO and CO2 as waste streams, the invention recovers carbon from these by-products and reintroduces it into the aromatic production cycle. The carbon is recovered through sequential conversion steps and fed back to the pyrolysis unit, eliminating substance loss while maintaining aromatic production.

Inventive Principle:
Principle #34Discarding and recovering

2Reliability

If aromatic complexes rely on oil or natural gas feedstocks, then stable aromatic production is achieved, but biobased aromatic production is not possible

Engineering Contradiction:
Improvearomatic production stabilityVSAvoidbiobased aromatic production capability
Core Design Contradiction:
ReliabilityVSAdaptability or versatility

Solution Approach 1:

The invention adds multi-functionality to the pyrolysis unit, enabling it to process both conventional hydrocarbon feedstocks and biobased ethanol. This allows the aromatic complex to maintain reliable production from traditional feedstocks while gaining the versatility to produce biobased aromatics, resolving the contradiction between stability and adaptability.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The invention introduces ethanol as an intermediary substance that bridges conventional and biobased production pathways. Ethanol can be produced from biobased sources via fermentation of CO (which comes from pyrolysis gas), then fed to the pyrolysis unit to generate biobased aromatics. This intermediary enables flexible feedstock selection while maintaining process stability.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Device complexity

If CO and CO2 by-products are not converted, then process simplicity is maintained, but carbon upgrade to high-value compounds is not achieved

Engineering Contradiction:
Improveprocess simplicityVSAvoidcarbon upgrade efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The invention performs preliminary conversion of CO2 to CO via RWGS reaction before fermentation. This preliminary action prepares the carbon in a more reactive form (CO instead of CO2), facilitating subsequent fermentation to ethanol and final conversion to aromatics. The staged approach manages complexity while achieving high carbon upgrade efficiency.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention creates a continuous carbon conversion cycle where CO and CO2 from pyrolysis are continuously converted to ethanol via fermentation, which is then continuously fed back to pyrolysis for aromatic production. This continuous cyclic process maximizes carbon utilization efficiency while maintaining operational simplicity through integrated recycling.

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

This approach significantly increases the production of aromatics by pyrolysis of hydrocarbon compounds, upgrading CO and CO2 by-products into high-value compounds, particularly increasing para-xylene production and achieving gains of up to 40% by weight of aromatic compounds.

Implementation Method 1

Incorporating a reverse water gas shift (RWGS) unit to convert CO2 into CO

Methodology Applied
Scientific EffectReverse water gas shift reaction: Chemical Bonding

Implementation Method 2

followed by a fermentation process to produce ethanol

Methodology Applied
Scientific EffectFermentation: Fermentation

Implementation Method 3

significantly increases the production of aromatics by pyrolysis of hydrocarbon compounds

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Data Source

PatentUS11692206B2Production of aromatics by reverse water gas shift, fermentation and recycling to pyrolysis
Publication Date: 2023.07.04 IFP ENERGIES NOUVELLES
  • US11692206B2 patent drawing

AI summary

Device and process for the conversion of a feedstock of aromatic compounds, in which the feedstock is treated notably by means of a fractionation train (4-7), a xylene separation unit (10) and an isomerization unit (11), and in which a pyrolysis unit (13) treats a second hydrocarbon feedstock, produces a pyrolysis effluent feeding the feedstock, and produces a pyrolysis gas comprising CO, CO2 and H2; a reverse water gas shift RWGS reaction section (50) treats the pyrolysis gas and produces an RWGS gas enriched in CO and in water; a fermentation reaction section (52) treats the RWGS gas enriched in CO and in water, to produce ethanol and recycle the ethanol to the inlet of the pyrolysis unit.