Aromatics Production with CO2 Conversion to Ethanol

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Solution Overview

Problem

Current aromatic complexes in the petrochemical industry are unable to produce biobased aromatics and co-produce ethanol, and they fail to effectively upgrade carbon in the form of CO and CO2 into high-value compounds.

Innovation Solution

Incorporating a reverse water gas shift (RWGS) unit to convert CO2 into CO, followed by a fermentation unit to produce ethanol, while recycling CO2 and utilizing existing catalytic units for aromatics production, allowing for the conversion of all carbon in the feedstock into aromatics and ethanol.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If pyrolysis is used to produce aromatic compounds, then aromatic production is achieved, but CO and CO2 by-products are generated that are not upgraded

Engineering Contradiction:
Improvearomatics productionVSAvoidcarbon in CO and CO2
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent converts the harmful CO and CO2 by-products from pyrolysis into valuable ethanol through a two-step process: first, CO2 is converted to CO via reverse water-gas shift reaction, then both CO and remaining CO2 are fermented into ethanol by microorganisms. This transforms waste carbon into a high-value product, resolving the contradiction between maintaining high aromatics productivity and preventing carbon loss.

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

Solution Approach 2:

The patent changes the chemical state and form of carbon through sequential reactions: CO2 is converted to CO (change in oxidation state and molecular form), then both gases are converted to liquid ethanol through fermentation. These parameter changes enable the transformation of gaseous by-products into a liquid fuel product, achieving carbon upgrading while maintaining aromatics production.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conventional aromatic complex processes are used, then aromatics are produced, but biobased carbon cannot be upgraded and ethanol cannot be co-produced

Engineering Contradiction:
Improvearomatics productionVSAvoidability to produce biobased aromatics and ethanol
Core Design Contradiction:
ProductivityVSAdaptability or versatility

Solution Approach 1:

The patent adds multi-functionality to the aromatic complex by integrating a reverse water-gas shift unit and a fermentation unit. The pyrolysis unit now serves dual purposes: producing aromatics for the existing complex and generating CO/CO2 feedstock for ethanol production. This universal approach enables the same facility to simultaneously produce conventional aromatics, biobased aromatics, and ethanol, resolving the contradiction between productivity and adaptability.

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

Solution Approach 2:

The patent introduces intermediate processing units (reverse water-gas shift unit and fermentation unit) that act as mediators between pyrolysis and final products. These intermediaries convert CO2 to CO, then convert both gases to ethanol, enabling the complex to handle biobased feedstocks and produce multiple products without disrupting existing aromatics production capabilities.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Device complexity

If CO and CO2 are not converted, then process simplicity is maintained, but carbon upgrading and ethanol co-production are lost

Engineering Contradiction:
Improveprocess structureVSAvoidcarbon in by-products
Core Design Contradiction:
Device complexityVSLoss of substance

Solution Approach 1:

Rather than simply disposing of CO and CO2 or burning them for energy, the patent converts these by-products into valuable ethanol through chemical transformation. The reverse water-gas shift unit and fermentation unit add complexity but transform waste into wealth, achieving carbon upgrading and ethanol co-production while maintaining overall process efficiency.

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

Solution Approach 2:

The patent ensures continuous utilization of carbon throughout the process. CO2 from pyrolysis continuously feeds the reverse water-gas shift unit, which continuously produces CO for fermentation, which continuously generates ethanol. This continuous conversion eliminates carbon loss and maintains productive action throughout the entire system, justifying the added complexity through sustained value creation.

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 enables the complete conversion of CO and CO2 by-products into ethanol, co-producing aromatics and upgrading biobased carbon, thereby overcoming the limitations of existing technologies.

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 Transport Reactions

Implementation Method 2

followed by a fermentation unit to produce ethanol

Methodology Applied
Scientific EffectFermentation: Fermentation

Implementation Method 3

Processes for the pyrolysis of hydrocarbon compounds produce aromatic compounds

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Data Source

PatentUS20230374555A1Production of aromatics and ethanol by pyrolysis, reverse water-gas shift reaction, and fermentation
Publication Date: 2023.11.23 IFP ENERGIES NOUVELLES
  • US20230374555A1 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, and produces ethanol.