Red Mud-Supported Catalyst for Single-Step Furfural to EFE Conversion

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Solution Overview

Problem

Existing catalytic methods for converting furfural to ethylfurfuryl ether (EFE) are inefficient, often requiring multi-step processes and showing poor selectivity, leading to diminished yields and the need for numerous purification steps.

Innovation Solution

A single-step process using a red mud-supported catalyst, such as Rh@RM, Ir@RM, or Ru@RM, in the presence of a hydrogen-containing gas and an alcohol solvent, effectively converts furfural to EFE with improved selectivity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional catalytic methods are used for converting furfural to EFE, then the process can be established, but the selectivity towards EFE is poor and multiple purification steps are required

Engineering Contradiction:
Improveselectivity towards EFEVSAvoidnumber of purification steps
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent combines hydrogenation and etherification reactions into a single integrated catalytic process using a bifunctional catalyst system. The metal component (Ru, Rh, or Ir) performs hydrogenation of furfural to furfuryl alcohol, while the acidic support (red mud, alumina, or silica) simultaneously catalyzes the etherification with ethanol to form EFE, eliminating the need for separate reaction steps and purification operations.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The invention employs composite catalysts consisting of noble metals (Ru, Rh, or Ir) supported on acidic materials (red mud, alumina, or silica). This composite structure integrates the hydrogenation activity of the metal with the acid-catalyzed etherification capability of the support, achieving high selectivity towards EFE in a single step while simplifying the overall process configuration.

Inventive Principle:
Principle #40Composite materials

2Productivity

If multi-step processes are used for EFE production, then the conversion can be achieved, but the process efficiency is reduced and yields are diminished

Engineering Contradiction:
Improveprocess efficiencyVSAvoidnumber of process steps
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent merges two separate chemical transformations (hydrogenation and etherification) into a single concerted catalytic process. By using a bifunctional catalyst that possesses both metal sites for hydrogenation and acidic sites for etherification, the process completes both reactions in one operation, significantly improving productivity and reducing processing time compared to sequential multi-step methods.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The catalyst is pre-designed with dual functionality before the reaction begins. The metal particles are deposited on the acidic support in advance, creating a integrated catalytic system that can perform both hydrogenation and etherification simultaneously when reactants are introduced, eliminating the need for separate preparation steps and intermediate handling.

Inventive Principle:
Principle #10Preliminary action

3Quantity of substance

If conventional catalysts are used for furfural hydrogenation, then the reaction can proceed, but the yield of desired products is reduced due to poor selectivity

Engineering Contradiction:
Improveyield of EFEVSAvoidselectivity towards EFE
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The invention uses composite catalysts where noble metals (Ru, Rh, or Ir) are supported on acidic materials (red mud, alumina, or silica). The metal component provides high activity for hydrogenation while the acidic support directs the reaction towards etherification, achieving high selectivity towards EFE and maximizing the yield of the desired product.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The catalyst exhibits different functional properties at different locations: the metal particles provide hydrogenation activity while the acidic support sites provide etherification activity. This spatial distribution of different catalytic functions within a single catalyst structure enables high selectivity towards EFE by ensuring that the hydrogenated intermediate is immediately converted to the desired ether product.

Inventive Principle:
Principle #3Local quality

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 achieves furfural conversion of at least 60% with EFE present in 30 to 80 wt% of the conversion product, overcoming the inefficiencies of previous methods by enhancing selectivity and reducing the need for multiple steps.

Implementation Method 1

reacting the hydrogen of the hydrogen-containing gas and furfural in the presence of the red mud-supported catalyst to form the conversion product

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

calcining a red mud material at a temperature of 400 to 600° C. to form a calcined material

Methodology Applied
Scientific EffectHeating: Heating

Data Source

PatentUS20250376453A1Hydrogenation of furfural to biofuel using a metal nanoparticle impregnated red mud catalyst
Publication Date: 2025.12.11 KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
  • US20250376453A1 patent drawing
  • US20250376453A1 patent drawing
  • US20250376453A1 patent drawing

AI summary

A method of converting furfural to a conversion product includes introducing furfural, an alcohol solvent and a red mud-supported catalyst to a reactor and mixing to form a mixture. The method includes introducing a hydrogen-containing gas into the reactor and contacting with the mixture thereby reacting the hydrogen of the hydrogen-containing gas and furfural in the presence of the red mud-supported catalyst to form the conversion product. The red mud-supported catalyst is at least one of a red mud-supported rhodium (Rh@RM) catalyst, a red mud-supported iridium (Ir@RM) catalyst, and a red mud-supported ruthenium (Ru@RM) catalyst.