2,3-BDO Recovery via Acetalization Phase Separation

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Solution Overview

Problem

Current methods for the separation and recovery of biomass-derived 2,3-butanediol (2,3-BDO) from fermentation broth are energy-intensive and result in low yields due to its aqueous solubility and the need for high thermal energy, as well as challenges in downstream processing, including membrane fouling and solvent usage.

Innovation Solution

A method involving acetalization with an aldehyde in the presence of a heterogeneous catalyst to form cyclic acetals (dioxolanes), followed by trans-acetylation and distillation, which allows for the phase separation and high-purity recovery of 2,3-BDO, with the option to convert dioxolanes into methyl ethyl ketone and butanal for recycling.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If distillation is used to separate 2,3-BDO from fermentation broth, then separation is achieved, but high thermal energy is required making the process energy-intensive and less economical

Engineering Contradiction:
Improveseparation efficiencyVSAvoidthermal energy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The invention changes the physical-chemical parameters of the system by forming cyclic acetals (dioxolanes) through reaction with aldehydes. This chemical transformation alters the volatility and solubility characteristics of 2,3-BDO, enabling separation at lower temperatures via liquid-liquid extraction instead of high-energy distillation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Aldehydes serve as intermediary substances that react with 2,3-BDO to form cyclic acetals. These intermediates enable phase separation by creating a distinct organic phase that can be easily separated from the aqueous fermentation broth, avoiding direct thermal separation

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If conventional homogeneous catalysts are used in reactive extraction, then extraction efficiency is improved, but corrosive strongly acidic environment requires advanced alloys or coatings making the process costly

Engineering Contradiction:
Improveextraction efficiencyVSAvoidequipment cost
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The invention employs solid heterogeneous catalysts that are stable, non-corrosive, and can be easily separated and reused. These catalysts eliminate the need for expensive corrosion-resistant equipment while maintaining high catalytic activity throughout the extraction process

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The invention replaces homogeneous liquid-phase catalysts with heterogeneous solid-phase catalysts. This substitution eliminates the corrosive liquid acid environment while providing easier catalyst separation and reuse, reducing equipment cost and complexity

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Use of energy by moving object

If liquid-liquid extraction is used for 2,3-BDO purification, then energy consumption is reduced, but membrane fouling and solvent usage issues arise

Engineering Contradiction:
Improveenergy consumptionVSAvoiddownstream processing complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

Aldehydes act as intermediaries that form cyclic acetals with 2,3-BDO, creating a distinct organic phase that separates cleanly from the aqueous phase. This intermediary approach enables efficient liquid-liquid extraction without membrane fouling or complex downstream processing

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The invention utilizes liquid-liquid phase separation by forming cyclic acetals that partition into an organic phase. This phase transition approach enables easy separation of 2,3-BDO from fermentation broth without membranes or complex processing equipment

Inventive Principle:
Principle #36Phase transitions

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 process achieves high-purity 2,3-BDO recovery with at least 90% isolated yield, reducing energy consumption and downstream processing challenges, and enables the recycling of butanal, enhancing the economic and environmental sustainability of the process.

Implementation Method 1

acetalization with an aldehyde in the presence of a heterogeneous catalyst forming cyclic acetal (dioxolane)

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

Upon coordination to form cyclic acetals (dioxolane), the product phase separates from the 2,3-BDO/water mixture

Methodology Applied
Scientific EffectPhase separation: Liquid-Liquid Extraction

Implementation Method 3

Trans-acetylation of dioxolane with methanol (methanolysis) followed by distillation of acetal yielding high purity 2,3-BDO

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS11565989B2Separation, recovery and upgrading of biomass derived 2,3-butanediol
Publication Date: 2023.01.31 THE UNITED STATES AS REPRESENTED BY THE DEPARTMENT OF ENERGY
  • US11565989B2 patent drawing
  • US11565989B2 patent drawing
  • US11565989B2 patent drawing

AI summary

The invention relates to a two-way approach to isolate, recover and upgrade 2,3-Butanediol (2,3-BDO) from fermentation broth. A complete separation and recovery process for 2,3-BDO using acetalization and trans-acetalization sequence. Acetalization with butyraldehyde using heterogeneous catalysts, either Amberlyst-15® or Nafion NR50®, efficiently isolates 2,3-BDO as phase-separated protected dioxolane. The approach provides significant process advantages with easy product recovery and high recyclability of the catalyst. Trans-acetalization of dioxolane with methanol (methanolysis) followed by distillation of acetal, yielded very high purity 2,3-BDO with about 90% isolated yield. Alternatively, dioxolane is used in a process direct to methyl ethyl ketone (MEK) as a BDO synthon allowing for recovery of the aldehyde.