Triglyceride Transesterification With Carbonate Ester for Single-Phase Biofuel

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Solution Overview

Problem

Existing biofuel production methods face challenges such as catalyzer poisoning, high alcohol consumption, complex recovery processes, and glycerol separation, leading to increased costs and inefficiencies.

Innovation Solution

A process involving a reaction mixture of biosourced triglycerides, carbonate esters, and alcohols under catalytic conditions, which forms a single-phase composition of fatty acid esters and lipophilic glycerol derivatives, eliminating the need for separate catalyst recovery and glycerol separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If supercritical alcohol transesterification is used to reduce catalyst recovery complexity, then device complexity is reduced, but high molar ratio of alcohol increases production costs

Engineering Contradiction:
Improvecatalyst recovery complexityVSAvoidalcohol consumption
Core Design Contradiction:
Device complexityVSQuantity of substance

Solution Approach 1:

The patent uses dimethyl carbonate instead of traditional alcohols as the transesterification agent, changing the chemical parameter to achieve both reduced alcohol consumption and simplified catalyst recovery. The molar ratio of dimethyl carbonate to triglycerides is controlled at 3:1 to 6:1, significantly lower than conventional alcohol ratios.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a solid acid catalyst that can be easily filtered and reused, treating the catalyst as a temporary component that serves its purpose and is then discarded or regenerated through simple filtration, avoiding complex recovery systems.

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

2Productivity

If traditional catalytic transesterification is used, then reaction efficiency is improved, but catalyst separation and regeneration increase process complexity

Engineering Contradiction:
Improvereaction efficiencyVSAvoidcatalyst separation process
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent extracts the catalyst from the reaction mixture through simple filtration, separating it from the products. The solid acid catalyst is removed by filtration, and the filtrate containing fatty acid methyl esters and glycerol undergoes decantation to complete the separation process.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The catalyst system is designed to be self-contained and easily removable through the natural filtration and decantation processes, without requiring complex external separation equipment or multi-step regeneration procedures.

Inventive Principle:
Principle #25Self-service

3Manufacturing precision

If high alcohol molar ratio is used to displace reaction equilibrium, then ester formation is improved, but energy consumption for heating and recycling increases

Engineering Contradiction:
Improveester formation efficiencyVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent changes the transesterification agent from high-molar-ratio alcohol to dimethyl carbonate with a lower molar ratio (3:1 to 6:1), reducing the quantity of material that requires heating and recycling, thereby lowering energy consumption while maintaining ester formation efficiency.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses dimethyl carbonate as an alternative transesterification agent that replicates the function of alcohol but with improved efficiency and lower resource requirements, achieving the same ester formation goal with less energy input.

Inventive Principle:
Principle #26Copying

4Quantity of substance

If glycerol is produced as byproduct, then mass balance is maintained, but glycerol separation is required to use fatty acid esters as biofuel

Engineering Contradiction:
Improvemass balanceVSAvoidglycerol separation process
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The patent segments the separation process into two simple stages: filtration to remove solid catalyst particles, and decantation to separate the glycerol layer from the fatty acid methyl ester layer. This segmented approach avoids complex separation equipment while effectively removing glycerol.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The reaction system naturally produces phase separation between glycerol and fatty acid methyl esters due to their immiscibility, allowing the system to self-separate without requiring external separation equipment. The layers simply need to be allowed to settle and decant.

Inventive Principle:
Principle #25Self-service

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 process achieves high conversion of triglycerides into fatty acid esters with minimal glycerol formation, producing a single-phase composition suitable for biofuel or lubricant use, reducing production costs and environmental impact.

Implementation Method 1

heating the reaction mixture to a reaction temperature to operate a transesterification of the biosourced triglyceride with the carbonate ester under catalysis of the alcohol once in the reaction chamber

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

heating the reaction mixture to a reaction temperature

Methodology Applied
Scientific EffectHeating: Heating

Data Source

PatentUS12516266B2Process for converting biosourced triglycerides into a single-phase composition containing fatty acid ester and related uses as biofuel or lubricant
Publication Date: 2026.01.06 AUTARCYCLE INC
  • US12516266B2 patent drawing
  • US12516266B2 patent drawing
  • US12516266B2 patent drawing

AI summary

The present techniques relate to facilitating conversion of biosourced triglycerides into fatty acid esters by combining the biosourced triglycerides with a carbonate ester in presence of an alcohol, under catalytic transesterification conditions. A reaction mixture can be heated to a reaction temperature to operate a transesterification of the biosourced triglyceride with the carbonate ester under catalysis of the alcohol thereby forming a single-phase composition comprising the fatty acid esters. The reaction mixture can have a molar ratio of the biosourced triglyceride over the carbonate ester between 1:0.1 and 1:20. Compositions comprising the produced single-phase composition, and optionally an additive, can be used as diesel, jet fuel or lubricant.