Supercritical Alkyl Ester Production with CO2 and Metal Oxide Catalyst

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Solution Overview

Problem

Current methods for producing biodiesel from lipid feedstocks are inefficient and do not fully utilize the potential of carbon dioxide and carbon monoxide in catalyzing transesterification and esterification reactions, leading to incomplete conversion and high residual free fatty acid levels.

Innovation Solution

A process involving mixing lipid feedstocks with alcohol, carbon dioxide, and/or carbon monoxide, along with a metal oxide catalyst under supercritical conditions, which includes using alumina, titania, or zirconia catalysts, to enhance the conversion of triglycerides to alkyl esters, and optionally adding acids or bases to optimize reaction conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional transesterification or esterification reactions are used without carbon dioxide and acids, then the process is simpler, but the conversion of triglycerides to alkyl esters is incomplete and residual free fatty acid levels remain high

Engineering Contradiction:
Improveconversion rate of triglycerides to alkyl estersVSAvoidreaction mixture composition complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

Carbon dioxide and acids are introduced as intermediary substances that facilitate the transesterification and esterification reactions. The carbon dioxide, when combined with water, forms carbonic acid which acts as a catalyst to enhance the conversion of triglycerides to alkyl esters and reduce residual free fatty acids, thereby improving productivity without requiring complex additional equipment

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The reaction conditions are optimized by controlling the amount of carbon dioxide (at least 0.1 wt. percent of alcohol mass) and adjusting temperature (200-400°C) and pressure to supercritical conditions. These parameter changes enhance the catalytic effect and reaction efficiency, achieving high conversion rates while maintaining a relatively simple process

Inventive Principle:
Principle #35Parameter changes

2Productivity

If metal oxide catalysts are used under supercritical conditions with carbon dioxide and acids, then the yield of alkyl esters increases by at least 10%, but the reaction conditions become more stringent

Engineering Contradiction:
Improveyield of alkyl estersVSAvoidreaction temperature and pressure requirements
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent utilizes supercritical conditions (temperature 200-400°C and pressure sufficient to achieve supercritical state) to enhance the solubility and reactivity of carbon dioxide and alcohol, thereby significantly improving alkyl ester yield. The metal oxide catalyst (alumina, titania, or zirconia) is specifically selected for its stability and catalytic activity under these stringent supercritical conditions, achieving at least 10% higher yield compared to conventional methods

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The combination of metal oxide catalyst with carbon dioxide and acid creates a composite catalytic system that leverages the synergistic effects of all components. The metal oxide provides surface catalysis while carbon dioxide and acids contribute to the reaction mechanism, resulting in enhanced productivity that justifies the more stringent temperature and pressure requirements

Inventive Principle:
Principle #40Composite materials

3Manufacturing precision

If carbon dioxide is added in amounts of at least 0.1 wt. percent of alcohol mass, then residual free fatty acids are reduced to acceptable levels, but the process complexity increases

Engineering Contradiction:
Improveresidual free fatty acid level controlVSAvoidprocess control complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

By precisely controlling the carbon dioxide dosage (at least 0.1 wt. percent of alcohol mass) and maintaining supercritical conditions, the patent achieves excellent control over residual free fatty acid levels. This parameter control enables the carbon dioxide to effectively participate in the reaction and reduce free fatty acids to acceptable levels without requiring complex additional control systems

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Carbon dioxide serves as an intermediary that, when dissolved in the reaction mixture under supercritical conditions, forms carbonic acid which catalyzes the esterification of free fatty acids. This intermediary mechanism provides a straightforward pathway to reduce free fatty acid levels while maintaining relatively simple process control

Inventive Principle:
Principle #24Intermediary (Mediator)

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 increases the yield of alkyl esters by at least 10% compared to reactions without carbon dioxide and/or acids, while reducing residual free fatty acids to acceptable levels, achieving high conversion rates and meeting ASTM D6751-06a specifications.

Implementation Method 1

contacting the reaction mixture with a catalyst under supercritical conditions for the alcohol, the catalyst including a metal oxide

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

contacting the reaction mixture with a catalyst under supercritical conditions for the alcohol

Methodology Applied
Scientific EffectSupercritical fluid: Supercritical Fluid

Data Source

PatentUS10696923B2Methods and apparatus for producing alkyl esters from lipid feed stocks, alcohol feedstocks, and acids
Publication Date: 2020.06.30 SARTEC CORP
  • US10696923B2 patent drawing
  • US10696923B2 patent drawing
  • US10696923B2 patent drawing

AI summary

Embodiments herein relate to the production of alkyl esters from lipid feed stocks. In an embodiment, a process for producing alkyl esters is included. The process can include mixing a lipid feed stock with an alcohol, water, and at least one of carbon dioxide, carbon monoxide, and/or one or more acids to form a reaction mixture, and contacting the reaction mixture with a catalyst under supercritical conditions for the alcohol, the catalyst comprising a metal oxide. Other embodiments are also included herein.