Direct Epoxide Esterification for Diester Lubricant Synthesis

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Solution Overview

Problem

Current methods for synthesizing diester-based lubricants are complex and costly, with a need for simpler and more efficient processes that utilize renewable raw materials, such as biomass and low-value precursors like Fischer-Tropsch olefins and alcohols, to produce high-value ester lubricants.

Innovation Solution

The method involves directly epoxidizing olefins with a carbon number of 8 to 16 and subsequently esterifying the epoxide with C2 to C18 carboxylic acids to form diester species, bypassing the production and isolation of diol intermediates, and using biomass or Fischer-Tropsch reaction products as precursors.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If the conventional three-step synthesis route (epoxidation, diol formation, esterification) is used to produce diester-based lubricants, then the lubricant composition can be obtained, but the process complexity and production cost increase

Engineering Contradiction:
Improveprocess complexityVSAvoidproduction efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent combines steps (2) and (3) of the conventional synthesis route into a single direct esterification step. Instead of isolating the diol intermediate and then esterifying it separately, the method performs direct esterification of the epoxide with carboxylic acid in one operation, thereby reducing process complexity while maintaining production efficiency

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent extracts and eliminates the diol intermediate formation and isolation step from the synthesis pathway. By taking out this intermediate stage, the process is simplified from three steps to two steps, reducing both process complexity and production time without compromising the final lubricant quality

Inventive Principle:
Principle #2Taking out (Extraction)

2Object-affected harmful factors

If renewable raw materials such as biomass and Fischer-Tropsch olefins are used as precursors, then environmental friendliness and cost-effectiveness are improved, but the synthesis process requires optimization to achieve suitable lubricant properties

Engineering Contradiction:
Improveenvironmental impactVSAvoidlubricant property control
Core Design Contradiction:
Object-affected harmful factorsVSManufacturing precision

Solution Approach 1:

The patent employs parameter changes in the direct esterification process, including temperature control (100-200°C), catalyst selection (acid catalysts), and reactant ratios, to optimize the conversion of renewable precursors into diesters with controlled molecular weight and viscosity. These parameter adjustments ensure that the final lubricant meets required performance specifications despite using variable renewable feedstocks

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent produces composite diester molecules combining renewable hydrocarbon chains from biomass or Fischer-Tropsch sources with carboxylic acid moieties. This creates hybrid molecular structures that maintain the desirable lubrication properties of traditional esters while incorporating sustainable feedstock components, achieving both environmental and performance goals

Inventive Principle:
Principle #40Composite materials

3Loss of time

If direct esterification of epoxides is performed without isolating diol intermediates, then production time and cost are reduced, but the reaction selectivity and product purity must be carefully controlled

Engineering Contradiction:
Improveproduction timeVSAvoidreaction selectivity
Core Design Contradiction:
Loss of timeVSManufacturing precision

Solution Approach 1:

The patent uses acid catalysts as intermediaries to facilitate the direct esterification reaction. The catalyst mediates the reaction between epoxide and carboxylic acid, enabling direct conversion without diol isolation while maintaining high selectivity. Common catalysts include sulfuric acid, p-toluenesulfonic acid, or solid acid catalysts that promote the reaction while allowing easy product separation

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The process incorporates feedback control through monitoring reaction progress and adjusting conditions to maintain selectivity. By controlling parameters such as temperature, catalyst amount, and reactant feed rates, the system ensures high conversion to desired diester products while minimizing side reactions, even in the simplified one-step process

Inventive Principle:
Principle #23Feedback

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 results in diester-based lubricants with suitable viscosity and pour point for use as lubricants, offering a more efficient and environmentally friendly alternative by utilizing renewable resources, reducing production costs, and enhancing lubrication properties.

Implementation Method 1

directly esterifying the epoxide with a C2 to C18 carboxylic acid to form a diester species

Methodology Applied
Scientific EffectEsterification: Chemical Bonding

Implementation Method 2

epoxidizing an olefin having a carbon number of from 8 to 16 to form an epoxide comprising an epoxide ring

Methodology Applied
Scientific EffectEpoxidation: Oxidation

Data Source

PatentEP2250241B1Synthesis of diester-based biolubricants from epoxides
Publication Date: 2016.12.21 CHEVRON USA INC
  • EP2250241B1 patent drawing
  • EP2250241B1 patent drawing
  • EP2250241B1 patent drawing

AI summary

The present invention is generally directed to methods of making diester-based lubricant compositions, wherein formation of diester species proceeds via direct esterification of epoxide intermediates. In some embodiments, the methods for making such diester-based lubricants utilize a biomass precursor and/or low value (e.g., Fischer-Tropsch (FT) olefins and/or alcohols) so as to produce high value diester-based lubricants. In some embodiments, such diester-based lubricants are derived from FT olefins and fatty acids. The fatty acids can be from a bio-based source (i.e., biomass, renewable source) or can be derived from FT alcohols via oxidation.