High Viscosity PAO Production via 1-Decene-1-Dodecene Mixture Oligomerization

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Solution Overview

Problem

Current methods lack flexibility in producing high viscosity PAO compositions with adequate low temperature performance suitable for industrial lubricants using 1-decene/1-dodecene mixtures, limiting their economic viability and effectiveness.

Innovation Solution

The process involves oligomerizing a mixture of 1-decene and 1-dodecene using an aluminum halide complex with water, with the catalyst and olefins being fed into multiple reactors in series to achieve high viscosity PAOs with kinematic viscosities between 40 to 100 cSt at 100°C and desired low temperature properties, such as low pour points.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If olefins with molecular weight greater than 1-decene are used in oligomerization, then higher viscosity PAOs are produced, but pour points increase (worsening low temperature performance)

Engineering Contradiction:
ImproveviscosityVSAvoidpour point
Core Design Contradiction:
TemperatureVSObject-affected harmful factors

Solution Approach 1:

The invention changes the molecular weight parameters of the olefin feedstock by using a specific mixture ratio of C10/C12 olefins (40-60 wt% C10, 60-40 wt% C12), which allows producing high viscosity PAOs (40-100 cSt at 100°C) while maintaining acceptable pour points through the balanced composition of different chain lengths

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention uses a composite olefin feedstock comprising a mixture of 1-decene and 1-dodecene in specific proportions, combining the benefits of both lighter (lower pour point) and heavier (higher viscosity) components to achieve the desired balance between viscosity and low temperature performance

Inventive Principle:
Principle #40Composite materials

2Adaptability or versatility

If 1-decene/1-dodecene mixtures are used for oligomerization, then high viscosity PAOs with good low temperature performance can be produced, but current methods lack flexibility in achieving desired viscosity ranges

Engineering Contradiction:
Improveviscosity range controlVSAvoidprocess flexibility
Core Design Contradiction:
Adaptability or versatilityVSEase of manufacture

Solution Approach 1:

The invention introduces dynamic control capabilities by adjusting the C10/C12 olefin mixture ratio and using multiple reactors in series with varying residence times, enabling flexible production of PAOs across a wide viscosity range (40-100 cSt at 100°C) while maintaining good low temperature performance

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The invention divides the oligomerization process into multiple reactors in series, allowing different stages of conversion and product distribution in each reactor, which provides flexibility in controlling the final viscosity and molecular weight distribution of the PAO product

Inventive Principle:
Principle #1Segmentation

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 method produces high viscosity PAOs with excellent low temperature performance, achieving kinematic viscosities of 40 to 100 cSt at 100°C and pour points below -30°C, enhancing their suitability for industrial lubricant applications while maintaining economic efficiency.

Implementation Method 1

The process involves oligomerizing a mixture of 1-decene and 1-dodecene using an aluminum halide complex with water

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS7550640B2High viscosity PAOs based on 1-decene/1-dodecene
Publication Date: 2009.06.23 EXXONMOBIL CHEMICAL PATENTS INC

AI summary

This invention relates to the use of 1-decene/1-dodecene olefin mixture to produce high viscosity polyalphaolefins (PAOs) having a viscosity of from about 40 cSt to about 100 cSt at 100° C. (ASTM D-445) and a number average molecular weight of between about 1200 to about 4000, particularly useful as lubricant base stocks.