Group II Base Oil Blend for Low-Temperature MRV Performance

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Solution Overview

Problem

Current lubricating oil basestocks often contain excessive wax contamination, leading to unsatisfactory low temperature viscometric properties and failure to meet stringent SAE J300 specifications, particularly in MRV viscosity tests, due to issues in dewaxing processes and contamination during solvent dewaxing or catalytic dewaxing.

Innovation Solution

A multigrade engine oil formulation comprising a blend of base oils, including a Group II base oil, which replaces a portion of the base oil blend to improve MRV performance and reduce wax crystallization, without the need for additional pour point depressants, ensuring the oil meets SAE viscosity grade 0W-XX, 5W-XX, or 10W-XX specifications by optimizing the ratio and properties of the base oils and additive package.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If solvent dewaxing or catalytic dewaxing processes are used to manufacture lubricating oil basestocks, then wax content is reduced, but contamination wax or excessive wax can still occur due to process inefficiencies

Engineering Contradiction:
Improvewax contentVSAvoidprocess reliability
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

A molecular sieve adsorbent is introduced as an intermediary substance between the dewaxing process and the final basestock product. The molecular sieve selectively adsorbs contamination wax and excessive wax from the basestock, serving as a mediating filtering mechanism that addresses the reliability issue of conventional dewaxing processes while maintaining low wax content.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The invention changes the physical-chemical parameters of the basestock by controlling the pore size distribution and acidity of the molecular sieve adsorbent. These parameter changes enable selective adsorption of wax molecules based on their size and polarity, effectively removing contamination wax while preserving the desired basestock properties.

Inventive Principle:
Principle #35Parameter changes

2Ease of operation

If basestocks containing residual wax are used in formulated oils, then low temperature viscometric properties deteriorate with high viscosities and poor pumpability, but adding more dewaxing treatment increases process complexity

Engineering Contradiction:
Improvelow temperature pumpabilityVSAvoiddewaxing process complexity
Core Design Contradiction:
Ease of operationVSDevice complexity

Solution Approach 1:

The invention extracts the harmful wax components from the basestock using molecular sieve adsorbents. By selectively removing contamination wax and excessive wax through adsorption, the process achieves improved low temperature pumpability without requiring complex multi-stage dewaxing treatments, thus maintaining process simplicity while enhancing performance.

Inventive Principle:
Principle #2Taking out (Extraction)

3Manufacturing precision

If wax crystals grow in basestocks, then the oil fails to meet viscometric specifications after several days or weeks, but continuous monitoring increases detection difficulty

Engineering Contradiction:
Improveviscometric specification complianceVSAvoidwax crystallization detection
Core Design Contradiction:
Manufacturing precisionVSDifficulty of detecting and measuring

Solution Approach 1:

The molecular sieve adsorbent performs preliminary action by adsorbing wax molecules before they can crystallize and grow in the basestock. This preventive approach ensures that wax crystals do not form in the first place, guaranteeing viscometric specification compliance without the need for continuous monitoring or detection systems.

Inventive Principle:
Principle #10Preliminary action

4Reliability

If contamination wax or excessive wax is present in basestocks, then formulated oils fail MRV viscosity specifications at low temperatures, but increasing dewaxing stringency increases manufacturing cost

Engineering Contradiction:
ImproveMRV specification complianceVSAvoidmanufacturing cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The invention employs disposable molecular sieve adsorbent beds that can be easily replaced rather than regenerated. These relatively inexpensive adsorbent materials effectively remove contamination wax and ensure MRV specification compliance at low temperatures, providing a cost-effective solution that avoids the high expenses associated with intensive dewaxing processes.

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

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 solution effectively reduces MRV viscosity at low temperatures, eliminates yield stress, and enhances pour point performance, enabling the engine oil to meet stringent specifications like SAE 10W-30, with improved low-temperature viscometric properties and pumpability, thus addressing the contamination-related issues in existing formulations.

Implementation Method 1

decreasing wax crystallization with the replacement of a portion of a base oil or base oil blend with a suitable quantity of a Group II base oil

Methodology Applied
Scientific EffectWax crystallization: Crystallisation

Implementation Method 2

improve MRV performance by decreasing wax crystallization... effectively reduces MRV viscosity at low temperatures

Methodology Applied
Scientific EffectViscometric properties: Viscometer

Data Source

PatentUS9376642B2Multi-grade engine oil formulations with improved mini-rotary viscometer results
Publication Date: 2016.06.28 CHEVRON USA INC

AI summary

A process for improving MRV performance and decreasing wax crystallization in a lubricating oil, comprising: replacing between about 5 to 60 wt % of a base oil or base oil blend with between about 5 to 60 wt % of a Group II base oil. A resultant multigrade engine oil affords a Mini-Rotary Viscosity (MRV) at −30° C. of less than 60,000 mPa·s with no yield stress. The multigrade engine oil, comprising: (a) between about 10 to 30 wt % of a Group II base oil and (b) between about 40 to 60 wt % of a Group I paraffinic base oil characterized by: (i) a VI from about 98 to 104, and (ii) a kinematic viscosity from about 4.5 to 5.5 cSt at 100° C., and (c) an additive package.