Lubricant Flow Mixing Control for Target Temperature and Volume

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing methods for dispensing lubricating fluids to mechanical components require complex individual heating and cooling to achieve optimal viscosity and temperature, leading to increased measurement tolerances and complexity, especially when supplying multiple components.

Innovation Solution

A method and system that calculate and regulate the partial volume flows of input fluids based on the actual and target values of the output fluid's volume flow and temperature, reducing the need for multiple measurements and independent control circuits, allowing for precise adjustment of output fluid flow to predetermined targets.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If individual heating and cooling of individual lubricant flows is used to supply multiple components with optimal temperature and viscosity, then the lubrication quality is improved, but the system complexity becomes disproportionately high

Engineering Contradiction:
Improvelubrication qualityVSAvoidsystem complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The system segments the lubrication supply by providing individual temperature and flow control for each component through separate control loops, while using a common reference measurement point to reduce overall system complexity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A common reference measurement point acts as an intermediary for all control loops, allowing individual component control while sharing the measurement infrastructure to reduce complexity

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If separate control loops with independent measurements are used for each input fluid partial flow, then the volume flow and temperature control precision is improved, but the measurement tolerances and error accumulation increase

Engineering Contradiction:
Improvecontrol precisionVSAvoidmeasurement tolerance
Core Design Contradiction:
Manufacturing precisionVSMeasurement precision

Solution Approach 1:

The patent merges the measurement reference point for all control loops into a single common location, combining the measurement infrastructure while maintaining separate control loops for precision

Inventive Principle:
Principle #5Merging (Combining)

3Adaptability or versatility

If multiple independent control loops are implemented for multiple input fluids, then the flexibility and adjustability of the system is improved, but the measurement effort and control complexity increase

Engineering Contradiction:
Improvesystem flexibilityVSAvoidcontrol complexity
Core Design Contradiction:
Adaptability or versatilityVSDevice complexity

Solution Approach 1:

The common reference measurement point serves multiple control loops simultaneously, providing a universal measurement infrastructure that supports flexible control of multiple input fluids without proportionally increasing complexity

Inventive Principle:
Principle #6Universality (Multi-functionality)

Data Source

PatentEP2960744B1Volume flow and temperature control of an output fluid flow
Publication Date: 2023.04.05 SKF LUBRICATION SYST GERMANY
  • EP2960744B1 patent drawingFigure 1~2
  • EP2960744B1 patent drawing
  • EP2960744B1 patent drawing

AI summary

The invention relates to a method for outputting an output fluid flow (Qout), in particular a lubricating fluid flow, with a predetermined target volume flow (Qsoll) and a predetermined target temperature (Tsoll), which consists of at least two input fluids (F1, F2), each with an adjustable partial volume flow (Q1) or (Q2) and a determinable temperature (T1) or (T2).(T2), comprising the steps: - Acquiring an actual volume flow rate (Qist) and an actual temperature (Tist) of the fluid flow (Qout), - Calculating the target partial volume flow rates (Q1 target, Q2 target) to be set based on the target volume flow rate (Qsoll) and the target temperature (Tsoll) of the fluid flow (Qout) and based on the temperatures (T1, T2) of the input fluids (F1, F2), - Calculating actual partial volume flow rates (Q1 actual, Q2 actual) based on the actual volume flow rate (Qist) and the actual temperature (Tist) of the fluid flow (Qout) and based on the temperatures (T1, T2) of the input fluids (F1, F2), and - Controlling the partial volume flow rates (Q1, Q2) to the target partial volume flow rates (Q1 target, Q2 target) using the calculated actual partial volume flow rates (Q1 actual, Q2 is).