Multi-Level Stirring Element for Agitators

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Solution Overview

Problem

Existing agitators face challenges in achieving high-speed operation without compromising mixing efficiency, leading to air intake, foam formation, shear forces, and heating issues, especially when handling sensitive materials like paints, ceramics, and biochemical products, which require gentle stirring and low energy consumption.

Innovation Solution

The agitator design features cups arranged on different levels perpendicular to the shaft, allowing for higher speeds and increased power input while maintaining effective mixing, with each cup having a cone shape and an inlet larger than the outlet, and being connected via support arms to a hub or shaft, enabling efficient mixing at both high and low speeds.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high rotational speeds are used to achieve effective mixing, then mixing efficiency is improved, but air intake and foaming occur

Engineering Contradiction:
Improvemixing efficiencyVSAvoidair intake and foaming
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent transitions from conventional planar cup arrangement to a three-dimensional multi-level configuration where cups are distributed along the axial direction of the shaft. This spatial redistribution allows the mixing system to operate effectively at higher rotational speeds without generating excessive air intake and foaming, as the multi-level arrangement distributes the mixing action across different heights rather than concentrating it in a single plane.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

Solution Approach 2:

The mixing system is divided into multiple independent cup elements arranged at different levels along the shaft. Each cup operates semi-independently, creating localized mixing zones that prevent bulk air entrainment and foaming while maintaining high mixing efficiency. The segmentation allows the system to achieve effective mixing without the harmful effects associated with high-speed operation of conventional single-plane agitators.

Inventive Principle:
Principle #1Segmentation

2Productivity

If high rotational speeds are used to achieve effective mixing, then mixing efficiency is improved, but shear forces damage sensitive mixtures

Engineering Contradiction:
Improvemixing efficiencyVSAvoidshear forces
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

By distributing cups along the axial dimension rather than arranging them in a single plane, the system achieves effective mixing at higher speeds without creating excessive shear forces. The multi-level configuration distributes shear stress across different axial positions, preventing localized high-shear zones that would damage sensitive mixtures while maintaining overall mixing efficiency.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

Solution Approach 2:

Each cup in the multi-level arrangement creates localized mixing zones with controlled shear characteristics. The conical geometry of individual cups generates gentle flow patterns suitable for sensitive materials, while the multi-level distribution ensures comprehensive mixing without requiring excessively high rotational speeds that would generate damaging shear forces throughout the entire mixture.

Inventive Principle:
Principle #3Local quality

3Productivity

If high rotational speeds are used to achieve effective mixing, then mixing efficiency is improved, but heating of the mixture occurs

Engineering Contradiction:
Improvemixing efficiencyVSAvoidmixture temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The multi-level cup arrangement distributes mixing action across different axial positions, allowing effective mixing to be achieved with moderate rotational speeds. This prevents the excessive heat generation that would occur with high-speed operation of conventional single-plane agitators, thereby maintaining temperature control for heat-sensitive mixtures while still achieving thorough mixing.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

Solution Approach 2:

The mixing process is segmented into multiple localized zones created by individual cups at different levels. Each zone contributes to overall mixing efficiency without requiring high rotational speeds, thereby minimizing cumulative heat generation across the entire mixing process while maintaining effective homogenization.

Inventive Principle:
Principle #1Segmentation

4Ease of manufacture

If cups are arranged in a common plane perpendicular to the shaft, then manufacturing and assembly are simplified, but rotational speed is limited without reducing stirring effect

Engineering Contradiction:
Improveassembly simplicityVSAvoidrotational speed
Core Design Contradiction:
Ease of manufactureVSSpeed

Solution Approach 1:

The patent extends the cup arrangement from a two-dimensional planar configuration to a three-dimensional multi-level structure along the axial direction. This spatial extension enables the system to operate at higher rotational speeds while maintaining effective stirring, as the multi-level arrangement distributes the mixing action across different heights, preventing flow disturbances that would limit speed in conventional planar designs.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

5Ease of manufacture

If conventional agitator design is used, then manufacturing is simplified, but dead zones form reducing mixing completeness

Engineering Contradiction:
Improvedesign simplicityVSAvoidmixing completeness
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

By distributing cups along the axial dimension in a multi-level configuration, the system eliminates dead zones that form in conventional single-plane designs. The multi-level arrangement ensures comprehensive fluid circulation throughout the entire mixing volume, including regions near the top and bottom surfaces, thereby achieving complete mixing without significantly complicating the manufacturing of individual cup elements.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 design allows for efficient mixing with reduced energy consumption and prevents flow disturbances, enabling complete coverage and thorough mixing of materials, even at higher speeds, while minimizing the formation of dead zones and maintaining the integrity of temperature-sensitive substances.

Implementation Method 1

the cross-section of the conical pipe section narrows in the opposite direction of rotation, i.e., in the direction of flow. The inlet opening for the flowing material is therefore larger than the outlet opening. Furthermore, the longitudinal axis of the conical pipe section is angled downwards in the direction of rotation.

Methodology Applied
Scientific EffectFlow conditions:

Implementation Method 2

The low speed of the agitators causes counter-currents to form in the mixture, promoting the mixing effect.

Methodology Applied
Scientific EffectCounter-currents:

Implementation Method 3

This design allows for efficient mixing with reduced energy consumption and prevents flow disturbances, enabling complete coverage and thorough mixing of materials

Methodology Applied
Scientific EffectFlow disturbances:

Data Source

PatentEP3639915B1Multi-level stirring element
Publication Date: 2022.07.20 VISCO JET RUHRSYST
  • EP3639915B1 patent drawing
  • EP3639915B1 patent drawing

AI summary

The present invention relates to a stirring element for an agitator for mixing and/or homogenizing flowable media, comprising at least two stirring bodies (2) having an inlet opening and an outlet opening for the flowable medium, wherein the inlet opening (5) is larger than the outlet opening (6), characterized in that the stirring bodies (2) belonging to the stirring element (1) are arranged on different planes normal (perpendicular) to the agitator shaft, each having a defined distance from the other in the axial direction.