Centrifugal Separator Discharge Radius Adjustment for Viscosity Management

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Solution Overview

Problem

The continuous discharge of the heavier phase in centrifugal separators used for processing vegetable or animal oils and fats is hindered by increased viscosity, which cannot be precisely determined, leading to potential blockages and reduced processing efficiency, especially when dealing with substances like soapstock or phosphatides.

Innovation Solution

The method involves adjusting the discharge radius of the heavier liquid phase by pivoting the inlet of the separator element to a larger diameter when viscosity exceeds a limit, and subsequently resetting it to a smaller radius after discharge, using a pivoting mechanism to manage varying feed pressures and prevent clogging.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the discharge radius for the heavier liquid phase is kept fixed, then the separator structure is simple, but the viscosity increase of the heavier phase causes discharge blockages and reduced processing efficiency

Engineering Contradiction:
Improvecontinuous discharge capabilityVSAvoidadjustable discharge radius mechanism
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The discharge radius of the heavier liquid phase is made dynamically adjustable rather than fixed. The separator element can pivot between a first radius (normal operating position) and a second, larger radius (high viscosity position), allowing the system to adapt to changing viscosity conditions and prevent discharge blockages while maintaining processing efficiency.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes the discharge radius parameter in response to viscosity variations. When viscosity exceeds a threshold, the discharge radius is increased to accommodate the thicker liquid phase, preventing clogging. This parameter adjustment allows continuous operation despite changing product properties.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If the discharge radius is increased to handle high viscosity, then blockages are prevented, but the separator element must be reset to smaller radius for normal operation

Engineering Contradiction:
Improvedischarge continuityVSAvoidseparator element positioning
Core Design Contradiction:
ReliabilityVSEase of operation

Solution Approach 1:

The system uses feedback from viscosity monitoring to automatically adjust the discharge radius. When viscosity increases beyond a predetermined threshold, the control system pivots the separator element to the larger radius. After discharge, the element returns to the smaller radius for normal operation, ensuring continuous reliable discharge without manual intervention.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The separator system automatically monitors and adjusts its own discharge radius based on viscosity conditions without requiring external manual control. The control system detects viscosity changes and autonomously positions the separator element at the appropriate radius, making the system self-regulating and easier to operate.

Inventive Principle:
Principle #25Self-service

3Productivity

If the discharge radius is adjusted for high viscosity, then processing efficiency is maintained, but the separator element immersion depth in the heavier phase changes

Engineering Contradiction:
Improveprocessing efficiencyVSAvoidimmersion depth control
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The separator element's radial position is dynamically adjusted based on viscosity conditions. At normal viscosity, the element operates at a smaller radius with greater immersion depth for efficient discharge. When viscosity increases, the element pivots to a larger radius, automatically reducing immersion depth to prevent clogging while maintaining discharge capability.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes the radial position parameter of the separator element in response to viscosity variations. This parameter change inherently adjusts the immersion depth, allowing the system to optimize discharge performance for different viscosity conditions without requiring separate control mechanisms for immersion depth.

Inventive Principle:
Principle #35Parameter changes

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 approach ensures continuous and efficient processing by maintaining the discharge of high-viscosity liquids at a further radius, reducing the risk of blockages and maintaining operational efficiency during changes in viscosity, thereby enhancing the durability and separability of oils and fats.

Implementation Method 1

processing the product, the processing occurring in a centrifuge arranged as a separator, the separator including a rotatable drum... a separator zone formed between the lighter phase and the heavier phase in the separator

Methodology Applied
Scientific EffectCentrifugal separation: Centrifugal Separation

Implementation Method 2

adjusting a discharge radius from discharging the heavier liquid phase when a viscosity of the heavier liquid phase exceeds a limit value... the inlet of the separator element for the heavier liquid phase is pivoted to a larger diameter

Methodology Applied
Scientific EffectViscosity-dependent flow control:

Data Source

PatentUS9561513B2Method for discharging a heavier liquid phase by adjusting a discharge radius based on a viscosity of the heavier liquid phase
Publication Date: 2017.02.07 GEA MECHANICAL EQUIP GMBH
  • US9561513B2 patent drawing
  • US9561513B2 patent drawing
  • US9561513B2 patent drawing

AI summary

A method for the continuous processing of a product such as a vegetable or animal oil or fat. The processing occurs via a separation into two liquid phases and a solid phase. The method step includes processing the product, the processing occurring in a centrifuge arranged as a separator, the separator including a rotatable drum, a disk stack having risers arranged in the drum, a product feed having a feed tube, a first separator disk to discharge a lighter liquid phase from the drum, a second separator disk to discharge a heavier liquid phase from the drum, and a solids discharge opening to discharge a solids phase from the drum. A separation zone is formed between the lighter phase and the heavier phase in the separator.