Nested Tray Separator for Grit Resuspension and Blockage Control

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Solution Overview

Problem

Existing separators for removing grit from wastewater are prone to resuspension of settled solids, leading to reduced efficiency and potential blockages due to insufficient spacing between tray units.

Innovation Solution

A separator design with nested tray units featuring a specific offset ratio and concavity ratio in the settling portion, along with controlled inlet positioning and minimum gaps, to minimize resuspension and blockages while enhancing collection efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the trays are spaced closely together to increase separation capacity, then productivity is improved, but the risk of blockages increases due to insufficient spacing

Engineering Contradiction:
Improveseparation capacityVSAvoidblockage risk
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent employs nested tray units where one tray is positioned inside another, creating a compact stacked arrangement. This nesting configuration allows multiple trays to be closely spaced vertically without requiring excessive horizontal clearance, thereby increasing separation capacity while maintaining adequate spacing to prevent blockages between adjacent trays

Inventive Principle:
Principle #7Nested doll (Nesting)

Solution Approach 2:

The invention transitions from a horizontal arrangement of trays to a vertical stacked configuration. By arranging trays in the vertical dimension rather than horizontally, the system achieves higher separation capacity within the same footprint while maintaining sufficient spacing between trays to avoid blockages

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

2Manufacturing precision

If the inlet opening is positioned closer to the separator axis to improve flow distribution, then manufacturing precision is improved, but resuspension of settled solids increases

Engineering Contradiction:
Improveflow distribution uniformityVSAvoidresuspension of solids
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent positions the inlet opening asymmetrically relative to the separator axis, specifically offsetting it from the central axis. This asymmetric positioning creates a controlled flow pattern that distributes wastewater uniformly across the tray surface while directing flow away from the settled solids region, thereby preventing resuspension while maintaining flow distribution uniformity

Inventive Principle:
Principle #4Asymmetry

Solution Approach 2:

The invention creates different flow conditions in different regions of the tray. The inlet opening is positioned to generate a specific flow trajectory that provides gentle, uniform distribution over the settling surface while avoiding direct impingement on settled solids. This localized flow quality control prevents resuspension in the settling zone while maintaining good distribution

Inventive Principle:
Principle #3Local quality

3Productivity

If the settling portion has a steep taper to improve settling efficiency, then productivity is improved, but the cross-sectional area becomes insufficient leading to blockages

Engineering Contradiction:
Improvesettling efficiencyVSAvoidcross-sectional area
Core Design Contradiction:
ProductivityVSArea of stationary object

Solution Approach 1:

The patent employs a curved, concave settling portion rather than a straight taper. The curved surface provides adequate cross-sectional area throughout the settling zone, preventing blockages, while still maintaining sufficient slope to enable efficient particle settling. The curvature allows the surface to taper gradually without creating narrow constrictions

Inventive Principle:
Principle #14Spheroidality (Curvature)

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 design effectively reduces resuspension of solids and minimizes blockages, improving the underflow and total collection efficiencies by optimizing the flow dynamics within the separator.

Implementation Method 1

the low energy vortex allows grit particles entrained by the flow to settle on the sloping inner surface of each tray whereupon the particles gravitate towards and pass through the openings in the trays

Methodology Applied
Scientific EffectGravity: Gravitation

Implementation Method 2

The inlet opening is arranged to provide a tangential inlet such that a low energy vortex flow is established between adjacent trays

Methodology Applied
Scientific EffectVortex flow: Vortex Ring

Data Source

PatentEP4585288A1A separator for separating solids from a solid-liquid mixture
Publication Date: 2025.07.16 HYDRO INTERNATIONAL AG
  • EP4585288A1 patent drawingFigure 1
  • EP4585288A1 patent drawingFigure 2A~2B
  • EP4585288A1 patent drawingFigure 3A~3B

AI summary

There is described a separator 202, 302 for separating solids from a solid-liquid mixture, the separator 202, 302 having a separator axis 208, 308 and comprising a tray assembly 204, 304, the tray assembly 204, 304 comprising a plurality of nested tray units 210, 310, wherein each tray unit 210, 310 comprises: an outlet edge 214, 314 defining an outlet opening 234, 334, the outlet opening 234, 334 having a centroid 236, 336 through which the separator axis 208, 308 extends; an overflow edge 212, 312 defining an overflow opening 232, 332; and a surface 216, 316 extending between the outlet edge 214, 314 and the overflow edge 212, 312, the surface 216, 316 defining an internal volume 215, 315 of the tray unit 210, 310 and an inlet opening 230, 330 for receiving a respective portion of the solid-liquid mixture into the internal volume 215, 315, the surface 216, 316 having a settling portion 226, 326, wherein the settling portion 226, 326 faces the separator axis 208, 308 and tapers inwardly toward the separator axis 208, 308 in a direction 235, 335 toward the outlet edge 214, 314, wherein a cross-sectional area bounded by the settling portion 226, 326 and defined perpendicular to the separator axis 208, 308 is at a maximum on a first plane 238, 338 of the tray unit 210, 310, wherein a cross-sectional profile 241, 341 of the settling portion 226, 326 on the first plane 238, 338 has a centroid 240, 340, wherein a first distance d1 between the inlet opening 230, 330 and the centroid 240, 340 of the cross-sectional profile 241, 341 is greater than a second distance d2 between the inlet opening 230, 330 and the separator axis 208, 308.