High-Rate Thickener Eductors for Compact Slurry Separation

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Solution Overview

Problem

Conventional and deep bed thickeners face limitations in operating at optimal solids fraction, lack means to adjust the operating point, and do not effectively direct internal flow to enhance separation efficiency, leading to slow settling rates and high maintenance costs.

Innovation Solution

A high rate thickener design incorporating a central well with adjustable eductors and a lamella-type separator, utilizing counter-current jet streams and turbulence to separate solids from fluids without additional energy input, achieving efficient sediment particle removal.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional thickeners use large horizontal areas for settling, then settling capacity is improved, but space requirement and capital cost increase

Engineering Contradiction:
Improvesettling capacityVSAvoidspace requirement
Core Design Contradiction:
ProductivityVSArea of stationary object

Solution Approach 1:

The patent transitions from conventional horizontal settling areas to a vertical deep bed configuration. The thickener uses a height of 15-30 feet with a conical bottom, utilizing the vertical dimension to achieve hindered settling and compression. This dimensional change allows high settling capacity in a compact footprint, resolving the contradiction between productivity and space requirement.

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

2Productivity

If deep bed thickeners increase vertical height for hindered settling, then separation efficiency is improved, but maintenance requirement and complexity increase

Engineering Contradiction:
Improveseparation efficiencyVSAvoidmaintenance requirement
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent removes the rotating rake mechanism entirely from the deep bed thickener design. Instead of using mechanical rakes to collect solids, the design relies on the conical bottom geometry and hydraulic forces to direct solids to the central discharge opening. This extraction of the complex mechanical rake system eliminates maintenance requirements while preserving high separation efficiency through the vertical deep bed configuration.

Inventive Principle:
Principle #2Taking out (Extraction)

3Device complexity

If thickeners operate without flow direction control, then device complexity is reduced, but settling rate decreases

Engineering Contradiction:
Improvestructure simplicityVSAvoidsettling rate
Core Design Contradiction:
Device complexityVSSpeed

Solution Approach 1:

The patent employs an asymmetric conical bottom geometry with a specific slope angle (30-60 degrees) that naturally directs flow and solids toward the central discharge opening. This asymmetric shape creates hydraulic forces that enhance settling rate without requiring additional mechanical flow direction control devices, thus maintaining structural simplicity while improving settling performance.

Inventive Principle:
Principle #4Asymmetry

4Ease of operation

If conventional thickeners use rotating rake arms for solids removal, then solids discharge is improved, but power consumption and maintenance increase

Engineering Contradiction:
Improvesolids dischargeVSAvoidpower consumption
Core Design Contradiction:
Ease of operationVSUse of energy by moving object

Solution Approach 1:

The thickener design allows solids to be discharged automatically through the central opening at the bottom of the conical structure. The hydraulic forces and gravity acting on the solids naturally move them toward the discharge point without requiring external power or rotating rake mechanisms. This self-service approach eliminates power consumption for solids removal while maintaining effective discharge capability.

Inventive Principle:
Principle #25Self-service

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 promotes higher settling rates and reduces the need for external power, resulting in physically smaller units and lower operational costs while maintaining high separation efficiency.

Implementation Method 1

A high rate thickener design incorporating a central well with adjustable eductors and a lamella-type separator, utilizing counter-current jet streams and turbulence to separate solids from fluids

Methodology Applied
Scientific EffectTurbulence: Turbulence

Implementation Method 2

The separation of solids from the carrier fluid (typically water), settling of the solids is initiated and preferably expedited

Methodology Applied
Scientific EffectSedimentation: Sedimentation

Implementation Method 3

deep bed thickeners/clarifiers rely on the height of the hindered settling to cause separation of the slurry into its clarified liquid and settled solids phases

Methodology Applied
Scientific EffectHindered settling: Sedimentation

Implementation Method 4

deep bed thickeners/clarifiers further typically have a deep, high angle conical bottom for directing the settled solids toward the discharge opening

Methodology Applied
Scientific EffectGravity: Gravitation

Data Source

PatentUS12600656B2High rate thickener and eductors therefor
Publication Date: 2026.04.14 MARMON IND WATER LLC
  • US12600656B2 patent drawing
  • US12600656B2 patent drawing
  • US12600656B2 patent drawing

AI summary

A thickener for dewatering fluids having a vessel with a central well extending proximate a top portion of the vessel to a lower cone-shaped portion, a hindered settling zone, and a compressible sediment layer zone within the lower cone-shaped portion. Eductors housed in inlet wells have an inlet nozzle and a mixing tube to receive slurry to be treated and clear fluid to be mixed with the slurry. The fluid from the eductors is directed in counter circular paths via circular chambers situated proximate the inlet wells, such that fluid flowing in each direction collides and forms turbulence within the central well. Resultant fluid is directed into a lamella-type separator circumferentially located about a portion of the central well, having layered fluid paths directed radially outwards from said center longitudinal axis and upwards towards said vessel top portion through a conical, inclined fluid path, plate structure. The eductors are adjustable with a movable iris for limiting the amount of clear fluid exiting the eductor.