Ultrafiltration Phosphorus Removal After Coagulation-Flocculation

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Solution Overview

Problem

Existing wastewater and raw water treatment systems struggle to achieve ultra-low residual phosphorus concentrations, particularly in effluents destined for environmental discharge or reuse, due to limitations in current biological treatment methods and the need for advanced processing to meet stringent phosphorus discharge limits.

Innovation Solution

A water treatment system incorporating a coagulating and flocculating system followed by an ultrafiltration membrane, operated with specific process control parameters, to precipitate and separate dissolved phosphorus effectively, achieving high removal efficiency and sustainable membrane performance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional biological treatment methods are used, then the treatment process is simple and cost-effective, but the residual phosphorus concentration cannot meet stringent discharge limits

Engineering Contradiction:
Improvephosphorus removal precisionVSAvoidtreatment system complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The treatment process is divided into distinct stages: coagulation, flocculation, and ultrafiltration. Each stage targets specific aspects of phosphorus removal, with coagulation precipitating phosphorus compounds, flocculation aggregating particles, and ultrafiltration separating the floc from the effluent. This segmentation enables ultra-low phosphorus concentrations while maintaining operational simplicity through standardized unit operations.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Coagulation and flocculation are performed as preliminary actions before ultrafiltration to pre-concentrate phosphorus into removable floc particles. This preliminary concentration step enhances the efficiency of the subsequent ultrafiltration process, enabling ultra-low residual phosphorus levels without requiring excessively complex or energy-intensive treatment configurations.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If ultrafiltration is operated at high flux rates to increase productivity, then treatment capacity improves, but membrane fouling increases and sustainable operation becomes difficult

Engineering Contradiction:
Improvetreatment capacityVSAvoidmembrane performance stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

Coagulation and flocculation are performed upstream to pre-concentrate phosphorus into large, settleable floc particles before the ultrafiltration membrane. This preliminary action reduces the concentration of fine suspended solids that cause fouling, enabling the membrane to operate at high flux rates (≥150 LMH) sustainably without rapid performance degradation.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system operates the ultrafiltration membrane at high flux rates (≥150 LMH), which is a significant parameter change from conventional low-flux operation. This high-flux operation, combined with optimized coagulant dosing and pH control, maintains high productivity while managing fouling through enhanced scouring effects and reduced contaminant load on the membrane surface.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If coagulating and flocculating agents are added to precipitate phosphorus, then phosphorus removal efficiency improves, but chemical usage and sludge production increase

Engineering Contradiction:
Improvephosphorus removal efficiencyVSAvoidchemical consumption
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The chemical treatment is segmented into coagulation (using aluminum or iron salts to precipitate phosphorus) and flocculation (using polymers to aggregate particles). This segmentation allows optimization of each chemical's dosage and function, improving phosphorus removal efficiency while minimizing total chemical consumption and sludge production through targeted chemical application at each stage.

Inventive Principle:
Principle #1Segmentation

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 system achieves ultra-low residual phosphorus concentrations, exceeding regulatory limits, by utilizing a coagulating and flocculating process with a pH control system and ultrafiltration membrane, ensuring continuous operation and minimizing fouling, thus enhancing the quality of effluents for environmental discharge or reuse.

Implementation Method 1

The coagulating and flocculating system is configured to precipitate dissolved reactive/ortho-phosphorous from the water using the coagulating and flocculating agent

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 2

The ultrafiltration membrane is configured to separate the precipitated phosphorus solids from the flocculated effluent

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Data Source

PatentUS20250361167A1Systems and methods for removing phosphorus from water
Publication Date: 2025.11.27 COMPLETE FILTRATION RESOURCES INC
  • US20250361167A1 patent drawing
  • US20250361167A1 patent drawing
  • US20250361167A1 patent drawing

AI summary

A water treatment system includes a coagulating and flocculating system, an ultrafiltration membrane, and a fluid driver. The coagulating and flocculating system includes a first inlet for receiving water and a second inlet configured to receive a coagulating and flocculating agent. The coagulating and flocculating system is configured to precipitate dissolved phosphorous from the water, and to provide a flocculated effluent at an outlet of the coagulating and flocculating system. The ultrafiltration membrane includes an inlet that is fluidly coupled to an outlet of the coagulating and flocculating system. The ultrafiltration membrane is configured to separate the precipitated phosphorus from the flocculated effluent. The fluid driver is adapted to transfer the flocculated effluent from the outlet of the coagulating and flocculating system to the inlet of the ultrafiltration membrane at sustained flux rates of at least 150 LMH.