Self-adaptive UF Membrane Control via Real-time Resistance Monitoring

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Solution Overview

Problem

Ultrafiltration (UF) systems face challenges in maintaining long-term operation due to membrane fouling, as existing backwash strategies are often inefficient and require frequent chemical cleaning, leading to increased operational costs and reduced membrane lifespan.

Innovation Solution

A self-adaptive control system that monitors UF membrane resistance in real-time, triggering backwash operations based on resistance thresholds and adjusting coagulant dosing to optimize filtration and backwash cycles, utilizing RO concentrate for backwash and integrating with reverse osmosis (RO) systems for enhanced efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If frequent backwash operations are performed to clean the UF membrane, then filtration performance is maintained, but operational time and productivity are reduced

Engineering Contradiction:
Improvefiltration performanceVSAvoidoperational time
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The system continuously monitors transmembrane pressure (TMP) and calculates membrane resistance in real-time. When resistance reaches a predetermined threshold indicating fouling, the controller automatically triggers backwash operations. This feedback mechanism ensures backwash is performed only when necessary, maintaining filtration performance while maximizing operational time between backwashes.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The UF system performs self-cleaning through automatic backwash operations triggered by the control system based on monitored resistance levels. The system serves itself by detecting fouling conditions and initiating cleaning without external intervention, optimizing the balance between maintaining performance and preserving operational time.

Inventive Principle:
Principle #25Self-service

2Reliability

If chemical cleaning is performed frequently to remove fouling, then membrane reliability is maintained, but membrane lifespan is reduced and operational costs increase

Engineering Contradiction:
Improvemembrane performanceVSAvoidmembrane lifespan
Core Design Contradiction:
ReliabilityVSDuration of action of stationary object

Solution Approach 1:

The system performs preliminary mechanical backwashing before chemical cleaning is required. By continuously monitoring membrane resistance and triggering backwash at optimal thresholds, the system removes fouling layers mechanically before they become entrenched and require harsh chemical cleaning, thereby extending membrane lifespan and reducing chemical consumption.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system dynamically adjusts backwash parameters including flow rate, duration, and frequency based on real-time membrane resistance measurements. This adaptive approach optimizes cleaning effectiveness while minimizing the need for intensive chemical cleaning operations, preserving membrane integrity and extending service life.

Inventive Principle:
Principle #35Parameter changes

3Reliability

If coagulant dosing is increased to reduce fouling, then filtration performance is improved, but chemical consumption and operational costs increase

Engineering Contradiction:
Improvefiltration performanceVSAvoidchemical consumption
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The control system monitors membrane resistance and adjusts coagulant dosing dynamically based on actual fouling conditions. When resistance increases indicating fouling, the system adjusts dosing to optimize performance. This feedback-based dosing ensures chemicals are used only when and where needed, reducing overall consumption while maintaining effective filtration.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system transitions from static, fixed-dose coagulant addition to dynamic, adaptive dosing that responds to real-time membrane resistance measurements. This dynamic adjustment optimizes the balance between filtration performance and chemical consumption, using more coagulant when fouling risk is high and less when conditions are favorable.

Inventive Principle:
Principle #15Dynamics

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 extends the operational period of UF systems, reduces chemical cleaning frequency, and maintains effective filtration performance by adapting to changing fouling conditions and water quality, thereby improving membrane longevity and operational efficiency.

Implementation Method 1

Ultrafiltration (UF) is a filtration process utilized for treating water and other liquids in order to remove colloids, micron- and submicron-sized particles (e.g., >about 20-50 nanometers) and biological entities (e.g., bacteria) from water

Methodology Applied
Scientific EffectUltrafiltration: Filter (physical)

Implementation Method 2

a desalination device fluidly connected to the filtration device, the desalination device configured to perform reverse osmosis desalination on the filtrate

Methodology Applied
Scientific EffectReverse osmosis: Reverse Osmosis

Implementation Method 3

the metering unit configured to supply a coagulant into the feed stream

Methodology Applied
Scientific EffectCoagulation: Coagulation

Data Source

PatentUS10576428B2Self-adaptive control and optimization of membrane filtration
Publication Date: 2020.03.03 RGT UNIV OF CALIFORNIA
  • US10576428B2 patent drawing
  • US10576428B2 patent drawing
  • US10576428B2 patent drawing

AI summary

An apparatus includes 1) a filtration device including a filtration module to generate a filtrate from an input stream; 2) a desalination device fluidly connected to the filtration device; and 3) a controller configured to direct operation of the filtration device and the desalination device. In a first mode of operation, the filtration module is configured to perform filtration as part of generating the filtrate. In a second mode of operation, the filtration module is configured to receive an output from the desalination device such that the output backwashes the filtration module. The controller is configured to monitor a change in membrane resistance of the filtration module during the first mode of operation, and is configured to trigger the filtration module to enter the second mode of operation based on the change in membrane resistance.