Dual Membrane Brine Concentration for High-Recovery Desalination

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing desalination technologies face challenges with high energy consumption, brine volume management, and environmental impact due to high-concentration brine disposal, as well as limitations in membrane durability from scale deposition at high recovery rates.

Innovation Solution

A dual nano-filtration-reverse osmosis brine concentration system utilizing hollow fine fiber forward osmosis (HFF FO) to treat two brine streams, one rich in divalent ions and the other in monovalent ions, allowing for efficient concentration up to 250,000 ppm, facilitating mineral extraction and zero liquid discharge.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If thermal process-based systems (MVC or TVC) are used for brine concentration, then high brine concentration (250,000 ppm) can be achieved, but energy consumption becomes excessively high (24 kWh/m3)

Engineering Contradiction:
Improvebrine concentrationVSAvoidenergy consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The brine concentration process is divided into multiple stages with progressively higher operating pressures. The system uses a first stage operating at lower pressure (e.g., 30-50 bar) and a second stage operating at higher pressure (e.g., 80-100 bar), allowing each stage to operate within optimal efficiency ranges rather than requiring one stage to handle the entire concentration range at excessively high energy input

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system dynamically adjusts operating parameters including pressure, flow rates, and stage configuration based on feed brine characteristics and desired concentrate concentration. This allows optimization of energy consumption across varying operational conditions while maintaining effective brine concentration

Inventive Principle:
Principle #15Dynamics

2Quantity of substance

If recovery rate is increased beyond 50% in SWRO systems, then brine volume is reduced, but osmotic pressure approaches membrane bursting levels and power consumption increases

Engineering Contradiction:
Improvebrine volumeVSAvoidpower consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The recovery process is segmented into multiple stages, with each stage operating at optimized pressure levels. This allows the system to achieve high overall recovery rates by progressively concentrating brine through stages rather than attempting single-stage high recovery, keeping osmotic pressure differences within manageable ranges at each stage

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system changes operating parameters (pressure, temperature, flow rate) across different stages to optimize performance. By adjusting these parameters dynamically, the system can achieve high recovery rates while managing osmotic pressure effects and minimizing power consumption increases

Inventive Principle:
Principle #35Parameter changes

3Quantity of substance

If recovery rate is increased beyond 50% in SWRO systems, then brine volume is reduced, but membrane durability deteriorates due to scale deposition

Engineering Contradiction:
Improvebrine volumeVSAvoidmembrane durability
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

The concentration process is divided into stages with progressively higher operating conditions. This segmentation allows intermediate cleaning and maintenance between stages, preventing cumulative scale deposition that would occur in single-stage high recovery systems, thereby extending membrane life

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system performs preliminary actions such as feed pretreatment and anti-scalant dosing before brine enters the membrane stages. This preliminary protection reduces scale formation on membranes, enabling higher recovery rates without compromising membrane durability

Inventive Principle:
Principle #10Preliminary action

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 enhances energy efficiency, reduces brine volume, and enables commercially viable mineral extraction while maintaining membrane integrity, achieving higher recovery rates and lower specific power consumption.

Implementation Method 1

hollow fine fiber forward osmosis (HFF FO) to treat two brine streams

Methodology Applied
Scientific EffectOsmosis: Osmosis

Implementation Method 2

utilizing hollow fine fiber forward osmosis (HFF FO) to treat two brine streams, one rich in divalent ions and the other in monovalent ions, allowing for efficient concentration up to 250,000 ppm

Methodology Applied
Scientific EffectOsmotic pressure: Osmotic Pressure

Implementation Method 3

dual nano-filtration-reverse osmosis brine concentration system

Methodology Applied
Scientific EffectReverse osmosis: Reverse Osmosis

Data Source

PatentUS20260022046A1Desalination brine concentration system and method
Publication Date: 2026.01.22 SAUDI WATER AUTHORITY
  • US20260022046A1 patent drawing
  • US20260022046A1 patent drawing
  • US20260022046A1 patent drawing

AI summary

A system and method for producing very high concentration brine streams from which commercially efficiently obtained minerals may be obtained is produced by a dual membrane brine concentrator system (DTRI Concentrator). The system includes a nano-filtration system which removes divalent ions from the seawater, a brine concentrator such as a hollow fine fiber forward osmosis system which receives and further concentrates the brine rejected from the nano-filtration system, a SWRO system which receives the NF system permeate and removes monovalent ions, and another brine concentrator which further concentrates the brine rejected from SWRO system. Various permeate and reject brine flow may be forwarded through the Dual Membrane Brine Concentrator system, and multiple stages of the system components may be used, to enhance brine concentration and improve system efficiency.