Blended Ionic Liquid Draw Material for Forward Osmosis
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Solution Overview
Problem
The existing forward-osmosis desalination technology faces challenges in reducing the residual amount of draw solution in the produced water, which increases operating costs and affects water quality, due to temperature-sensitive materials used in the draw solution.
Innovation Solution
A blended-type extracted material for forward osmosis is developed, comprising specific ionic compounds that adjust phase-transition temperatures and reduce residual amounts in the water-rich phase by mixing temperature-sensitive ionic compounds, allowing for efficient separation of the draw solution from water.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Ease of manufacture
If temperature-sensitive materials are used as draw solution to facilitate separation, then separation procedure is simplified, but residual draw solution concentration in produced water increases to 10-15%
Solution Approach 1:
The patent uses a composite draw solution comprising multiple temperature-sensitive materials (such as combinations of PEG and polysaccharides, or multiple ionic liquids with different LCSTs) to achieve both easy temperature-based separation and reduced residual concentration. The composite formulation allows synergistic effects where each component contributes to different aspects of separation efficiency and residual reduction.
Solution Approach 2:
The patent employs materials with specific lower critical solution temperatures (LCSTs) that change phase behavior at controlled temperatures. By selecting materials with appropriate LCST parameters (e.g., PEG 200 with LCST ~20°C, PEG 400 with LCST ~35°C), the system enables complete phase separation at elevated temperatures, reducing residual draw solution concentration below detection limits while maintaining high osmotic pressure during operation.
2Device complexity
If single-type ionic compound is used, then system is simple, but phase-transition temperature adjustment and residual reduction are limited
Solution Approach 1:
The patent divides the draw solution into multiple ionic compound components, each with distinct properties (different anions like CH3SO3−, I−, CF3COO−, or different cations with varying alkyl chains). This segmentation allows independent optimization of each component's contribution to osmotic pressure and phase-transition behavior, enabling precise control over separation temperature and residual concentration through compositional adjustments.
Solution Approach 2:
The patent designs ionic compounds with multifunctional characteristics where the same base structure (e.g., phosphonium or nitrogen-containing cations) can pair with different anions to achieve multiple functions: maintaining high osmotic pressure, enabling temperature-responsive phase separation, and reducing residual concentration. This universality allows a single ionic liquid platform to address multiple performance requirements simultaneously.
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 blended material effectively reduces the residual concentration of the draw solution in the water-rich phase, optimizing the forward-osmosis system's performance and energy consumption by adjusting the phase-transition temperature and improving the separation efficiency.
Implementation Method 1
The forward-osmosis (FO) desalination technology uses the difference of osmotic pressure across a membrane as a driving force to attract water from a water-feeding end with low salinity (low osmotic pressure) to a draw-solution end with high salinity (high osmotic pressure).
Implementation Method 2
The phase-separation unit includes an aqueous layer and an ionic liquid layer. The concentration of the extracted material in the ionic liquid layer is greater than the concentration of the extracted material in the aqueous layer.
Data Source
AI summary
An extracted material for forward osmosis is provided. The extracted material includes a first ionic compound, a second ionic compound and a third ionic compound, which are represented by formula {K[A+(R1)(R2)(R3)]p}(X−)c(Y−)d. X− is the same as Y− in the first ionic compound. X− is the same as Y− in the second ionic compound. X− in the first ionic compound is different from X− in the second ionic compound. X− differs from Y− in the third ionic compound. X− in the third ionic compound is the same as X− in the first ionic compound or X− in the second ionic compound. Y− in the third ionic compound is the same as Y− in the first ionic compound or Y− in the second ionic compound. A method for preparing an extracted material and a forward-osmosis water desalination system using the same are also provided.


