Membrane Pervaporation Using Venturi Nozzle Vacuum
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Solution Overview
Problem
Existing membrane separation processes face challenges in achieving a sufficient vacuum on the downstream side of the membrane, particularly due to the limitations of vacuum pumps and steam ejectors, which are costly, require complex maintenance, and often necessitate additional treatment of effluent streams.
Innovation Solution
The use of a Venturi-type nozzle with a working fluid that is poorly miscible with the permeate, creating a vacuum without the need for vacuum pumps or steam ejectors, allowing for efficient separation of permeate from the working fluid through immiscibility and gravity separation.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Stress or pressure
If vacuum pumps are used to maintain low partial pressure of permeate, then vacuum is achieved, but maintenance cost increases and permeate condensation becomes difficult
Solution Approach 1:
The invention extracts the vacuum generation function from complex vacuum pumps and implements it through a simple Venturi nozzle that uses fluid dynamics (pressure differential) to create vacuum, eliminating the need for mechanical vacuum pumping equipment and its associated maintenance issues
Solution Approach 2:
The invention replaces the mechanical vacuum pump system with a fluid-based Venturi nozzle system that uses pressure differential and fluid flow to generate vacuum, substituting mechanical complexity with hydraulic simplicity
2Stress or pressure
If steam ejectors are used to produce vacuum, then vacuum is achieved, but steam flow rate requirements increase and effluent treatment is needed
Solution Approach 1:
The invention uses a non-volatile working fluid in the Venturi nozzle that does not require the high steam flow rates needed by steam ejectors, and the working fluid is not contaminated by permeate, eliminating the need for effluent treatment
Solution Approach 2:
The invention converts the pressure differential created by fluid flow through the Venturi nozzle into a beneficial vacuum effect, transforming what would be wasted pressure energy into useful vacuum generation without the harmful byproducts of steam ejectors
3Stress or pressure
If a Venturi nozzle with a working fluid having affinity for permeate is used, then vacuum is produced, but permeate separation becomes complicated
Solution Approach 1:
The invention inverts the conventional approach by using a working fluid that is immiscible with and has no affinity for the permeate, allowing permeate to be easily separated from the working fluid through simple phase separation rather than requiring complex separation processes
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 method provides an efficient and cost-effective vacuum for membrane separation, reducing maintenance needs and improving the separation process by using a converging-diverging nozzle with a liquid working fluid that does not contaminate the permeate, enabling effective separation of multi-component feed streams without the limitations of traditional methods.
Implementation Method 1
the vacuum being produced by a fluid conducted through a Venturi nozzle
Implementation Method 2
selectively permeating at least the first species through the membrane from the first surface to an opposed second surface
Implementation Method 3
under the influence of a concentration gradient that is produced by evaporating the sorbed molecules
Implementation Method 4
the fluid comprises at least one solvent that is poorly miscible with the permeate
Implementation Method 5
efficient separation of permeate from the working fluid through immiscibility and gravity separation
Data Source
AI summary
The invention relates to an improved membrane pervaporation and vapor permeation system in which the vacuum is produced by a fluid passing through a Venturi-type nozzle. The fluid is chosen from solvents that have little or no affinity for the permeate molecules. It is applicable over process feed rates, and can be used for the separation of aromatic species from hydrocarbon.


