Carbon-Modified Zeolite Membrane for Ethanol Dehydration

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Solution Overview

Problem

Zeolite membranes with high water separation performance typically have low hydrothermal endurance, limiting their effectiveness in sustained separation processes.

Innovation Solution

A zeolite membrane complex with a molar ratio of carbon to aluminum and silicon greater than or equal to 0.1 and a silicon/aluminum molar ratio of 1 to 6, incorporating a structure-directing agent (SDA) that stabilizes the crystal structure, enhancing both water separation performance and hydrothermal endurance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a zeolite membrane with high water separation performance is used, then water separation performance is improved, but hydrothermal endurance deteriorates

Engineering Contradiction:
Improvewater separation performanceVSAvoidhydrothermal endurance
Core Design Contradiction:
ReliabilityVSDuration of action of stationary object

Solution Approach 1:

The patent changes the chemical composition parameters of the zeolite membrane by incorporating carbon at a molar ratio of C/(Al+Si) ≥ 0.1 and controlling the Si/Al molar ratio between 1 and 6. This parameter modification allows the membrane to achieve both high water separation performance (separation factor ≥ 1000) and improved hydrothermal endurance, resolving the traditional trade-off between these two properties.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates a composite zeolite membrane material that combines traditional aluminum-silicon zeolite structure with carbon incorporation. This composite approach, where carbon is integrated into the zeolite framework at specific ratios, produces a material that simultaneously exhibits high water separation performance and enhanced resistance to hydrothermal degradation.

Inventive Principle:
Principle #40Composite materials

2Duration of action of stationary object

If carbon content in zeolite membrane is increased to improve hydrothermal endurance, then hydrothermal endurance is improved, but water separation performance may deteriorate

Engineering Contradiction:
Improvehydrothermal enduranceVSAvoidwater separation performance
Core Design Contradiction:
Duration of action of stationary objectVSReliability

Solution Approach 1:

The patent optimizes the carbon content parameter by specifying a molar ratio of C/(Al+Si) ≥ 0.1, which is sufficient to improve hydrothermal endurance without excessive carbon accumulation. This precise parameter control ensures that hydrothermal stability is enhanced while water separation performance is maintained at separation factor ≥ 1000 levels.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent applies carbon incorporation locally within the zeolite structure at controlled concentrations rather than uniformly throughout. This localized quality approach allows carbon to provide hydrothermal protection at specific sites within the membrane structure while maintaining the overall water separation functionality of the zeolite framework.

Inventive Principle:
Principle #3Local quality

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 zeolite membrane complex achieves a total permeation flux of at least 1.0 kg/m2 h and a water-to-ethanol separation factor of 1000, while maintaining high hydrothermal endurance, even after exposure to hot water, due to the presence of the SDA in the pores.

Implementation Method 1

Zeolite membrane are conventionally used as separation membranes using a molecular-sieving function

Methodology Applied
Scientific EffectMolecular sieving: Molecular Sieve

Implementation Method 2

when a mixed solution having a temperature of 60° C. and containing 50 mass % of water and 50 mass % of ethanol is supplied with a permeate pressure of −94.66 kPaG, a total permeation flux is higher than or equal to 1.0 kg/m2 h

Methodology Applied
Scientific EffectPermeation: Permeation

Data Source

PatentUS20240278193A1Zeolite membrane complex and membrane reactor
Publication Date: 2024.08.22 NGK INSULATORS LTD
  • US20240278193A1 patent drawing
  • US20240278193A1 patent drawing

AI summary

A zeolite membrane complex includes a porous support and a zeolite membrane formed on the support and containing aluminum, silicon, and carbon. In the zeolite membrane, the molar ratio of carbon to the sum of aluminum and silicon is higher than or equal to 0.1. In the zeolite membrane complex, when a mixed solution having a temperature of 60° C. and containing 50 mass % of water and 50 mass % of ethanol is supplied with a permeate pressure of −94.66 kPaG, the total permeation flux is higher than or equal to 1.0 kg/m2 h, and a separation factor of water to ethanol is greater than or equal to 1000.