Zeolite Membrane Operation for Crack-Free Adsorption Separation

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing membrane separation methods, such as those using LTA-type zeolite membranes, are prone to breakage during temperature changes due to uneven adsorptive substance concentration distribution, leading to cracks in the separation membrane.

Innovation Solution

An operating method for a separation device that controls the adsorptive substance concentration distribution within a specific range (0 to 0.3) and adjusts the average Reynolds number of the mixture to 2,000 or more, using a zeolite membrane with a SiO2/Al2O3 molar ratio less than 5, to stabilize the membrane during temperature and pressure changes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If the temperature of the LTA-type zeolite membrane is increased to an adsorption temperature or decreased from the adsorption temperature to room temperature, then the adsorption separation function is improved, but the membrane may break due to thermal stress

Engineering Contradiction:
Improveadsorption temperatureVSAvoidmembrane integrity
Core Design Contradiction:
TemperatureVSStrength

Solution Approach 1:

The patent applies parameter changes by controlling the concentration distribution of adsorptive substance (water) in the mixture to be equal to or less than 0.3. This parameter control prevents uneven adsorption-induced stress on the zeolite membrane during temperature changes, allowing the membrane to maintain its strength while operating at adsorption temperatures. The method transforms the problem from managing thermal stress directly to managing concentration distribution, which indirectly protects the membrane.

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If the concentration distribution of adsorptive substance in the mixture is high, then the adsorption capacity is improved, but uneven volume expansion and contraction of the membrane occurs leading to breakage

Engineering Contradiction:
Improveadsorptive substance concentrationVSAvoidmembrane uniformity
Core Design Contradiction:
Quantity of substanceVSStability of the object's composition

Solution Approach 1:

The patent uses parameter changes by setting a specific threshold (0.3) for the concentration distribution of adsorptive substance. By controlling this parameter, the patent achieves a balance where sufficient adsorption capacity is maintained while preventing the concentration gradients that cause uneven volume expansion and contraction. This parameter control ensures the membrane composition remains uniform during operation.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements feedback control by continuously monitoring the concentration distribution of adsorptive substance in the mixture and adjusting operating conditions to maintain it at or below 0.3. This feedback mechanism ensures that the membrane is always operated within safe concentration limits, preventing the development of uneven stress patterns that would lead to breakage while still achieving effective separation.

Inventive Principle:
Principle #23Feedback

3Stress or pressure

If the Reynolds number of the mixture is low, then the pressure drop is reduced, but the adsorption efficiency decreases due to insufficient mass transfer

Engineering Contradiction:
Improvepressure dropVSAvoidadsorption efficiency
Core Design Contradiction:
Stress or pressureVSProductivity

Solution Approach 1:

The patent applies parameter changes by adjusting the Reynolds number of the mixture to 2,000 or more. This parameter adjustment optimizes the flow regime to enhance mass transfer and adsorption efficiency. By controlling the Reynolds number, the patent achieves sufficient turbulence to improve mass transfer to the membrane surface while managing the pressure drop through system design and operating conditions.

Inventive Principle:
Principle #35Parameter changes

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 method effectively suppresses membrane breakage by ensuring uniform volume expansion and contraction, allowing stable adsorption and separation of substances without cracking.

Implementation Method 1

a mixture heated to a predetermined adsorption temperature is supplied to the LTA-type zeolite membrane to allow a specific substance to be adsorbed to the LTA-type zeolite membrane and separated from the mixture

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

the breakage of the LTA-type zeolite membrane, for example, a crack may occur in a step of separating the specific substance, in particular, in a step of increasing the temperature of the LTA-type zeolite membrane to an adsorption temperature and a step of decreasing the temperature of the LTA-type zeolite membrane from the adsorption temperature to room temperature

Methodology Applied
Scientific EffectThermal expansion: Thermal Expansion

Data Source

PatentEP4691610A1Method for operating separation device
Publication Date: 2026.02.11 NGK INSULATORS LTD
  • EP4691610A1 patent drawingFigure 1
  • EP4691610A1 patent drawingFigure 2
  • EP4691610A1 patent drawingFigure 3

AI summary

Provided is an operating method for a separation device, which enables suppression of breakage of a separation membrane. The operating method for a separation device according to an embodiment of the present disclosure is an operating method for a separation device including a separation membrane, the separation device including: a first flow path to which a mixture containing an adsorptive substance to be adsorbed to the separation membrane is to be supplied; and a second flow path through which a substance that has permeated through the separation membrane is allowed to flow. The operating method for a separation device includes a step of supplying the mixture to the first flow path so that an adsorptive substance concentration distribution in a direction of passage of the mixture becomes larger than 0 and equal to or less than 0.3.