Isocarbon-NumberHydrocarbon Separation Membrane

Multi-channel molecular sieve membranes are formed by intergrown zeolite crystals on a multi-channel ceramic support, yielding a dense selective layer 5-10 um thick. Membrane elements incorporate 19 to 61 parallel channels - substantially increasing packing density and reducing footprint compared with conventional tubular molecular sieve modules. Separation is driven by partial-pressure differences across the membrane, exploiting differences in adsorption-diffusion kinetics, molecular size, and shape among isocarbon-number hydrocarbon isomers (e.g., n-butane/isobutane, n-pentane/isopentane) to achieve efficient n/iso separation with high selectivity and low energy consumption. Typical applications include separation and purification of light hydrocarbon mixtures in petrochemical and refining operations.

Multi-channel isocarbon-number hydrocarbon separation membrane elements

Performance Snapshot

01

Packing Density

440 m2/m3

Multi-channel format

02

n/iso-Butane alpha

> 15

Reference binary pair

03

Energy Saving

> 65%

vs. heat-pump distillation

Core Engineering Features

Advanced technological implementations defining the next generation of membrane performance.

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High Packing Density

Packing density reaches 440 m2/m3 - more than six times that of tubular molecular sieve membranes - enabling compact plant design with reduced capital footprint.

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Reduced Sealing and Higher Strength

Sealing components are reduced by approximately 90% versus tubular modules, while mechanical strength is improved by an order of magnitude - supporting reliable industrial operation.

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Molecular-Scale Precision Sieving

Ordered zeolite micropores deliver precise molecular-scale discrimination with high permeation flux and separation selectivity for demanding n/iso hydrocarbon systems.

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Broad C4/C5 Isomer Applicability

Engineered for separation of multiple n/iso-isomer mixtures including C4 and C5 hydrocarbon systems encountered in petrochemical and refining process trains.

Process Architecture

Multi-Channel Architecture and Separation Mechanism

A dense zeolite selective layer (5-10 um) is intergrown on a multi-channel ceramic support. Separation proceeds via adsorption-diffusion differences and molecular size/shape discrimination under a trans-membrane partial-pressure driving force. For n-butane/isobutane systems, isobutane purity can exceed 98% with no auxiliary extractants added - delivering an environmentally friendly, energy-efficient alternative to heat-pump distillation with potential energy savings exceeding 65%.

  • check_circleCompact equipment footprint with straightforward operation and maintenance
  • check_circleNo comparable commercial separation-membrane product category on the market
  • check_circleTypical service life of 5 years or more under recommended operating conditions
Multi-channel molecular sieve membrane module in industrial separation service
Live Telemetry
GS_PORE_CARBON_ARCH

Technical Specifications

Standard specifications for 19-channel and 61-channel multi-channel molecular sieve membrane elements.

ParameterValue
Outer diameter, mm30
Outer diameter, mm30
Length, mm500-1000
Length, mm500-1000
Channel diameter, mm4
Channel diameter, mm2.0
Membrane area per element, m20.23
Membrane area per element, m20.38
n-/iso-Butane selectivity> 15
n-/iso-Butane selectivity> 15
n-Butane permeation rate>=0.001 mol/(m2/s)
n-Butane permeation rate>=0.001 mol/(m2/s)
Applicable systemsPetrochemical and refining light-hydrocarbon mixture separation and purification

Technical FAQ & Resources

Common engineering inquiries and essential documentation for integration planning.

Multi-channel elements (19-61 channels) achieve packing densities up to 440 m2/m3 - more than six times tubular modules - while reducing sealing components by ~90% and improving mechanical strength by an order of magnitude.

For n-butane/isobutane systems, the membrane process can reduce energy consumption by more than 65% compared with heat-pump distillation, while delivering isobutane product purity exceeding 98% without adding auxiliary separation agents.

The membrane is designed for isocarbon-number hydrocarbon isomer separation - including C4 systems such as n-butane/isobutane and C5 systems such as n-pentane/isopentane - leveraging adsorption-diffusion and molecular sieving differences across the zeolite micropore network.

Under recommended operating and maintenance conditions, product service life typically reaches 5 years or more. Equipment structure is compact with straightforward installation, operation, and maintenance procedures.