Application of ZSM-48 Zeolite

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1. Introduction

The development of zeolite catalysts with tailored pore architectures has been central to the success of the modern petrochemical industry. While medium-pore zeolites (e.g., ZSM-5, ZSM-11, ZSM-22, ZSM-35) dominate many industrial processes, large-pore zeolites play an irreplaceable role in reactions involving bulky molecules that cannot fit into 10-MR channels.

ZSM-48 is a large-pore zeolite with the AFI framework and was first reported by Rubin, Chu, and Maxwell (1981) at Mobil Oil Corporation. It was assigned the structure code AFI by the International Zeolite Association (IZA). Unlike its smaller-pore cousins, ZSM-48 features 12-membered ring channels — the largest ring size among common zeolite frameworks — giving it a pore aperture of ~7.3 Å, comparable to zeolite Beta and significantly larger than ZSM-5 (5.5 Å).

The general chemical composition of ZSM-48 is:

NanAlnSi96nO192mH2O(0<n<96)

with the Si/Al ratio tunable from approximately 5 to infinity, enabling precise control over acidity and hydrophobic character.


2. Structural Characteristics

Property Value
Framework type AFI
Channel system 1D, parallel
Pore opening 7.3 × 7.3 Å (12-MR)
Channel dimension 7.3 × 7.3 Å (elliptical)
Cage type Hexagonal prism
Space group P6/mmm (hexagonal)
Si/Al ratio 5–∞ (tunable)
Crystal density ~1.75 g/cm³
Unit cell parameters a = 18.9 Å, c = 5.1 Å

2.1 The Unique 1D 12-MR Channel System

The defining structural feature of ZSM-48 is its one-dimensional channel system composed of 12-membered rings:

  • The channels run parallel to the c-axis of the hexagonal unit cell.
  • The pore aperture is 7.3 × 7.3 Å (elliptical), which is large enough to accommodate:
    • Tri-isopropylbenzene (kinetic diameter ~7.0 Å)
    • 1,3,5-tri-tert-butylbenzene (~9.0 Å, at channel entrance)
    • Most polycyclic aromatic hydrocarbons (PAHs) up to naphthalene and phenanthrene

However, the strictly one-dimensional nature of the channels means:

  • Diffusion is unidirectional — molecules must enter and exit through the same channel openings
  • Coke precursors formed inside the channels cannot easily escape, leading to faster deactivation compared to 3D large-pore zeolites like Beta
  • This limitation can be mitigated by hierarchical structuring and nanosheet synthesis
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