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What are the characteristics and differences of different types of molecular sieve adsorbents?


There are many types of molecular sieve adsorbents, with their core differences stemming from their crystal structure, pore size, silicon-to-aluminum ratio, and cation type. These differences directly determine their adsorption selectivity, stability, and application scenarios. The following are the characteristics and key differences of common types:

1Type A Molecular Sieve

Structure: Cubic crystal system (LTA structure), composed of silicon-oxygen tetrahedra and aluminum-oxygen tetrahedra forming a cage-like structure, with uniform and small pore size.

Key Features: Small pore size (3-5 Å), strong polarity, high selectivity, and low cost.

2Type X and Type Y Molecular Sieve (Type X & Y)

Structure: Both are cubic (FAU) crystals composed of supercages with large pore sizes (8-10 Å). The core difference lies in the silicon-aluminum ratio (SiO/AlO).

3. ZSM-5 Molecular Sieve

Structure: Orthorhombic/monoclinic (MFI structure), composed of intersecting 10-membered ring channels, a high-silica molecular sieve.

Key Features:

Pore diameter approximately 5-6 Å (suitable for adsorption of small C5-C10 molecules), shape selectivity (allowing only linear or small cyclic molecules to enter);

Very wide adjustable Si/Al ratio range (20-2000); high-silica versions exhibit weak hydrophilicity, excellent acid resistance, and thermal stability (1000°C);

Not only an adsorbent, it is also commonly used as a catalyst (due to adjustable surface acidity).

Typical Applications:

Catalysis: Petroleum cracking (gasoline production), methanol to olefins (MTO), aromatics isomerization;

Adsorption: Separation of xylene isomers (such as p-xylene and o-xylene); Removal of trace organic matter from water.

Mordenite (MOR)

Structure: Orthorhombic crystal system, composed of 12-membered and 8-membered ring channels, pore diameter approximately 6-7 Å. Core Features:

High thermal stability (800°C), strong acid resistance (can be used in strong acid environments);

Weak water adsorption (low hydrophilicity), preferring to adsorb non-polar or weakly polar molecules (such as aromatic hydrocarbons and amines).

Typical Applications:

Gas separation (such as separation of C2-C3 hydrocarbons);

Wastewater treatment (adsorption of ammonia nitrogen and organic amines);

Catalysis (such as alkylation reactions).

V. SAPO Series Molecular Sieves (Silicoaluminophosphate Molecular Sieves)

Structure: Synthetic heteroatom molecular sieves with a framework containing Si, Al, and P, and diverse structures (such as SAPO-34, which has a CHA structure).

Core Features:

Adjustable pore size (3-10 Å), low polarity (due to the presence of P, less hydrophilic than pure silica-aluminophosphate molecular sieves);

High adsorption selectivity for non-polar molecules (such as methane and olefins), and excellent thermal and hydrothermal stability. Typical Applications:

Natural gas purification (separation of methane and CO);

Catalysis (e.g., SAPO-34 for methanol to propylene);

Gas drying in low-humidity environments.

Key Differences

Pore Size: Determines the size of molecules that can be adsorbed (e.g., 3A only adsorbs water, 5A adsorbs propane, and 13X adsorbs larger aromatics);

Si/Al Ratio: A higher Si/Al ratio indicates greater thermal stability and acid resistance, but lower hydrophilicity (e.g., Y-type > X-type, ZSM-5 > A-type);

Cation Type: Pore size is adjusted through ion exchange (e.g., 4A 5A: Na⁺ → Ca²⁺, pore size from 4 to 5 Å);

Application Focus: A/X types are primarily used for drying/separation, Y/ZSM-5 for catalysis, and SAPO is suitable for handling non-polar molecules.

Selection should be based on a comprehensive consideration of target molecule size, polarity, operating temperature, and stability requirements.

There are many types of molecular sieve adsorbents, with their core differences stemming from their crystal structure, pore size, silicon-to-aluminum ratio, and cation type. These differences directly determine their adsorption selectivity, stability, and application scenarios. The following are the characteristics and key differences of common types:

1Type A Molecular Sieve

Structure: Cubic crystal system (LTA structure), composed of silicon-oxygen tetrahedra and aluminum-oxygen tetrahedra forming a cage-like structure, with uniform and small pore size.

Key Features: Small pore size (3-5 Å), strong polarity, high selectivity, and low cost.

2Type X and Type Y Molecular Sieve (Type X & Y)

Structure: Both are cubic (FAU) crystals composed of supercages with large pore sizes (8-10 Å). The core difference lies in the silicon-aluminum ratio (SiO/AlO).

3. ZSM-5 Molecular Sieve

Structure: Orthorhombic/monoclinic (MFI structure), composed of intersecting 10-membered ring channels, a high-silica molecular sieve.

Key Features:

Pore diameter approximately 5-6 Å (suitable for adsorption of small C5-C10 molecules), shape selectivity (allowing only linear or small cyclic molecules to enter);

Very wide adjustable Si/Al ratio range (20-2000); high-silica versions exhibit weak hydrophilicity, excellent acid resistance, and thermal stability (1000°C);

Not only an adsorbent, it is also commonly used as a catalyst (due to adjustable surface acidity).

Typical Applications:

Catalysis: Petroleum cracking (gasoline production), methanol to olefins (MTO), aromatics isomerization;

Adsorption: Separation of xylene isomers (such as p-xylene and o-xylene); Removal of trace organic matter from water.

Mordenite (MOR)

Structure: Orthorhombic crystal system, composed of 12-membered and 8-membered ring channels, pore diameter approximately 6-7 Å. Core Features:

High thermal stability (800°C), strong acid resistance (can be used in strong acid environments);

Weak water adsorption (low hydrophilicity), preferring to adsorb non-polar or weakly polar molecules (such as aromatic hydrocarbons and amines).

Typical Applications:

Gas separation (such as separation of C2-C3 hydrocarbons);

Wastewater treatment (adsorption of ammonia nitrogen and organic amines);

Catalysis (such as alkylation reactions).

V. SAPO Series Molecular Sieves (Silicoaluminophosphate Molecular Sieves)

Structure: Synthetic heteroatom molecular sieves with a framework containing Si, Al, and P, and diverse structures (such as SAPO-34, which has a CHA structure).

Core Features:

Adjustable pore size (3-10 Å), low polarity (due to the presence of P, less hydrophilic than pure silica-aluminophosphate molecular sieves);

High adsorption selectivity for non-polar molecules (such as methane and olefins), and excellent thermal and hydrothermal stability. Typical Applications:

Natural gas purification (separation of methane and CO);

Catalysis (e.g., SAPO-34 for methanol to propylene);

Gas drying in low-humidity environments.

Key Differences

Pore Size: Determines the size of molecules that can be adsorbed (e.g., 3A only adsorbs water, 5A adsorbs propane, and 13X adsorbs larger aromatics);

Si/Al Ratio: A higher Si/Al ratio indicates greater thermal stability and acid resistance, but lower hydrophilicity (e.g., Y-type > X-type, ZSM-5 > A-type);

Cation Type: Pore size is adjusted through ion exchange (e.g., 4A 5A: Na⁺ → Ca²⁺, pore size from 4 to 5 Å);

Application Focus: A/X types are primarily used for drying/separation, Y/ZSM-5 for catalysis, and SAPO is suitable for handling non-polar molecules.

Selection should be based on a comprehensive consideration of target molecule size, polarity, operating temperature, and stability requirements.