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Potassium Type A (3A) molecular sieves

Performance

3A molecular sieve, the Shanghai Jiading molecular sieve production plants refers to the crystal structure of the A-type potassium type adsorption critical diameter not greater than 3A molecular,

Typical chemical composition: 2/3K2O·1/3Na2O·Al2O3·2SiO2·9/2H2O.

Use

For unsaturated hydrocarbon materials such as pyrolysis gas, propylene, butadiene, hexyne industrial dehydration can also be used for water, gas, polar liquid (such as ethanol) and gas drying. 3A-type smaller aperture, can be excluded in the process of water adsorption, all other molecules thereby preventing the hydrocarbons of adsorption.

Technical Specifications

Name of index Strip Spherical Hollow glass
Ø1.5-1.7mm Ø3-3.3mm Ø2.0-2.8mm Ø2.8-4.75mm Ø1.0-1.6mm Ø1.6-2.0mm
Attrition rate %≤ 0.3 0.35 0.15 0.15 0.15 0.15
Bulk density g/ml 0.70 0.70 0.75 0.75
Granularity % 98 98 98 98
Static water adsorption % 21.5 21.5 21.5 21.5 21.5 21.5
Ethylene adsorption % 3.0 3.0 3.0 3.0 2.5 2.5
Compressive strength Unit area crush strength N/Granule N/mm2 20 20 60 70 25 26
The coefficient of variation 0.5 0.5 0.3 0.3 0.3 0.3
Package moisture content% 1.5 1.5 1.5 1.5 1.5 1.5

GB10504-89 National Institute of Standards

Name of index Strip Spherical
Ø1.5-1.7mm Ø3-3.3mm Ø2.0-2.8mm Ø2.8-4.75mm
First grade Qualified products First grade Qualified products First grade Qualified products First grade Qualified products
Attrition rate %≤ 0.4 0.6 0.4 0.6
Bulk density g/ml 0.68 0.6 0.68 0.6
Granularity % 96 95 96 95
Static water adsorption % 20 19 20 19 20 19 20 19
Ethylene adsorption % 3.0 3.0 3.0 3.0 3.0 3.0 3.0 3.0
Compressive strength Unit area crush strength
N/Granule N/mm2
18.5 15 18.5 15 44 44 59 59
The coefficient of variation 0.5 0.5 0.5 0.5 0.3 0.3 0.3 0.3
Package moisture content % 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5
Package moisture content Hollow glass
Ø1.0-1.6mm Ø1.6-2.0mm
First grade Qualified products First grade Qualified products
Attrition rate%≤ 0.2 0.3 0.2 0.3
Bulk density g/ml 0.74 0.68 0.74 0.68
Granularity % 98 97 98 97
Static water adsorption% 20 19 20 19
Ethylene adsorption % 2.0 2.0 2.0 2.0
Compression Strength Unit area crush strength
N/Granule N/mm2
14 14 20 20
The coefficient of variation 0.3 0.3 0.3 0.3
Package moisture content % 1.5 1.5 1.5 1.5

Regeneration conditions

I plant the production of 3A, 4A, 5A, 13X molecular sieve available heating and purge or evacuated, renewable reuse.

1. the removal of moisture: available drying gas, such as nitrogen, air, hydrogen, saturated carbonized hydrogen was heated to 150-320 ° C in 0.3-0.5kg/m2 under pressure introduced into the molecular sieve bed, continuing for 3-4 hours, and then tothe sorber pass into the dry cold gas for approximately 2-3 hours, isolated air-cooled to room temperature.

2. the removal of organic material: the available steam from the molecular sieve, the first adsorbate alternative out, then heated to 1, and the regeneration may also be in the 200-350 ℃ superheated vapor or inert gas through the regeneration, (can not be used with the adsorbate.contact produce an explosive mixture of gas).

3. the removal of gaseous material removal method available vacuum regeneration.


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