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.
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.
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 |
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 |
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.
Potassium Type A (3A) molecular sieves
Sodium Type A (4A) molecular sieves
Calcium type A (5A) Zeolite
The sodium X type (13X) zeolite
DG-palladium catalyst catalyst
XH-7 zeolite
XH-9 zeolite
Massive desiccant
Hollow glass molecular sieve
Ammonia decomposition catalyst (N-938)
Activated Alumina
Ceramic ball