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Molecular Sieves 3A

Molecular Sieve 3A is cation exchanged potassium form of A type crystal structure. The potassium ion is larger than sodium ion, is effectively exchanged in basic 4A type molecular sieve to reduce the pore size to 3 Angstroms and it enables selective adsorption depending upon molecular size.

Molecular sieve 3A is used for dehydration of Hydrocarbon streams in liquid phase or vapour phase due to high drying efficiency and minimizes the interface of Hydrocarbon co-adsorption. Our molecular sieve being spherical in shape produces uniform packing and adsorbate diffusion in the adsorber also exhibits high resistance to attrition and physical damage during service.

Typical Applications :
Drying of Olefines (Cracked gas Drying), liquids for alkylation reactions,
acetylene, ethylene, propylene, ethanol, methanol, carbon dioxide etc.

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Typical technical Data
Parameter  
Shape Spherical Beads

Size 0.5-0.2, 1-3, 2-4 & 3-5 mm

Nominal Pore Opening 3 Angstroms unit

Moisture content as packed 1-2% by wt. At 350’C.

Bulk Density 760 Kgs/cub.mtr.

Crushing strength 2.5-7.5 (varies with dia.)

Attrition Loss 0.25% by wt.

Equilibrium H2O Adsorption Capacity
@ 15% RH & 30’C.
@ 75% RH & 30’C.

 

21.0% wt.
24.0% wt.


Specific Heat 0.20-0.25 Kcals/Kg’C.

Heat of Adsorption Heat of Adsorption

 

 

 

 
Molecular Sieves 4A

Introduction : Molecular Sieves are Crystalline Metal Allumino Silicate with a three dimensional interconnecting network structure of silica and alumina tetrahedra. The widely used Zeolite A is represented by the formula Na12[(AlO2)12(SiO2)12]xH2O. This Molecular Sieve offers maximum degree of selectivity because of its crystalline structure and uniform defined pore diameter.

Regeneration of Molecular Sieve : The original adsorption capacity of a Molecular Sieve is recovered by regeneration. In order to maintain continuos operation, the adsorption continues in a second bed during the regeneration of the saturated bed,. There are different methods of regeneration based on the similar principle. The conditions in the adsorber are modified in such a way that they correspond to a very low loading on the adsorbent.

Thermal regeneration : This involves heating to a temperature at which the adsorption capacity is reduced to a low level so that the adsorbate leaves molecular sieve, This method is commonly used. Heating of the adsorber bed is best carried out indirectly with a steam of hot gas. This serves as a purge medium to remove the desorbed molecules from the bed. In practice the regeneration is carried out at temperature between 180’C. to 300’C.

Regeneration by pressure swing : In this method, the pressure on the adsorber is released so that partial pressure on the impurities lowers remarkably.

Regeneration by Purging : In this method adsorbent is regenerated by Purging by pure medium e.g. liquid or gas without impurities.

 

 

 

 
Product Data :

Grade   244 345

Shape   Sphere Sphere

Size mm 2-4 dia 3-5 dia

Bulk Density Kg/Lit 0.70 min. 0.70 min.

Equilibrium Water Adsorption Capacity @ 30’C.
i. 15% Rh
ii. 75% Rh


% w/w
% w/w

 

21 min.
24 min.

 

21 min.
24 min.


Attrition Loss
% w/w
0.25 max. 0.25 max.

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