MSDS

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Zeolite Y Type Products

CBV 100

SiO2/Al2O3 Mole Ratio: 5.1
Nominal Cation Form: Sodium
Na2O Weight %: 13.0
Unit Cell Size, A: 24.65
Surface Area, m2/g: 900

CBV 300

SiO2/Al2O3 Mole Ratio: 5.1
Nominal Cation Form: Ammonium
Na2O Weight %: 2.8
Unit Cell Size, A: 24.68
Surface Area, m2/g: 925

CBV 400

SiO2/Al2O3 Mole Ratio: 5.1
Nominal Cation Form: Hydrogen
Na2O Weight %: 2.8
Unit Cell Size, A: 24.50
Surface Area, m2/g: 730

CBV 500

SiO2/Al2O3 Mole Ratio: 5.2
Nominal Cation Form: Ammonium
Na2O Weight %: 0.2
Unit Cell Size, A: 24.53
Surface Area, m2/g: 750

CBV 600

SiO2/Al2O3 Mole Ratio: 5.2
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.2
Unit Cell Size, A: 24.35
Surface Area, m2/g: 660

CBV 712

SiO2/Al2O3 Mole Ratio: 12
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Unit Cell Size, A: 24.35
Surface Area, m2/g: 730

CBV 720

SiO2/Al2O3 Mole Ratio: 30
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.03
Unit Cell Size, A: 24.28
Surface Area, m2/g: 780

CBV 760

SiO2/Al2O3 Mole Ratio: 60
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.03
Unit Cell Size, A: 24.24
Surface Area, m2/g: 720

CBV 780

SiO2/Al2O3 Mole Ratio: 80
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.03
Unit Cell Size, A: 24.24
Surface Area, m2/g: 780

CBV 901

SiO2/Al2O3 Mole Ratio: 80
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.03
Unit Cell Size, A: 24.24
Surface Area, m2/g: 700

 

Zeolite Beta Type Products

CP814E*

SiO2/Al2O3 Mole Ratio: 25
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 680

CP814C*

SiO2/Al2O3 Mole Ratio: 38
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 710

CP811C-300

SiO2/Al2O3 Mole Ratio: 360
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.05
Surface Area, m2/g: 620

 

Ferrierite Type Product

CP914c

SiO2/Al2O3 Mole Ratio: 20
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 400

Mordenite Type Products

CBV 10A

SiO2/Al2O3 Mole Ratio: 13
Nominal Cation Form: Sodium
Na2O Weight %: 6.5
Surface Area, m2/g: 425

CBV 21A

SiO2/Al2O3 Mole Ratio: 20
Nominal Cation Form: Ammonium
Na2O Weight %: 0.08
Surface Area, m2/g: 500

CBV 90A

SiO2/Al2O3 Mole Ratio: 90
Nominal Cation Form: Hydrogen
Na2O Weight %: 0.05
Surface Area, m2/g: 500

 

ZSM-5 Type Products

CBV 2314

SiO2/Al2O3 Mole Ratio: 23
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 425

CBV 3024E

SiO2/Al2O3 Mole Ratio: 30
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 400

CBV 5524G

SiO2/Al2O3 Mole Ratio: 50
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 425

CBV 8014

SiO2/Al2O3 Mole Ratio: 80
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 425

CBV 28014

SiO2/Al2O3 Mole Ratio: 280
Nominal Cation Form: Ammonium
Na2O Weight %: 0.05
Surface Area, m2/g: 400

 

Aromatics Hydrocarbons Processing

Transalkylation

ATA-11 and ATA-12 catalysts are used in aromatics complexes in the toluene disproportionation unit or transalkylation unit when conversion of toluene and C9+ aromatics to mixed xylenes and benzene is required. The incorporation of a transalkylation unit into an aromatics complex can more than double the yield of paraxylene from naphtha feedstock.

Ethylbenzene reforming

OparisTM series catalysts are used in aromatics complexes when conversion of ethylbenzene to xylenes is required in combination with isomerization of xylenes into the equilibrium composition. Owing to its very high activity and selectivity, OparisTM series catalysts can be used for catalyst replacement when debottlenecking and/or minimum benzene production is desirable.

Ethylbenzene dealkylation type

Zataris catalyst can be used in aromatics complexes when conversion of ethylbenzene to benzene is required in combination with isomerization of xylenes into the equilibrium composition. Zataris catalyst is designed to operate at high activity and selectivity, and is suitable to be used for catalyst replacement when debottlenecking.