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Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene

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Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene

Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene
Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene

Large Image :  Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene

Product Details:
Place of Origin: china
Brand Name: QD
Certification: ISO9001:2015
Model Number: SiO2/Al2O3=20-150
Payment & Shipping Terms:
Minimum Order Quantity: 1 kg
Price: USD40000-100000 Ton
Packaging Details: 25kg/bags or 500kg/bags and carbon
Delivery Time: 5-8days
Payment Terms: T/T, L/C
Supply Ability: 1000Ton per month

Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene

Description
SiO2/Al2O3: 20-200 Color: White Powder
Total Specific Surface: 500-650 M2/g Microporous Specific Surface: 430-460m2/g
CAS: 1318-02-1 Larger Export: 1000ton
High Light:

650 M2/G Beta Zeolite Catalysts

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Sodium Beta Zeolite Catalysts

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Zeolite Catalysts for Benzylation of Naphthalene

Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene: Effect of Pore Structure and Acidity

SiO2/Al2O3 Mole Ratio: 25-200

Nominal Cation Form: Sodium/Hydrogen

Na2O Weight %: 0.1

Surface Area, m2/g: 540

Zeolite beta

Mesoporous Beta Zeolite Catalysts for Benzylation of Naphthalene 0

 

Abstract: To improve the catalytic performance of zeolite catalysts in reactions involving bulky
molecules, a series of mesoporous Beta zeolite were prepared using organic functionalized fumed
silica as the silicon source, which were thoroughly characterized in terms of porosity and acidity.
The peaks in X-ray diffraction (XRD) patterns showed broadening, and the external surface area
and mesoporosity increased progressively when the content of organic functionalization increased.
An infrared (IR) spectroscopy study of adsorbed probe molecules, including pyridine (Py-IR),
2,6-ditertbutylpyridine (DTBPy-IR) and pivalonitrile (Pn-IR), showed that the improvement of
mesoporosity increased the accessibility of acidic sites. In the catalytic benzylation of naphthalene
with benzyl chloride (BC) over the mesoporous Beta zeolite catalysts, the conversion of BC was
signifificantly increased when the accessibility of Brönsted acid sites improved. The increase of
mesoporosity not only improved the diffusion ability of the reactants and products, but also increased
the accessibility of acid sites, which greatly enhanced the activity of the mesoporous Beta zeolite
catalysts. It is highlighted that the interdependence of mesoporosity, acid type, acid concentration,
and strength of the mesoporous Beta zeolites on the catalytic performance in the benzylation of
naphthalene with BC was comprehensively studied.

 

β molecular sieves have three mutually intersecting 12-ring channels, it is only 12 yuan a three-dimensional pore structure of zeolite ring.

β zeolite having high hydrocracking, hydroisomerization catalytic activity and adsorption capacity of linear paraffins, and good resistance to sulfur and nitrogen poisoning. It can be used in the petrochemical industry of benzene with propylene olefin system cumene, cumene metathesis diisopropylbenzene, toluene Isopropylation, aromatics alkylation, transalkylation diisopropylbenzene, propylene ether, methanol aryl structured, propylene oxide and acetic ether of phenol methylation, methylation of aniline, toluene transalkylation preparation of cumene and toluene disproportionation and transalkylation reaction with a catalyst such. β-type USY zeolite used in conjunction with the increase of the octane number of gasoline. In the fine chemical industry, β zeolite has excellent activity and selectivity in the dehydration deamination.

Beta zeolite 25

Item Unit Min Typical Max Analytical Method
Relative crystallinity % 78 80   X-ray diffractometer
Crystal size nm 50 70    
Total specific surface m2/g 500 540   N2 adsorption
Microporous specific surface m2/g 430 460   N2 adsorption
Pore volume ml/g 0.3 0.4   N2 adsorption
silica-alumina ratio / 23 25 27 XRF
Na2O wt%     0.1 Flame photometric analysis
SO42- wt%     0.4 XRF
Cl- wt%     0.2 chemical analysis
L.O.I. wt%     10 Gravimetric analysis
D50 um     7 laster scatter distrioution
D90 um     9 laster scatter distrioution

 

Beta zeolite 28

Item Unit Min Typical Max Analytical Method
Relative crystallinity % 82 86   X-ray diffractometer
Crystal size nm 200 300    
Total specific surface m2/g 580 600   N2 adsorption
Microporous specific surface m2/g 460 480   N2 adsorption
Pore volume ml/g 0.35 0.37   N2 adsorption
silica-alumina ratio / 26 28 30 XRF
Na2O wt%     0.05 Flame photometric analysis
SO42- wt%     0.4 XRF
Cl- wt%     0.2 chemical analysis
L.O.I. wt%     10 Gravimetric analysis
D50 um     7 laster scatter distrioution
D90 um     9 laster scatter distrioution

Beta zeolite 30

Item Unit Min Typical Max Analytical Method
Relative crystallinity % 78 80   X-ray diffractometer
Crystal size nm 50 70    
Total specific surface m2/g 500 540   N2 adsorption
Microporous specific surface m2/g 430 460   N2 adsorption
Pore volume ml/g 0.3 0.4   N2 adsorption
silica-alumina ratio / 28 30 32 XRF
Na2O wt%     0.1 Flame photometric analysis
SO42- wt%     0.4 XRF
Cl- wt%     0.2 chemical analysis
L.O.I. wt%     10 Gravimetric analysis
D50 um     7 laster scatter distrioution
D90 um     9 laster scatter distrioution

Beta zeolite 50

Item Unit Min Typical Max Analytical Method
Relative crystallinity % 78 80   X-ray diffractometer
Crystal size nm 50 70    
Total specific surface m2/g 500 540   N2 adsorption
Microporous specific surface m2/g 430 460   N2 adsorption
Pore volume ml/g 0.3 0.4   N2 adsorption
silica-alumina ratio / 48 50 52 XRF
Na2O wt%     0.1 Flame photometric analysis
SO42- wt%     0.4 XRF
Cl- wt%     0.2 chemical analysis
L.O.I. wt%     10 Gravimetric analysis
D50 um     7 laster scatter distrioution
D90 um     9 laster scatter distrioution

 

Zeolite beta is used in isomerization of waxes, and Friedel Crafts reactions (alkylation and acylation)Zeolite β, hydrogen is used as a molecular sieve, filter, adsorbent, catalyst, drying agent, cation exchanger, dispersing agent and detergent builder. It serves as an acid catalyst and utilized as an alternative to the known methods for protection of alcohols as tetrahydropyranyl ethers and the deprotection of tetrahydropyranyl ethers. It is also used in the stereoselective Meerwein-Ponndorf-Verley reduction of ketones. Further, it is used as an efficient and recyclable catalyst for the tetrahydropyranylation of alcohols and phenols

 

We can produce beta zeolite according customers demand.

 

 

Our zeoite and catalyst factory are in follow.

The fixed-bed catalyst production project covers an area of about 5,000 square meters and a building area of 2,000 square meters. It is fully equipped with public works and has more than 40 sets of catalyst production equipment. It has a complete fixed-bed catalyst production system, and the production units that can be carried out mainly include: pretreatment of catalyst raw powder, impregnation, molding, drying/roasting, screening and environmental protection treatment, etc., which can meet the production of various fixed-bed catalysts.

 

 

 

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Contact Details
Catalyst Zeolite CO.,LTD

Contact Person: Mr. Kevin

Tel: +8615666538082

Fax: 86-533-52065599-2

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