ZSM-5 Series Zeolite (MFI) Powder
Hydrothermal method, MFI
Product Detail
ACS Material is excited to offer our customers a new class of shape-selective catalysts distinguished by unique channel structures. ZSM-5 is the trade name for zeolite socony mobil-5, a pentasil aluminosilicate zeolite. Each pentasil unit is made up of eight 5-membered rings, and individual pentasil units are connected to each other by oxygen bridges to form regular corrugate sheets with 10-ring holes. The channel structure and acidity of ZSM-5 lends itself to a number of industrial uses such as acid-catalyzed reactions and as a support material for catalysis.
CAS No.: 1318-02-1
| Preparation Method | Hydrothermal Method |
| Linear Formula | (SiO2)x(Al2O3)y |
| Pore Size |
~5A |
| Type |
Form |
SiO2/Al2O3 Molar Ratio |
Average Particle Size |
BET Surface Area m2/g |
Na2O (%) |
Adsorption (wt%) |
| P-25 | H+ | ~25 |
2-5μm |
>=340 | -- |
-- |
| P-38 | H+ | ~38 |
2μm |
>380 | <0.2 |
≥9.5 |
| P-38-Na | Na+ | ~38 |
2μm |
>380 | -- |
≥9.5 |
| P-117 | H+ | ~117 |
2μm |
>380 | <0.2 |
≥9.5 |
| P-360 | H+ | 360 |
2μm |
>380 | <0.1 |
≥9.5 |
ACS Material provides high-quality ZSM-5 Series Zeolite (MFI) powder at an excellent price accompanied by our outstanding customer service. Our ZSM-5 powder is calcined and ready to use directly. It can be reactivated by calcination at 550 °C in air. Increase the temperature by a step of 10°C per minute and heat it at 550°C for about 5-6 hours.
Industrial ZSM-5 MFI Zeolite Powder Available Now!
| Type | SAR (SiO2/Al2O3) |
Na2O (wt%) |
Morphology | Particle Size D50 (µm) |
BET Surface Area (m2/g) |
Relative Crystallinity (%) | Applications | Calcined or Not Calcined |
| P-1500s | >1500 | <0.1 | Single crystals | <15 | >350 | >90 | Adsorbent, Catalyst, VOC, Isomers Separation | Calcined |
| P-1500p | >1500 | <0.1 | Single crystals | <15 | >350 | >90 | Hydropbolic Adsorbent, Catalyst, Isomers Separation | Calcined |
| P-1200s | 900-1500 | <0.1 | Single crystals | <15 | >350 | >90 | Catalyst, Adsorbent, VOC | Calcined |
| P-800s | 700-900 | <0.1 | Single crystals | <15 | >350 | >90 | Catalyst, Adsorbent, VOC | Not Calcined |
| P-600s | 500-700 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, Adsorbent, VOC | Not Calcined |
| P-400s | 350-450 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, Adsorbent, VOC, MTP/MTPG | Not Calcined |
| P-300s | 250-350 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, Adsorbent, VOC, FCC ZSM-5 Additive for Octane Enhancement, | Not Calcined |
| P-200s | 160-230 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, catalyst carrier, Methanol and toluene alkylation | Not Calcined |
| P-150s | 140-160 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, catalyst carrier | Not Calcined |
| P-120s | 110-130 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, catalyst carrier | Not Calcined |
|
P-100s (Discontinued) |
90-110 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, catalyst carrier | Not Calcined |
|
P-80s (Discontinued) |
70-90 | <0.1 | Single crystals | <10 | >350 | >90 | Catalyst, catalyst carrier | Not Calcined |
|
P-60n (Discontinued) |
50-70 | <0.1 | Aggregates of nano crystals | <10 | >350 | >90 | Catalyst, catalyst carrier, MTG | Not Calcined |
| P-30n | 25-35 | <0.1 | Aggregates of nano crystals | <5 | >350 | >90 |
Catalyst, catalyst carrier, MTA/FCC ZSM-5 Additive for C3=, DewaxingAlkylation, Dealkylation, Oligomerization |
Not Calcined |
|
P-30s (Discontinued) |
25-35 | <0.1 | Single crystals | <5 | >350 | >90 |
Catalyst, catalyst carrier, MTA/FCC ZSM-5 Additive for C3=, DewaxingAlkylation, Dealkylation, Oligomerization |
Not Calcined |
| P-20n | 18-25 | <0.1 | Aggregates of nano crystals | <5 | >350 | >90 | Catalyst, catalyst carrier, MTA | Not Calcined |
|
P-20s (Discontinued) |
18-25 | <0.1 | Single crystals | <5 | >350 | >90 | Catalyst, catalyst carrier, MTA | Not Calcined |
For the products listed as NOT calcined, heat at 500-530°C for at least 3 hours. Time should be adjusted based on the total quantity of the product. Please contact us for calcination services, pricing and lead time.
Please contact us for bulk pricing.
Disclaimer: ACS Material LLC believes that the information on our website is accurate and represents the best and most current information available to us. ACS Material makes no representations or warranties either express or implied, regarding the suitability of the material for any purpose or the accuracy of the information listed here. Accordingly, ACS Material will not be responsible for damages resulting from use of or reliance upon this information.
FAQ
1. What the bulk density of Nano H-ZSM-5, Powder, Molar 52？
A: The bulk density of Nano H-ZSM-5, Powder, Molar 52 is 0.187g/mL.
2. What the bulk density of ZSM-5 Series Zeolite Powder, P-38？
A: The bulk density of ZSM-5 Series Zeolite Powder, P-38 is 0.356g/mL.
3. What the bulk density of ZSM-5 Series Zeolite Powder, P-300s？
A: The bulk density of ZSM-5 Series Zeolite Powder, P-300s is about 0.3g/mL.
4. What is the morphology of ZSM-5 Series Zeolite Powder, P-38？
A: The morphology of ZSM-5 Series Zeolite Powder, P-38 is polycrystal. It is white powder.
Research Citations of ACS Material Products
- Chifiriuc, M. Carmen, et al. “Influence of hybrid inorganic/Organic mesoporous and nanostructured materials on the cephalosporins’ efficacy on different bacterial strains.” IET Nanobiotechnology, vol. 6, no. 4, Jan. 2012, pp. 156–161., doi:10.1049/iet-nbt.2011.0066.
- Zhu, Bo, et al. “Temperature and Pressure Effects of Desalination Using a MFI-Type Zeolite Membrane.” Membranes, vol. 3, no. 3, 2013, pp. 155–168., doi:10.3390/membranes3030155.
- Wagner, Jonathan L., et al. “Catalytic cracking of sterol-Rich yeast lipid.” Fuel, vol. 130, 2014, pp. 315–323., doi:10.1016/j.fuel.2014.04.048.
- Lazdovica, K., et al. “Catalytic pyrolysis of wheat bran for hydrocarbons production in the presence of zeolites and noble-Metals by using TGA-FTIR method.” Bioresource Technology, vol. 207, 2016, pp. 126–133., doi:10.1016/j.biortech.2016.01.117.
- Lazdovica, K., et al. “Comparative wheat straw catalytic pyrolysis in the presence of zeolites, Pt/C, and Pd/C by using TGA-FTIR method.” Fuel Processing Technology, vol. 138, 2015, pp. 645–653., doi:10.1016/j.fuproc.2015.07.005.
- Bianchini, Emma, et al. “Pyrolysis of spirulina and zeolite cracking over HZSM-5. An analytical investigation on the chemical route of bio-Oil from cultivation to combustion.” Journal of Analytical and Applied Pyrolysis, vol. 126, 2017, pp. 230–238., doi:10.1016/j.jaap.2017.06.004.
- Zhu, Bo, et al. “A method for defect repair of MFI-Type zeolite membranes by multivalent ion infiltration.” Microporous and Mesoporous Materials, vol. 237, 2017, pp. 140–150., doi:10.1016/j.micromeso.2016.09.011.
- Williamsona, Philip A., Pavithra M. Shanthib, Ramalinga Kurubac, Prashanth J. Hanumanthac, and Prashant N. Kumtaa. "The Effect of Zeolite Additives on Li-ion Conductivity of Gel-Polymer Electrolytes." Highlighting Undergraduate Research at the University of Pittsburgh Swanson School of Engineering (2018): 87.
- Muñoz-Olasagasti, M., A. Sañudo-Mena, J. A. Cecilia, M. López Granados, P. Maireles-Torres, and R. Mariscal. "Direct Conversion of Levulinic Acid into Valeric Biofuels Using Pd Supported Over Zeolites as Catalysts." Topics in Catalysis: 1-10.
- Schulzke, Tim, S. Conrad, B. Shumeiko, M. Auersvald, David Kubička, and L. F. J. M. Raymakers. "Fuels from Reliable Bio-based Refinery Intermediates: BioMates." Waste and Biomass Valorization (2019): 1-20.
- Shehab, Amal. "The Role of Carbon in the Catalytic Isomerisation-Cracking of n-Alkanes." PhD diss., University of Sheffield, 2018.