3a molecular sieve price mathanol drying 3a 4a 5a 13x synthetic zeolite molecular sieve for co2 remove
Product Description
3a Molecular Sieve price mathanol drying 3a 4a 5a 13x synthetic zeolite Molecular Sieve for co2 remove
Product Description
Guangdong Xintao specialized in the production of 3A,4A,5A,13X,13XAPG,Insulating Glass Molecular Sieve, which can be used in different industries based on their adsorbent requirements.
3A Molecular Sieve
| Nominal pore diameter | 3 angstroms | |||
| Shape | Sphere | Pellet | ||
| Diameter (mm) | 1.7-2.5 (8*12mesh) | 3.0-5.0 (4*8mesh) | 1.6 (1/16 inch) | 3.2 (1/8 inch) |
| Size ratio up to grade(%) | ≥98 | ≥98 | ≥96 | ≥96 |
| Bulk density (g/ml) | ≥0.70 | ≥0.70 | ≥0.68 | ≥0.68 |
| Wear ratio (%) | ≤0.20 | ≤0.20 | ≤0.40 | ≤0.40 |
| Crushing strength (N) | ≥35/piece | ≥85/piece | ≥30/piece | ≥50/piece |
| Static H2O adsorption(%) | ≥21 | ≥21 | ≥21 | ≥21 |
| Dynamic capacity (%) | ≥20 | ≥20 | ≥20 | ≥20 |
| Ethylene adsorption (‰) | ≤3.0 | ≤3.0 | ≤3.0 | ≤3.0 |
| Water content (%) | ≤1.5 | ≤1.5 | ≤1.5 | ≤1.5 |
| Typical Application | a) Drying of unsaturated hydrocarbons (e.g. ethylene, propylene, butadien) b) Cracked Gas Drying c) Drying of natural gas, if COS minimization is essential, or a minimum co-adsorption of hydrocarbons is required. d) Drying of highly polar compounds, such as methanol and ethanol e) Drying of liquid alcohol,CNG. f) Static, (non-regenerative) dehydration of insulating glass units, whether air filled or gas-filled. g) Drying of CNG. | |||
4A Molecular Sieve
| Nominal pore diameter | 4 angstroms | |||
| Shape | Sphere | Pellet | ||
| Diameter (mm) | 1.7-2.5 (8*12mesh) | 3.0-5.0 (4*8mesh) | 1.6 (1/16 inch) | 3.2 (1/8 inch) |
| Size ratio up to grade(%) | ≥98 | ≥98 | ≥96 | ≥96 |
| Bulk density (g/ml) | ≥0.70 | ≥0.70 | ≥0.68 | ≥0.68 |
| Wear ratio (%) | ≤0.20 | ≤0.20 | ≤0.40 | ≤0.40 |
| Crushing strength (N) | ≥35/piece | ≥85/piece | ≥30/piece | ≥70/piece |
| Static H2O adsorption(%) | ≥21.5 | ≥21.5 | ≥21.5 | ≥21.5 |
| Static methanol adsorption (%) | ≥15 | ≥15 | ≥15 | ≥15 |
| Water content (%) | ≤1.5 | ≤1.5 | ≤1.5 | ≤1.5 |
| Typical Application | a) Drying and removing of CO2 from natural gas, LPG, air, inert and atmospheric gases, etc. b) Removal of hydrocarbons, ammonia and methanol from gas streams (ammonia syn gas treating) c) Special types are used in the air break units of buses, trucks and locomotives. d) Packed in small bags, it may be used simply as a packaging desiccant. | |||
5A Molecular Sieve
| Nominal pore diameter | 5 angstroms | |||
| Shape | Sphere | Pellet | ||
| Diameter (mm) | 1.7-2.5 (8*12mesh) | 3.0-5.0 (4*8mesh) | 1.6 (1/16 inch) | 3.2 (1/8 inch) |
| Size ratio up to grade(%) | ≥98 | ≥98 | ≥96 | ≥96 |
| Bulk density (g/ml) | ≥0.70 | ≥0.70 | ≥0.68 | ≥0.68 |
| Wear ratio (%) | ≤0.20 | ≤0.20 | ≤0.40 | ≤0.40 |
| Crushing strength (N) | ≥35/piece | ≥85/piece | ≥30/piece | ≥75/piece |
| Static H2O adsorption(%) | ≥21 | ≥21 | ≥21 | ≥21 |
| Static methanol adsorption (%) | ≥12 | ≥12 | ≥12 | ≥12 |
| Water content (%) | ≤1.5 | ≤1.5 | ≤1.5 | ≤1.5 |
| Typical Application | a) The strong ionic forces of the divalent calcium ion makes it an excellent adsorbent to remove water, CO2, H2S from sour natural gas streams, while mini missing COS formation. Light mercaptans are also adsorbed. b) Separation of normal- and iso paraffin’s. | |||
13X Molecular Sieve
| Nominal pore diameter | 10 angstroms | |||
| Shape | Sphere | Pellet | ||
| Diameter (mm) | 1.7-2.5 (8*12mesh) | 3.0-5.0 (4*8 mesh) | 1.6 (1/16 inch) | 3.2 (1/8 inch) |
| Size ratio up to grade (%) | ≥98 | ≥98 | ≥96 | ≥96 |
| Bulk density (g/ml) | ≥0.68 | ≥0.68 | ≥0.65 | ≥0.65 |
| Wear ratio (%) | ≤0.20 | ≤0.20 | ≤0.40 | ≤0.40 |
| Crushing strength (N) | ≥30/piece | ≥85/piece | ≥25/piece | ≥65/piece |
| Static H2O adsorption (%) | ≥25 | ≥25 | ≥25 | ≥25 |
| Static CO2 adsorption (%) | ≥17 | ≥17 | ≥17 | ≥17 |
| Water content (%) | ≤1.5 | ≤1.5 | ≤1.5 | ≤1.5 |
| Typical Application | a) Removal of CO2 and moisture from air (air pre-purification) and other gases. b) Separation of enriched oxygen from air. c) Removal of n-chained compositions from aromatics. d) Removal of R-SH and H2S from hydrocarbon liquid streams (LPG, butane etc.) e) Catalyst protection, removal of oxygenates from hydrocarbons (olefin streams). f) Production of bulk oxygen in PSA units. | |||
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