Alumina Catalyst
SKU
RXSOL-24-1905-125
Product Alias::
Supply Location::
Locations
Alumina Catalyst manufacturer supplier distributor in Mumbai, Kandla, Kolkata, Vizag, Chennai, India, Fujairah, Dubai, Sharjah, UAE, Gulf, Middle East, Muscat Oman, Kenya Africa. Get the best quality of Alumina Catalyst at a competitive price from us. We have ready stock of Alumina Catalyst in India, UAE Gulf, Oman, Kenya Africa. Contact us for bulk as well as small orders.
RXMARINE CHEMICAL TAG::
Category
Variations
Description::
Short Description
Activated Alumina Powder Absorbent and Catalyst
Application::
Technical Specifications::
Specification :-
Particle Size mm |
AGC-I (4-6) | AGC-II (4-6 ) |
| Specific surface area m2/g | 200 min | 280-400min |
| Pore Volume cm3/g | 0.4min | 0.45min |
| Bulk Density g/cm2 | 0.65min | 0.72min |
| Crushing Strength N/sphere | 100min | 110min |
| Abrasion rate % | 0.5 max | 0.5 max |
| Na2O3% | 0.3max | 0.25max |
| A12O3 | 94.0min |
3 Ǻ. According to the industrial application specialties. We endueourproductswiththecharactersofhigheradsorption speed, stronger crushing and anticontaminativeresistance, more cyclic times and longer work-span. All these advantages have made it come to be the most essential and necessary desiccant in the fields of the deep drying, refinery, polymerization for cracked gases, ethylene, propylene and any other non-acidic gases or liquids in petroleum and chemical industrial.The pore size of 3A molecular sieve is 3Ǻ. It does not adsorb any molecular larger than
3 Ǻ. According to the industrial application specialties. We endueourproductswiththecharactersofhigheradsorption speed, stronger crushing and anticontaminativeresistance, more cyclic times and longer work-span. All these advantages have made it come to be the most essential and necessary desiccant in the fields of the deep drying, refinery, polymerization for cracked gases, ethylene, propylene and any other non-acidic gases or liquids in petroleum and chemical industrial.
| Phone | +91 22 65113333 / 5555 / 9999 / 27611360 |
| Fax | +91 22 2781 1318 :::AOH :0091 9821214367 |
|
mail@rxmarine.com |
| Phone | +91 22 65113333 / 5555 / 9999 / 27611360 | |
| Fax | +91 22 2781 1318 :::AOH :0091 9821214367 | |
|
mail@rxmarine.com |
3 Ǻ. According to the industrial application specialties. We endueourproductswiththecharactersofhigheradsorption speed, stronger crushing and anticontaminativeresistance, more cyclic times and longer work-span. All these advantages have made it come to be the most essential and necessary desiccant in the fields of the deep drying, refinery, polymerization for cracked gases, ethylene, propylene and any other non-acidic gases or liquids in petroleum and chemical industrial.The pore size of 3A molecular sieve is 3Ǻ. It does not adsorb any molecular larger than
3 Ǻ. According to the industrial application specialties. We endueourproductswiththecharactersofhigheradsorption speed, stronger crushing and anticontaminativeresistance, more cyclic times and longer work-span. All these advantages have made it come to be the most essential and necessary desiccant in the fields of the deep drying, refinery, polymerization for cracked gases, ethylene, propylene and any other non-acidic gases or liquids in petroleum and chemical industrial.
| Phone | +91 22 65113333 / 5555 / 9999 / 27611360 |
| Fax | +91 22 2781 1318 :::AOH :0091 9821214367 |
|
mail@rxmarine.com |
Dose::
Product remark::
Industrial Usages::
Useful Area::
Related Information::
Note
Precautions:
1. In the operation process, prevent the bed layer of the reactor from high temperature, carbon deposition and sulfation, start or stop working carefully, so as to keep the high activity of catalyst and prolong the service life of catalyst.
2. The oxygen and sulfur dioxide content in the air flow entered into the reactor should be decreased as much as possible, so as to prevent the catalyst from sulfation poisoning. At normal operation H2S/SO2(molecular rate)should be about 2.
3. Under the air flow containing sulfur steam, the temperature in all part of the bed layer of the reactor should be less than the dew point of sulfur, so as to avoid the sulfur deposition on catalyst and plugging off the pipeline. Any wrong operation of raise temperature or drop temperature should be avoided.
4. Amines, hydrocarbons and ammonium etc. should be avoided into reactor, so as to prevent the catalyst from carbon deposition, plugging the pipeline and forming poisonous such as ammonium sulfate etc.