Skip to main content
Email :rxmarinechemical@gmail.com
Contact: 91 08069976670,
91 08069976671 , 91 08069976672

Catalyst Active Aluminium Oxide

Why Choose RX Marine International

Experience

30+ Years of Excellence

Proven industry leadership and chemical innovation since 1990.

Global Reach

Global Reach

Servicing clients in 35+ countries with reliable logistics.

Formulation

Advanced Formulation

High-performance chemicals built on cutting-edge R&D.

Fast Delivery

Fast Delivery

Ready stock and express fulfillment across regions.

Book a FREE call with our Technical Expert

 
 

Stock Points

Fully equipped factories at strategic locations:

Mumbai

Gandhidham

Kolkata

Vizag

Chennai

Dubai – UAE

Muscat – OMAN

 

Related Post

Catalyst Active Aluminium Oxide

SKU:
SKU
RXSOL-24-1905-225
Product Category:
Short Description
Short Description
Catalyst Active Aluminium Oxide
Product Description
This product is  γ-form white spheric  active aluminium oxide, which is used for the recovery of sulfur from acidic gas containing sulfur by liquefaction in petrochemical industry. The product is prepared from intermediate raw materials of quick dehydration process production. It has the feature of high crushing strength, low adsorption rate, good activity, long period of service life, good physic-chemical properties and high catalytic activity etc. The performances of the product such as hydrolytic activity of claus, hydrolytic activity to organics sulfur, resistance to sulfation, heat stability and chemical composition can reach the level of CR- form aluminium oxide catalyst made by France.
 
This Product is suitable for the sulfur recovery in the refined oil plant, natural gas plant, coal gas.
Application
Application Contentz[wt%]
Hydrodesul Furtization a CoO   (3-5)
MoO3   (13-21)
Al2O3   (balance)
(extrudates)
b NiO   (3-6)
MoO3  (13-21)
Al2O3   (balance)
Sulfur Removal a ZnO   90
Blinder   (Balance)
b CuO    6
Activated Carbon    (Balance)
(granules)
Chlorline Removal a Na2O  ( 7-10)
Al2O3    (balance)
(Spheres)
Steam reforming a NiO   -56
MgO   -12
SiO2  -10
Al2O3   (balance)
(tablet)
b NiO   (14-25)
K2O   (1-8.5)
CaAI12O19/@AI2O3  (balance)
c NiO   (12-14)
AI2O3   (balance)
High temperature CO converstaion a Fe2O3   -89
Cr2O3   -9
CuO   -2
(tablet)
Low temperature CO converstaion a CuO   (38-57 )
ZnO   (31-42 )
AI2O3   (10-12)
 
Note
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.
Product Remark
Remarks
Application Content (wt%)
Medium temperature CO Conversion a CuO    -30
ZnO    -60
Al2O3    -10
Sour Gas Shift   CoO    -3.5
MoO3   -14
AI2O3   (balance)
Ammonia
Synthesis
a Fe 78
Fe2O3+Feo    -10
b Fe2O3+FeO    -92
Methanol 
Synthesis
a CuO+ZnO+AI2O3
Methanol Reforming a CuO    -32
ZnO    -66
  CuO    -23
Zno    -11
AI2O3    -8
Ammonia Dissociation a NiO    -8
MgO (balance)
Production of town gas a NiO    -7
SiO2   -8
AI2O3   (balance)
b Fe2O3   -89
Cr2O3   -9
CuO    -2
Gas Purification a Pt    -0.3
NiO    -4
Al2O3    (balance)
  Pd    (0.2-0.5)
AI2O3    (balance)
MTBE catalyst    
MA catalyst    
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.
Supply Location
Locations

Catalyst Active Aluminium Oxide 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 Catalyst Active Aluminium Oxide at a competitive price from us. We have ready stock of Catalyst Active Aluminium Oxide in India, UAE Gulf, Oman, Kenya Africa. Contact us for bulk as well as small orders.

Product Categories

 
 

Copyright © 2021 Powered By RXMARINE - All Rights Reserved