Send Message
Home ProductsHydrotreating Catalyst

LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates

I'm Online Chat Now

LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates

LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates
LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates

Large Image :  LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates

Product Details:
Place of Origin: china
Brand Name: QD
Certification: ISO9001:2015
Model Number: catalyst
Payment & Shipping Terms:
Minimum Order Quantity: 1 kg
Price: USD3000-30000 /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

LSMAN-1 fixed bed benzene Oxidation to Maleic Anhydride catalyst extrudates

Description
Shape: Black-blue Color Chemical Component:: V2O5, MoO3 And Additives
Particle Size: mm: 7*4*4 Crushing Strength: 10kg
High Light:

10kg catalyst extrudates

,

10kg extrudate catalyst

 

LSMAN-1 fixed-bed benzene Oxidation to Maleic Anhydride catalyst


Product Description:
HTMAN-1 fixed-bed benzene Oxidation to Maleic Anhydride catalyst taking
Mixed oxide in the inert carrier,V2O5 and MoO3as active components,is used
In fixed-bed benzene oxidation to maleic anhydride. The catalyst possesses the
Characteristics of high activity,high intensity,98%-99% conversion rate,good
selectivity and upto 90%-95% yield. The catalyst has been treated with pre-activation
and processing longlife,the started induction period is reduced significantly,
The service life of the product is up to two years or more.
Physical and chemical properties:

items index
Appearance Black-blue color
Bulk density,g/ml 0.75-0.81g/ml
Shape specification,mm Regular hollow ring 7 * 4 * 4
Surface area, ㎡/g >0.1
Chemical composition V2O5, MoO3 and additives
Crushing strength Axial10kg/partical, radial5kg/partical

Reference operating conditions:


Temperature,℃
Initial stage 430-460℃,normal400-430℃
Space velocity,h -1 2000-2500
Benzene concentration 42g-48g /m³good effect, 52g/ /m³can be used
Level of activity Benzene conversion rate 98%-99%

1. Using oil-benzene is best to the catalyst,because thiophene and total sulfur in benzene will lower the catalyst activity of operating,after the device is running normally,superfine coking benzene can be used.
2. In the process, the hot-spot temperature should not exceed 460℃.
3. The catalyst’s space velocity within 2000-2500 h -1 has the best effect.of course,if the space velocity is larger than this,it also works well,since it is the catalyst with high space velocity.
Package and transportation:
During the storage and transportation process, the catalyst is absolute moisture proof,waterproof and it should not exceed 3 months when it is placed in the air. We can flexibly package according to the customers’requires.

Contact Details
CATALYSTS GROUP CO.,LTD

Contact Person: Mr. Kevin

Tel: +8615666538082

Fax: 86-533-52065599-2

Send your inquiry directly to us (0 / 3000)