MOQ | 1000 liters |
Port | Qingdao of China |
Packaging | 200 liters/ steel drum |
Lead Time | 7 to 10 days |
Color | yellow or red brown |
Vanadium pentoxide series of sulfuric acid catalysts could be used in the process of sulfuric acid production, to be more specific, is the process of SO2+I/2O2---SO3. With the help of Vanadium Catalyst, the rate of conversion can be improved greatly. It can guarantee the air speed of operation to add 10-20% more when using type star ring catalysts or ring catalysts.
Vanadium catalyst can be applied in many fields, such as, sulfur-based acid production, pyrite-based acid production, nonferrous smelting gas-based acid production, gypsum-based acid production etc.
1: Broad Temperature Type of Sulfuric Acid Catalyst: S101.
1) Type S101:
There are four products of type S101, in details, they are S101 (Cylinder); S101-H (Ring); S101-MH (Star ring); S101-YH (Three-rib cylinder)
Type S101 Catalyst is a medium broad temperature vanadium catalyst which promotes the oxidation from SO2 to SO3, and it is developed by China. With 20 years of manufacturing S101 catalyst, it has reached the international advanced level. Due to its high-quality and steady performance,
The advantages of S101 are as
listed.
Wide applicability, broad range of temperature, high conversion, and high mechanical strength etc. Ring or plum blossom shaped catalysts have solved some problems that cylinder-shaped catalyst encountered; namely, they are small pellets, high pressure drop and high energy consumption, bad resistance of dust accumulation.
Main Physical Property
Type Item |
S101 |
S101-H |
S101-MH |
S101-YH |
|
Physical Property |
Shape |
Cylinder |
Ring |
Star ring |
Three-rib cylinder |
Color |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
|
Diameter(mm) |
Φ 4.5-5.5 |
OD:9-11 ID:3-4 |
OD:12-13 ID: 3-4 |
Φ 4.5-5.5 |
Remark: The diameter and length mentioned above can be designed according to customer’s request.
Main Technical Index (HG/T2086-2013 Standards)
Item Type |
S101 |
S101-H |
S101-MH |
S101-YH |
Activity |
≥81 |
≥86 |
≥86 |
≥86 |
Crushing Strength |
≥70 |
≥40 |
≥40 |
≥70 |
Attrition loss |
≤5 |
≤5 |
≤5 |
≤5 |
V2O5% |
≥7.5 |
≥7.5 |
≥7.5 |
≥7.5 |
Bulk Density |
0.6-0.65 |
0.52-0.56 |
0.5-0.55 |
0.58-0.6 |
2: Low Temperature Type Sulfuric Acid Catalyst: S108.
Type S108: S108 Cylinder; S108-H (Ring); S108-MH (Star ring); S108-YH (Three-rib cylinder)
Type S108 Series sulfuric acid catalysts are invented in early 80s’ by China. The advantages of them are outstanding. In general, they are low ignition temperature, high activity in low temperature, high-resistant crushed strength etc. If can be used together with medium temperature type catalyst, such as, S101, you can make more profits; for instance, high conversion, and lowering environmental pollution.
Main Physical Property
Type Item |
S108 |
S108-H |
S108-MH |
S108-YH |
|
Physical Property |
Shape |
Cylinder |
Ring |
Star ring |
Three-rib cylinder |
Color |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
|
Diameter |
Φ 4.5-5.5 |
OD:9-11 ID:3-4 |
OD:12-13 ID: 3-4 |
Φ 4.5-5.5 |
Main Technical Index (HG/T2086-2013 Standards)
Type Item |
S108 |
S108-H |
S108-MH |
S108-YH |
Activity |
≥35 |
≥42 |
≥42 |
≥42 |
Crushing Strength |
≥60 |
≥40 |
≥40 |
≥60 |
Attrition loss |
≤5 |
≤5 |
≤5 |
≤5 |
V2O5% |
≥6.2 |
≥6.3 |
≥6.3 |
≥6.3 |
Bulk Density |
0.62-0.67 |
0.52-0.56 |
0.5-0.55 |
0.58-0.62 |
3: LS112 Type Cesium Catalyst
The characters of this type of catalyst are listed below:
Low ignition temperature; higher activity in low temperature; high-resistant crushed strength, high anti- poison; high anti- pulverization etc.
Main Physical Property
Physical Properties |
Type |
LS112 |
LS112-H |
LS112-MH |
LS112-YH |
Shape |
Cylinder |
Ring |
Star Ring |
Three-rib cylinder |
|
Color |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
Deep yellow or red brown |
|
Diameter (mm) |
4.5-5.5 |
OD:9-11 ID:3-4 |
OD:12-13 ID:3-4 |
4.5-5.5 |
|
Length (mm) |
≥5.5 |
≥10 |
≥10 |
≥5.5 |
|
Bulk density (kg/l) |
0.6-0.66 |
0.50-0.56 |
0.50-0.56 |
0.58-0.62 |
|
Chemical Composition |
V2O5 (%) |
≥5.5 |
≥5.5 |
≥5.5 |
≥5.5 |
Main Technical Index (HG/T2086-2013 Standards)
Type |
LS112 |
LS112-H |
LS112-MH |
LS112-YH |
|
Activity(SO2 conversion rate) (%) |
390℃ |
≥30.0 |
≥42.0 |
≥42.0 |
≥42.0 |
410℃ |
≥52.0 |
≥60.0 |
≥60.0 |
≥60.0 |
|
Crushing strength (N/cm) |
≥60 |
≥40 |
≥40 |
≥60 |
|
Attrition loss rate (%) |
≤5.0 |
≤5.0 |
≤5.0 |
≤5.0 |
Operating Requirements
1). Type S101 series are broad temperature catalysts which suit for every bed of converter.
2). Type S108 is low
temperature catalysts which suit for 1/3 top of the first bed to
decrease inlet operating temperature, and 4th bed, 5th bed to
improve equilibrium conversion and decrease gas
emission.
3). Install the catalyst beginning at the far side of the
converter working back towards the manway. Use the marks on the
converter wall as a guide for leveling the catalyst. Avoid
walking directly on the catalyst. Use plywood sheets or boards
laid on top of the catalyst if access is required across the top
of the bed.
4). New catalyst is easy to get damp, so it is better to choose
fine days to sift it and load it. Time that catalyst is exposed
in air should be as short as possible.
5). Catalysts used in low temperature beds can be moved to high
temperature beds, but contrarily it can’t be loaded. New
catalysts should be loaded in the surface of each bed, and
separated from used catalysts with stainless steel nets.
6). It should inspect the pressure drop of each bed before
repairing, and inspect the activity of catalysts in each bed
before loading, so that supply some information for screening,
loading or removing.