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HISTORY
PRODUCTS
CYCLONES
INDUSTRIAL
FCC
HANGER SYSTEMS
REACTOR AND REGENERATOR CYCLONES
3RD & 4TH STAGE
OTHER PRODUCTS
PETROCHEMICAL
MULTICELL
CYCLONE QUESTIONNAIRE
AIR CLASSIFIERS
OPERATING PRINCIPLES AND EFFICIENCY
BAG FILTERS
ENGINEERING SERVICES
NEWS
CONTACT
Cyclone Questionaire
Step 1 of 3
33%
In the following tables, please complete as much information as possible. The more information we have to complete the sizing the more accurate the sizing will be. If you are missing some information, that is acceptable. If it is critical information we will contact you to request the information that we need. Please note that all information given to Van Tongeren for sizing purposes will be kept confidential.
I have data for:
Select all that apply.
Design Case
Turn Down Case
Maximum Case
Minimum Case
Case 5
Case 6
I'm looking to replace a:
Select all that apply
Primary Regenerator Cyclone
Secondary Regenerator Cyclone
Design Case
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Turn Down Case
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Maximum Case
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Minimum Case
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Case 5
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Case 6
Number of Cyclones in service
Gas Volume, actual cubic feet per second (acfs)
Solids loading lb/ft3
APS of E-Cat
Gas temperature, deg F
Gas viscosity, centipoise
Dust particle density, g/cc
Gas operating pressure, psig
Molecular weight of gas
Gas density, lb/cf
Top tangent line to bed level, inches
Bulk Density, #/CF
Bed density, lb/ft3
Dipleg density, lb/ft3
Primary Cyclone
Section Break
Number of Cyclones
Cyclone Barrel Diameter, in. I.D. (Db)
Inlet Duct Height (Hi), inches
Inlet Duct Width (Wi), inches
Gas Outlet Tube Diameter (Dgo), inches
Barrel Height (Lb), inches
Cone Height (Lc), inches
Hopper Height (Lh), inches
Cyclone Barrel Cone Outlet Diameter (Dc), inches I.D.
Cyclone Length (L) I.S. Roof to top of Dipleg, inches
I.S. Roof to Vortex (Lv), inches
Dipleg Diameter (Ddg), inches I.D.
Gas Outlet Tube Penetration (Lgo), % of Inlet Duct Height
Vortex Clearance above top of Dipleg (Vc), inches
Available Dipleg Length, in
Total Inlet Area (Ai), ft2
Total Outlet Area (Ao), ft2
Total Barrel Area (Ab), ft2
Total Dipleg Area (Adg), ft2
Ao/Ai
Ratio: Barrel Area/Inlet Area
Cyclone Length / Barrel Diameter (L/Db)
I.S. Roof to Vortex / Barrel Diameter (Lv/Db)
Cyclone Inlet Height / Width Ratio (Hi/Wi)
Vessel Diameter, in
Design Temperature, °F
Barometric pressure, psia
Section Break
Section Break
Section Break
Secondary Cyclone
Section Break
Section Break
Number of Cyclones
Cyclone Barrel Diameter, in. I.D. (Db)
Inlet Duct Height (Hi), inches
Inlet Duct Width (Wi), inches
Gas Outlet Tube Diameter (Dgo), inches
Barrel Height (Lb), inches
Cone Height (Lc), inches
Hopper Height (Lh), inches
Cyclone Barrel Cone Outlet Diameter (Dc), inches I.D.
Cyclone Length (L) I.S. Roof to top of Dipleg, inches
I.S. Roof to Vortex (Lv), inches
Dipleg Diameter (Ddg), inches I.D.
Gas Outlet Tube Penetration (Lgo), % of Inlet Duct Height
Vortex Clearance above top of Dipleg (Vc), inches
Available Dipleg Length, in
Total Inlet Area (Ai), ft2
Total Outlet Area (Ao), ft2
Total Barrel Area (Ab), ft2
Total Dipleg Area (Adg), ft2
Ao/Ai
Ratio: Barrel Area/Inlet Area
Cyclone Length / Barrel Diameter (L/Db)
I.S. Roof to Vortex / Barrel Diameter (Lv/Db)
Cyclone Inlet Height / Width Ratio (Hi/Wi)
Vessel Diameter, in
Design Temperature, °F
Barometric pressure, psia
Section Break
Section Break
Section Break
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