Generalized Pressure Drop Correlation
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1 Bulletin Description Tellerette Tower Packing Technical Data Index Bulletin No. Generalized Pressure Drop Correlation No. 1 Pressure Drop vs. Gas Rate, #1 Tellerette Tower Packing Liquid Holdup vs. Gas Rate, #1 Tellerette Tower Packing HTU vs. Gas Rate Ammonia-Air-Water, #1 Tellerette Tower Packing Tellerette Performance, Particle Diameter vs. Collection Efficiency No. 2 Type-R Pressure Drop vs. Gas Rate, Air-Water System Liquid Holdup vs. Gas Rate, Air-Water System HTU vs. Gas Ammonia-Air-Water System HTU vs. Gas Ammonia-Air-H 2 SO 4 System HTU vs. Gas Rate, Gaseous HCI-Air-Water System Kga vs. Liquid Rate, CO 2 -Air Caustic System Tellerette Performance, Particle Diameter vs. Collection Efficiency HTU vs. Gas Rate, #2 Type-R Tellerette vs. 2 Intalox Saddles, Ammonia-Air-Water System Pressure Drop vs. Gas Rate, #2 Type-R Tellerette vs. 2 Intalox Saddles, Air-Water System No. 2 Type-K Pressure Drop vs. Gas Rate, Air-Water System Liquid Holdup vs. Gas Rate, Air-Water System HTU vs. Gas Rate, Ammonia-Air-Water System HTU vs. Gas Rate, H 2 S-Air-Caustic/Hypo HTU vs. Gas Rate, SO 2 -Air-Caustic System Pressure Drop vs. Gas Rate, #2 Type-K Tellerette vs #2 Tri-Packs, Air-Water System HTU vs. Gas Rate, #2 Type-K Tellerette vs. #2 Tri-Packs vs. 2 Saddles, Ammonia-Air-Water System HTU vs. Gas Rate, #2 Type-K Tellerette vs. #2 Tri-Packs vs. 3 Lanpac. So 2 -Air-Caustic System Stripping Data, Trichloroethylene-Air-Water Stripping Data, Methylene Chloride-Air-Water Stripping Data, Chloroform-Air-Water No. 3 Type-R Pressure Drop vs. Gas Rate, Air-Water System Liquid Holdup vs. Gas Rate, Air-Water System HTU vs. Gas Rate, Ammonia-Air-Water System No. 3 Type-K Pressure Drop vs. Gas Rate, Air-Water System Liquid Holdup vs. Gas Rate, Air-Water System HTU vs. Gas Rate, HCI-Air-Caustic System
2 00 GENERALIZED PRESSURE DROP CORRELATION THE TELLERETTE INDICATES TOWER PRESSURE DROP INCHES H2O/FT TELLERETTE PACKING FACTORS ARE SHOWN ON THE REVERSE SIDE.100 A B C FLOODING LINE A - APPROX. UPPER LIMIT OF LOADING ZONE B - LINE REPRESENTING MAJORITY OF DATA C - APPROX. LOWER LIMIT OF LOADING ZONE L = liquid mass velocity, lb./(hr) (sq. ft.) G = gas mass velocity, lb./(hr) (sq. ft.) = liquid density, lb./cu. ft. = gas density, lb./cu. ft. g C = gravitational conversion factor, 4.17 x 10 8 (lb. mass) (ft.)/(lb. force) (hr. 2 ) = viscosity of liquid, centipoise = ratio density of water to density of new liquid (dimensionless) F = packing factor L G
3 1 PRESSURE DROP vs. GAS RATE #1 TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING L = 8000 L = 6000 L = 2000 DRY PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.²
4 0 LIQUID HOLDUP vs. GAS RATE #1 TELLERETTE TOWER PACKING AIR-WATER SYSTEM.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING L = 8000 L = 6000 L = PARAMETER: LIQUID RATE - LBS./HR. - FT.²
5 5.0 HTU vs. GAS RATE #1 TELLERETTE TOWER PACKING AMMONIA-AIR-WATER SYSTEM L = 2500 HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 8000 L = 6000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT²
6 TELLERETTE PERFORMANCE PARTICLE DIAMETER VS. COLLECTION EFFICIENCY #1 TELLERETTE PARAMETERS: GAS VELOCITY = 8.0 FT./SEC. PACKING DEPTH = FT. 1 1 PARTICLE DIAMETER (MICRONS) SP. GR. = 6.0 SP. GR. = 5.0 SP. GR. = TOTAL EFFICIENCY - % (BY PARTICLE COUNT)
7 1 PRESSURE DROP vs. GAS RATE #2 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM L = L = L = 8000 L = 6000 L = 2000 PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING DRY PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.²
8 LIQUID HOLDUP vs. GAS RATE #2 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM 0.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING L = L = L = L = 8000 L = 6000 L = PARAMETER: LIQUID RATE - LBS./HR. - FT.²
9 5.0 HTU vs. GAS RATE #2 TYPE-R TELLERETTE TOWER PACKING AMMONIA-AIR-WATER SYSTEM HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 6000 L = 8000 L = TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT²
10 5.0 HTU vs. GAS RATE #2 TYPE-R TELLERETTE PACKING AMMONIA-AIR-SULFURIC ACID SYSTEM HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 2000 L = 6000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 4 FOOT PACKING DEPTH 0.05% AMMONIA GAS CONCENTRATION (BY VOLUME) % H2SO4 LIQUID CONCENTRATION 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT²
11 5.0 HTU vs. GAS RATE TELLERETTE TOWER PACKING GASEOUS HYDROCHLORIC ACID-AIR-WATER SYSTEM HEIGHT OF A TRANSFER UNIT (HTU)og - FEET #3 TYPE-R TELLERETTE PACKING #2 TYPE-R L = 2000 TELLERETTE PACKING #1 TELLERETTE PACKING PARAMETER: LIQUID RATE - 3,000 LBS./HR. - FT.² NOTE: FOR MIST REMOVAL EFFICIENCY REFER TO THE: PARTICLE DIAMETER VS. COLLECTION EFFICIENCY CURVES AND
12 Kga vs. LIQUID RATE TELLERETTE TOWER PACKING CARBON DIOXIDE-AIR-CAUSTIC SYSTEM 5.0 OVERALL MASS TRANSFER COEFFICIENTS (Kga) - LB.MOLES/HR. - FT. 3 - ATM. #1 TELLERETTE PACKING #2 TYPE-K TELLERETTE PACKING #2 TYPE-R TELLERETTE PACKING #3 TYPE-R TELLERETTE PACKING TEST CONDITIONS: 30 INCH COLUMN DIAMETER 8 FOOT PACKING DEPTH 500 LBS./HR. - FT.² GAS RATE 1% CO2 GAS CONCENTRATION 4% NaOH LIQUID CONCENTRATION 25% CARBONATE CONCENTRATION 25ºC/77ºF LIQUID TEMPERATURE LIQUID RATE - LBS./HR. - FT
13 TELLERETTE PERFORMANCE PARTICLE DIAMETER VS. COLLECTION EFFICIENCY #2 TYPE-R TELLERETTE TOWER PACKING PARAMETERS: GAS VELOCITY = 8.0 FT./SEC. PACKING DEPTH = FT. 1 1 PARTICLE DIAMETER (MICRONS) SP. GR. = 6.0 SP. GR. = 5.0 SP. GR. = TOTAL EFFICIENCY - % (BY PARTICLE COUNT)
14 5.0 HTU vs. GAS RATE #2 TYPE-R TELLERETTE vs. 2 INTALOX SADDLE PACKING* AMMONIA-AIR-WATER SYSTEM HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 6000 L = 6000 L = 8000 L = TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT² #2 TYPE-R TELLERETTE 2 PLASTIC INTALOX SADDLES * REGISTERED TRADEMARK OF KOCH-GLITSCH
15 PRESSURE DROP vs. GAS RATE #2 TYPE-R TELLERETTE vs. 2 INTALOX SADDLE PACKING* AIR-WATER SYSTEM 1 L = 5000 PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING L = 5000 DRY PACKING DRY PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.² #2 TYPE-R TELLERETTE #2 PLASTIC INTALOX SADDLES* *REGISTERED TRADEMARK OF KOCH - GLITSCH
16 1 PRESSURE DROP vs. GAS RATE #2 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING L = L = L = 6000 L = 2000 DRY PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.²
17 0 LIQUID HOLDUP vs. GAS RATE #2 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING L = L = L = 8000 L = 6000 L = PARAMETER: LIQUID RATE - LBS./HR. - FT.²
18 HTU vs. GAS RATE #2 TYPE-K TELLERETTE TOWER PACKING AMMONIA-AIR-WATER SYSTEM 5.0 HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 8000 L = 6000 L = 2000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT²
19 5.0 HTU vs. GAS RATE #2 TYPE-K TELLERETTE TOWER PACKING HYDROGEN SULFIDE-AIR-CAUSTIC/HYPO HEIGHT OF A TRANSFER UNIT (HTU)og - FEET TEST CONDITIONS: INLET CONCENTRATION = ppm HYDROGEN SULFIDE SODIUM HYDROXIDE =.0004% BY WEIGHT SODIUM HYPOCHLORITE = 0.25% BY WEIGHT LIQUID RATE = 3000 LBS./HR. FT.²
20 5.0 HTU vs. GAS RATE #2 TYPE-K TELLERETTE PACKING SULFUR DIOXIDE-AIR-CAUSTIC HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 2000 L = 3000 L = 6000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH SO2 GAS INLET CONCENTRATION ppmv NaOH ph > 8 LIQUID TEMPERATURE 50º TO 75º F. LIQUID RATE L = LBS./HR. - FT.²
21 1 PRESSURE DROP vs. GAS RATE #2 TYPE-K TELLERETTE vs. #2 TRI-PACKS * AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.² #2 TYPE-K TELLERETTE #2 TRI-PACKS * *REGISTERED TRADEMARK OF JAEGER PRODUCTS, INC
22 5.0 HTU vs. GAS RATE #2 TYPE-K TELLERETTE vs. #2 TRI-PACKS vs. 2 SADDLE PACKING AMMONIA-AIR-WATER SYSTEM HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = 6000 L = 8000 L = 8000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT² #2 TYPE-K TELLERETTE 2 PLASTIC SADDLES #2 TRI-PACKS * * TRADEMARK OF JAEGER PRODUCTS, INC
23 5.0 HTU vs. GAS RATE #2 TYPE-K TELLERETTE vs. #2 (3 ) TRI-PACKS * vs. 3 LANPAC ** PACKING SULFUR DIOXIDE-AIR-CAUSTIC HEIGHT OF A TRANSFER UNIT (HTU)og - FEET LANPAC ** PACKING #2 (3 ) TRI-PACKS * PACKING #2 TYPE-K TELLERETTE PACKING TEST CONDITIONS: 30 INCH DIAMETER COLUMN 4 FOOT PACKING DEPTH SO2 GAS INLET CONCENTRATION ppmv NaOH ph > 8 LIQUID TEMPERATURE 50º TO 75º F. LIQUID RATE L = 3000 LBS./HR. - FT.² * TRADEMARK OF JAEGER PRODUCTS INC. ** TRADEMARK OF LANTEC PRODUCTS INC
24 7.0 STRIPPING DATA #2 TYPE-K TELLERETTE TOWER PACKING TRICHLOROETHYLENE - AIR - WATER 6.0 HEIGHT OF A TRANSFER UNIT (HTU)OL - FEET 5.0 LIQUID RATE: 8150 LBS./HR. - FT.² TEMPERATURE 50º F
25 7.0 STRIPPING DATA #2 TYPE-K TELLERETTE TOWER PACKING METHYLENE CHLORIDE - AIR - WATER 6.0 HEIGHT OF A TRANSFER UNIT (HTU)OL - FEET 5.0 LIQUID RATE: 8150 LBS./HR. - FT.² TEMPERATURE 50º F
26 7.0 STRIPPING DATA #2 TYPE-K TELLERETTE TOWER PACKING CHLOROFORM - AIR - WATER 6.0 HEIGHT OF A TRANSFER UNIT (HTU)OL - FEET 5.0 LIQUID RATE: 8150 LBS./HR. - FT.² TEMPERATURE 50º F
27 1 PRESSURE DROP vs. GAS RATE #3 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM L = L = L = 6000 PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING DRY PACKING PARAMETER: LIQUID RATE - LBS./HR. - FT.²
28 0 LIQUID HOLDUP vs. GAS RATE #3 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING L = L = L = L = 8000 L = PARAMETER: LIQUID RATE - LBS./HR. - FT.²
29 5.0 HTU vs. GAS RATE #3 TYPE-R TELLERETTE TOWER PACKING AMMONIA-AIR-WATER SYSTEM L = 5000 HEIGHT OF A TRANSFER UNIT (HTU)og - FEET L = L = TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH 0% AMMONIA GAS CONCENTRATION (BY VOLUME) ONCE - THROUGH WATER 25ºC/77ºF LIQUID TEMPERATURE PARAMETER: LIQUID RATE - LBS./HR. - FT²
30 1 PRESSURE DROP vs. GAS RATE #3 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING L = L = L = L = L = PARAMETER LIQUID RATE: - LBS./HR. - FT.².04 L =
31 0 LIQUID HOLDUP vs. GAS RATE #3 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING L = 5000 L = PARAMETER: LIQUID RATE - LBS./HR. - FT.²
32 5.0 HTU vs. GAS RATE #3 TYPE-K TELLERETTE TOWER PACKING HCI-Air-H2O HEIGHT OF TRANSFER UNIT (HTU)og - FEET L = 2,000 L = 3,000 L = 10,000 OPERATING PARAMETERS: INLET CONCENTRATION 10-1,000 ppm HCI RECYCLE WATER WITH ph>2 LIQUID TEMPERATURE 77ºF (25ºC) LIQUID RATE - LBS./HR. - FT²
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