Bulletin Description Tellerette Tower Packing Technical Data Index Bulletin No. Generalized Pressure Drop Correlation... 12-10.00 No. 1 Pressure Drop vs. Gas Rate, #1 Tellerette Tower Packing...12-10.10 Liquid Holdup vs. Gas Rate, #1 Tellerette Tower Packing... 12-10.20 HTU vs. Gas Rate Ammonia-Air-Water, #1 Tellerette Tower Packing... 12-10.30 Tellerette Performance, Particle Diameter vs. Collection Efficiency... 12-100 No. 2 Type-R Pressure Drop vs. Gas Rate, Air-Water System...12-10.11 Liquid Holdup vs. Gas Rate, Air-Water System... 12-10.21 HTU vs. Gas Ammonia-Air-Water System... 12-10.31 HTU vs. Gas Ammonia-Air-H 2 SO 4 System... 12-100 HTU vs. Gas Rate, Gaseous HCI-Air-Water System... 12-100 Kga vs. Liquid Rate, CO 2 -Air Caustic System... 12-100 Tellerette Performance, Particle Diameter vs. Collection Efficiency... 12-101 HTU vs. Gas Rate, #2 Type-R Tellerette vs. 2 Intalox Saddles, Ammonia-Air-Water System... 12-102 Pressure Drop vs. Gas Rate, #2 Type-R Tellerette vs. 2 Intalox Saddles, Air-Water System... 12-103 No. 2 Type-K Pressure Drop vs. Gas Rate, Air-Water System...12-10.13 Liquid Holdup vs. Gas Rate, Air-Water System... 12-10.23 HTU vs. Gas Rate, Ammonia-Air-Water System... 12-10.33 HTU vs. Gas Rate, H 2 S-Air-Caustic/Hypo... 12-101 HTU vs. Gas Rate, SO 2 -Air-Caustic System... 12-102 Pressure Drop vs. Gas Rate, #2 Type-K Tellerette vs #2 Tri-Packs, Air-Water System... 12-100 HTU vs. Gas Rate, #2 Type-K Tellerette vs. #2 Tri-Packs vs. 2 Saddles, Ammonia-Air-Water System... 12-101 HTU vs. Gas Rate, #2 Type-K Tellerette vs. #2 Tri-Packs vs. 3 Lanpac. So 2 -Air-Caustic System... 12-104 Stripping Data, Trichloroethylene-Air-Water... 12-100 Stripping Data, Methylene Chloride-Air-Water... 12-101 Stripping Data, Chloroform-Air-Water... 12-102 No. 3 Type-R Pressure Drop vs. Gas Rate, Air-Water System...12-10.12 Liquid Holdup vs. Gas Rate, Air-Water System... 12-10.22 HTU vs. Gas Rate, Ammonia-Air-Water System... 12-10.32 No. 3 Type-K Pressure Drop vs. Gas Rate, Air-Water System...12-10.14 Liquid Holdup vs. Gas Rate, Air-Water System... 12-10.24 HTU vs. Gas Rate, HCI-Air-Caustic System... 12-104
00 GENERALIZED PRESSURE DROP CORRELATION 00 00 THE TELLERETTE INDICATES TOWER PRESSURE DROP INCHES H2O/FT..200 2 TELLERETTE PACKING FACTORS ARE SHOWN ON THE REVERSE SIDE.100 A B 1.060 C 0.040 0.25 FLOODING LINE.020.010 0.10.006.004.002 A - APPROX. UPPER LIMIT OF LOADING ZONE B - LINE REPRESENTING MAJORITY OF DATA C - APPROX. LOWER LIMIT OF LOADING ZONE.02.04.06.10.2 6.0 10.0 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 0 12-10.00
1 PRESSURE DROP vs. GAS RATE #1 TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING.3.2.15.10.09.08 L = 8000 L = 6000 L = 2000 DRY PACKING.07.06.05 PARAMETER: LIQUID RATE - LBS./HR. - FT.².04 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.10
0 LIQUID HOLDUP vs. GAS RATE #1 TELLERETTE TOWER PACKING AIR-WATER SYSTEM.30 LIQUID HOLDUP - CUBIC FEET OF WATER/CUBIC FOOT OF PACKING.20.10.09.08.07.06.05.04 L = 8000 L = 6000 L = 2000.03 PARAMETER: LIQUID RATE - LBS./HR. - FT.².02 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.20
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 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000 12-10.30
15.0 1 TELLERETTE PERFORMANCE PARTICLE DIAMETER VS. COLLECTION EFFICIENCY #1 TELLERETTE PARAMETERS: GAS VELOCITY = 8.0 FT./SEC. PACKING DEPTH = FT. 1 1 PARTICLE DIAMETER (MICRONS) 1 10.0 9.0 8.0 7.0 SP. GR. = 6.0 SP. GR. = 5.0 SP. GR. = 70 75 80 85 90 95 100 TOTAL EFFICIENCY - % (BY PARTICLE COUNT) 12-100
1 PRESSURE DROP vs. GAS RATE #2 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM L = 30000 L = 20000 L = 8000 L = 6000 L = 2000 PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING.3.2.15.10.09 DRY PACKING.08.07.06.05 PARAMETER: LIQUID RATE - LBS./HR. - FT.².04 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.11
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.20.10.09.08.07.06.05.04 L = 30000 L = 20000 L = 15000 L = 8000 L = 6000 L = 2000.03 PARAMETER: LIQUID RATE - LBS./HR. - FT.².02 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.21
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 = 15000 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 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 3200 12-10.31
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 2000 2100 2200 2300 2400 2500 2600 12-100
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 12-100 AND 12-101 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 12-100
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 1 2000 3000 4000 5000 6000 7000 8000 9000 10000 20000 30000 40000 LIQUID RATE - LBS./HR. - FT. 2 12-100
15.0 1 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) 1 10.0 9.0 8.0 7.0 SP. GR. = 6.0 SP. GR. = 5.0 SP. GR. = 70 75 80 85 90 95 100 TOTAL EFFICIENCY - % (BY PARTICLE COUNT) 12-101
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 = 15000 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 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 3200 * REGISTERED TRADEMARK OF KOCH-GLITSCH. 12-102
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.3.2.15.10.09 L = 5000 DRY PACKING DRY PACKING.08.07.06.05 PARAMETER: LIQUID RATE - LBS./HR. - FT.² #2 TYPE-R TELLERETTE #2 PLASTIC INTALOX SADDLES*.04 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 *REGISTERED TRADEMARK OF KOCH - GLITSCH 12-103
1 PRESSURE DROP vs. GAS RATE #2 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING.3.2.15.10.09 L = 30000 L = 20000 L = 6000 L = 2000 DRY PACKING.08.07.06.05 PARAMETER: LIQUID RATE - LBS./HR. - FT.².04 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.13
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.20.10.09.08.07.06.05.04 L = 30000 L = 20000 L = 8000 L = 6000 L = 2000.03 PARAMETER: LIQUID RATE - LBS./HR. - FT.².02 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.23
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 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 3200 12-10.33
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 = 5-200 ppm HYDROGEN SULFIDE SODIUM HYDROXIDE =.0004% BY WEIGHT SODIUM HYPOCHLORITE = 0.25% BY WEIGHT LIQUID RATE = 3000 LBS./HR. FT.² 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 12-101
5.0 HTU vs. GAS RATE #2 TYPE-K TELLERETTE PACKING SULFUR DIOXIDE-AIR-CAUSTIC HEIGHT OF A TRANSFER UNIT (HTU)og - FEET 1 1 1 1 1 1 1.3 1.2 1.1 L = 2000 L = 3000 L = 6000 TEST CONDITIONS: 30 INCH DIAMETER COLUMN 8 FOOT PACKING DEPTH SO2 GAS INLET CONCENTRATION 50-100 ppmv NaOH ph > 8 LIQUID TEMPERATURE 50º TO 75º F. LIQUID RATE L = LBS./HR. - FT.² 600 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 12-102
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.3.2.15.10.09.08.07.06.05.04 PARAMETER: LIQUID RATE - LBS./HR. - FT.² #2 TYPE-K TELLERETTE #2 TRI-PACKS * 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 *REGISTERED TRADEMARK OF JAEGER PRODUCTS, INC. 12-100
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 * 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 3200 * TRADEMARK OF JAEGER PRODUCTS, INC. 12-101
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 1 1 1 1 1 1 1.3 1.2 1.1 3 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 50-100 ppmv NaOH ph > 8 LIQUID TEMPERATURE 50º TO 75º F. LIQUID RATE L = 3000 LBS./HR. - FT.² 600 800 1000 1200 1400 1600 1800 2000 2200 2400 2600 2800 3000 * TRADEMARK OF JAEGER PRODUCTS INC. ** TRADEMARK OF LANTEC PRODUCTS INC. 12-104
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 300 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 12-100
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 300 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 12-101
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 300 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400 12-102
1 PRESSURE DROP vs. GAS RATE #3 TYPE-R TELLERETTE TOWER PACKING AIR-WATER SYSTEM L = 30000 L = 20000 L = 6000 PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING.3.2.15.10.09.08 DRY PACKING.07.06.05 PARAMETER: LIQUID RATE - LBS./HR. - FT.².04 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.12
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.20.10.09.08.07.06.05.04 L = 30000 L = 20000 L = 15000 L = 8000 L = 6000.03 PARAMETER: LIQUID RATE - LBS./HR. - FT.².02 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.22
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 = 15000 L = 20000 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 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000 12-10.32
1 PRESSURE DROP vs. GAS RATE #3 TYPE-K TELLERETTE TOWER PACKING AIR-WATER SYSTEM PRESSURE DROP - INCHES WATER COLUMN/FOOT OF PACKING.3.2.15.10.09.08.07 L = 30000 L = 25000.06 L = 20000 L = 15000 L = 3000.05 PARAMETER LIQUID RATE: - LBS./HR. - FT.².04 L = 5000 200 300 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.14
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.20.10.09.08.07.06.05.04 L = 5000 L = 3000.03 PARAMETER: LIQUID RATE - LBS./HR. - FT.².02 400 500 600 700 800 900 1000 1500 2000 3000 4000 12-10.24
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 1800 2000 2200 2400 2600 2800 3000 3200 3400 3600 3800 4000 12-104