Info

50*

42*

27*

Data courtesy of the Norton Company.

Operating conditions: CO2, 1 percent mole in air; NaOH, 4 percent weight (1 normal); 25 percent conversion to sodium carbonate; temperature, 24°C (75°F); pressure, 98.6 kPa (0.97 atm); gas rate = 0.68 kg/(s^m2) = 0.59 m/s = 500 Mbft2) = 1.92 ft/s except for values with asterisks, which were run at 1.22 kg/(s^m2) = 1.05 m/s = 900 lb/(h-ft2) = 3.46 ft/s superficial velocity; packed height, 3.05 m (10 ft); tower diameter, 0.76 m (2.5 ft). To convert table values to units of (lhmol)/(hft3), multiply by 0.0624.

Data courtesy of the Norton Company.

Operating conditions: CO2, 1 percent mole in air; NaOH, 4 percent weight (1 normal); 25 percent conversion to sodium carbonate; temperature, 24°C (75°F); pressure, 98.6 kPa (0.97 atm); gas rate = 0.68 kg/(s^m2) = 0.59 m/s = 500 Mbft2) = 1.92 ft/s except for values with asterisks, which were run at 1.22 kg/(s^m2) = 1.05 m/s = 900 lb/(h-ft2) = 3.46 ft/s superficial velocity; packed height, 3.05 m (10 ft); tower diameter, 0.76 m (2.5 ft). To convert table values to units of (lhmol)/(hft3), multiply by 0.0624.

TABLE 14-3 Typical KGa Values for Various Chemically Reacting Systems, kmol/(h m3)

Gas-phase reactant

Liquid-phase reactant

Koa

Special conditions

HCl

0 0

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