Question

In: Chemistry

A wastewater containing 150 mg/l chlorobenzene is treated in a laboratory adsorption unit using a PVC...

A wastewater containing 150 mg/l chlorobenzene is treated in a laboratory adsorption unit using a PVC column, 1.0 inch internal diameter, to an effluent concentration of 15 mg/l . Service times, and throughput volumes at specified depths and flowrates associated with a breakthrough concentration of 15.0 mg/l are given in table 1.

table1 : result of adsorption column experiment

Loading rate,gpm/ft2   Bed depth,ft Throughput volume, gal Time, hr

loading rate

gpm/ft2

bed depth

ft

throughput volume,

gal

time,

hr

2.5 3.0 810 980
5.0 1750 2230
7.0 2910 3440
5.0 3.0 605 420
5.0 1495 1000
9.0 3180 2185
7.5 5.0 1183 452
9.0 2781 1075
12.0 4000 1564

1) is the attainable effluent concentration satisfactory from a regulatory standpoint?

2) determine the Bohart-Adams constant ( K,N0 and x0) for each hydraulic loading.

3)base on data derived above design an adsorption column 2.0 ft internal diameter to treat a wastewater flow 5,000 gal/d containing 150 mg/l of CB. The attainable effluent concentration is 15 mg/l and it is desired to operate the column for 90 days(8 hourslday,7 days/week) before reching exhaustion.

4)calculate the yearly carbon requirements in cubic feet.

Solutions

Expert Solution

a) No, According to regulatory limits the concentration of chlorobenzene should not be more than 0.1 mg/l whereas in the effluent it is 15 mg/l therefore, it is not agreeable from the regulatory point of view also.

Where, C0 and Ct (mg/L) are the influent and effluent dyes concentration. kab (L/mg .min) is the kinetic constant, F (cm/min) is the linear velocity calculated by dividing the flow rate by the column section area, Z (cm) is the bed depth of column and N0 (mg/L) is the saturation concentration. The validity of this model is limited to the range of conditions used.

ln 15/150 = ln 15-ln 150 =2.70 -5.010 = -2.30

F =     flow rate /column section area

cross sectional area = pi r^2 = 3.14 * 0.041*0.041 =0.0052 Ft^2 = 4.83 cm^2

F = 2.5/4.83 = 0.517 cm/min

z values at 2.5 = 91.44cm, 152.4cm, 213.36 cm

suppose, for the first z value we calculate -2.30 = 0.517/91.44 Kab No

Kab No = 406.79

                                      


Related Solutions

A wastewater containing 150 mg/l chlorobenzene is treated in a laboratory adsorption unit using a PVC...
A wastewater containing 150 mg/l chlorobenzene is treated in a laboratory adsorption unit using a PVC column, 1.0 inch internal diameter, to an effluent concentration of 15 mg/l . Service times, and throughput volumes at specified depths and flowrates associated with a breakthrough concentration of 15.0 mg/l are given in table 1. table1 : result of adsorption column experiment Loading rate,gpm/ft2   Bed depth,ft Throughput volume, gal Time, hr loading rate gpm/ft2 bed depth ft throughput volume, gal time, hr 2.5...
Compute the carbonaceous and nitrogenous oxygen demand in mg/L for a wastewater containing a) 100 mg/L...
Compute the carbonaceous and nitrogenous oxygen demand in mg/L for a wastewater containing a) 100 mg/L C9N2H6O2 b) 100mg/L C6N2H4O c) 100mg/L C12N4H6O2 d) 100mg/L C10N2H8O2
compute the total organic carbon in mg/L for a wastewater containing. a) 100mg/L C9N2H6O2 b) 100mg/L...
compute the total organic carbon in mg/L for a wastewater containing. a) 100mg/L C9N2H6O2 b) 100mg/L C6N2H4O c) 100mg/L C12N4H6O2 d) 100mg/L C10N2H8O2
2. A wastewater treatment plant discharges an effluent containing 3 mg/L of dissolved oxygen to a...
2. A wastewater treatment plant discharges an effluent containing 3 mg/L of dissolved oxygen to a river that has a dissolved-oxygen concentration of 6 mg/L upstream of the discharge. The saturation dissolved oxygen for the river is 8 mg/L. Assume that the WWTP discharge rate represents 80% of the river flow rate which travels 0.5 km in an hour. The CBOD5 of the river is 5 mg/L with a decay coefficient of 0.25/day. The reaeration coefficient of the river is...
Determine the Theorethical Oxygen Demand(ThOD) for sewage containing 150 mg/L of CH2(NH2)COOH and 40 mg/L of...
Determine the Theorethical Oxygen Demand(ThOD) for sewage containing 150 mg/L of CH2(NH2)COOH and 40 mg/L of NH3. Find, (1) mg/L of oxygen for both carbon and nitrogen compounds (2) grams of oxygen per gram of CH2(NH2)COOH (oxygen used only for carbon oxidation) (3) grams of oxygen per gram of NH3 (oxygen used only for nitrification)
The treated effluent from a wastewater treatment plant contains ammonium (NH4+) at 76.0 mg NH4+-N/L and...
The treated effluent from a wastewater treatment plant contains ammonium (NH4+) at 76.0 mg NH4+-N/L and nitrate at 22.0 mg NO3--N/L. Convert these concentrations to mg NH4+/L and mg NO3-/L.
2.The treated effluent from a wastewater treatment plant contains ammonium (NH4+) at 76.0 mg NH4+-N/L and...
2.The treated effluent from a wastewater treatment plant contains ammonium (NH4+) at 76.0 mg NH4+-N/L and nitrate at 22.0 mg NO3--N/L. Convert these concentrations to mg NH4+/L and mg NO3-/L. For the data provided in question 2, express the ammonium and nitrate concentrations in (a) molar units, and (b) ppmm NH4+ and ppmm NO3-.
Calculate the molarity of the following: (a) 90 mg/L HNO3, (b) 150 mg/L CaCO3,
Calculate the molarity of the following: (a) 90 mg/L HNO3, (b) 150 mg/L CaCO3,
Calculate the total theoretical oxygen demand (mg/L) of a solution containing 750 mg/L of C5H7O2N. Also,...
Calculate the total theoretical oxygen demand (mg/L) of a solution containing 750 mg/L of C5H7O2N. Also, calculate Carbonaceous ThOD and Nitrogenous ThOD separately
The laboratory reports that the concentration of ammonia as nitrogen in a sample is 3.4 mg/l....
The laboratory reports that the concentration of ammonia as nitrogen in a sample is 3.4 mg/l. The pH value of the sample is 5.5 units. In what form is almost all of this ammonia? could this sample be toxic to aquatic organisms?
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT