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- Problem 7 - 69 Gasoline at 20°C (sp. gr. 0.719, u = 0.000292 Pa-s) flows at the rate of 2 L/s through a pipe having an inside diameter of 60 mm Determine the Reynolds number Ans: 104.400The sulfur dioxide (SO 2 ) stack gas concentration from fossil fuel combustion is 2 ppmv. Determine the stack gas SO2 concentration in units of ug/m 3 . Assume 0°C and 1 atm pressure.Several liquids are layered inside a tank with pressur- ized air at the top. If the air pressure is 3.2 kPa, calcu- late the pressure at the bottom of the tank if the lay- ers include 20 cm of SAE 10 oil, 10 cm of water, 15 cm of glycerin, and 18 cm of carbon tetrachloride.
- 3. Compute the formula weight and density of exhaust gas which contains 72% N2, 1% Ar, 12% H2O, and 15% CO2. The temperature and pressure of the mixture are 290K and 1.2atm.3 A tank contains 100 gal of brine in which 50 lb of salt is dissolved. Brine containing 2 lb/gal of salt runs into the tank at the rate of 3 gal/min; and the mixture, assumed to be kept uniform by stirring, runs out at the rate of 2 gal/min. Assuming that the tank is sufficiently large to avoid overflow, find the amount of salt in the tank as a function of the time t. When will the con- centration of salt in the tank reach Ib/gal? How much salt is in the tank at the end of 30 min? Work Exercise 3 with the rates of influx and efflux interchanged, and find the amount of salt in the tank after 1 h instead of at the end of 30 min. Under these circumstances, when will the 4 tank contain the maximum amount of salt, and what is this amount?Q2) A tank is initially filled with 100 gallon of salt solution containing 100 Hb of salt. Fresh brine containing 2 Ib of salt per gallon runs into the tank at the rate 5 gal./min. and the mixture, assumed to be kept uniform by stirring, runs out at the same rate. Find the amount of salt in the tank at any time, and determine how long it will take for this 5 galimin 2b saligal 100 gal 100 b salt 5 galimin amount to reach 150 b.
- Home Work 3.A core sample is saturated with an oil (po = 35°API), gas and water. The initial weight of the sample is 224.14 g. After the gas is displaced by water (pw = 1 g/cm'), the weight is increased to 225.90 g. The sample is the placed in a Soxhlet distillation apparatus, and 4.4cm water is extracted. After drying the core sample, the weight is now 209.75 g. The sample bulk volume, 95 cm3 is measured in a mercury pycnometer. Find the porosity, water saturation, oil saturation, gas saturation and lithology of the core sample.Given the following pump data: 10 ft-positive suction head, 198 ft - discharge head, 16 ft- friction loss, 421 gpm - flow, Motor eff. Is 80% and Pump eff. Is 90%. What is the bhp? O23.10 bhp O 25.47 bhp O 26.53 bhp O24.16 bhpHello, I have an equalization tank with the following dimensions: Tank Dimensions: Height: 5.15 meters Length: 10.3 meters Width: 30.48 meters Total volume calculated: 1616.8116 m³ The design flow is 2.5 MGD. I want to treat the pH and alkalinity with soda ash. pH: 4.9 (desired: 7) Alkalinity [mg/L]: 44 mg/L (desired: 200 mg/L) How can I calculate how much soda ash I need to treat the pH and alkalinity in the equalization tank?
- gxauple3: A pehroleum Cut has the tellewing ASTM distillation data. volx distille 3 0 50 90 10 70 95 Temp °C 166.5 35 50 73 97.5 126.5 (Q2-5 Convent these dater to T Bp data methead. plot the results fhen Caladate k and Mut.? Danbat's usingvated sludge. 12.61 A step-aeration activated-sludge system at a loading of 40 lb of BOD/1000 ft³/day requires an air supply of 1200 ft/lb of BOD applied to maintain an adequate dissolved-oxygen level. The measured average oxygen utilization of the mixed liquor is 36 mg/1/hr. Calculate the oxygen transfer efficiency. (Assume 0.0174 lb of oxygen per cubic foot of air, which is the amount at 20°C and 760 mm pressure.) 12.62 An air sunnly4.15 A gas-condensate reservoir has an areal extent of 200 acres, an average thickness of 15 ft, an average porosity of 0.18, and an initial water saturation of 0.23. A PVT cell is used to simulate the production from the reservoir, and the following data are collected: Condensate Produced from Separator (moles) Wet Gas Pressure Produced (psia) (cc) Wet Gas 4000 (dew point) 3700 3300 0. 0.75 400 0.77 0.0003 450 0.81 0.0002 The initial cell volume was 1850 cc, and the initial gas contained 0.002 moles of condensate. The initial préssure is 4000 psia, and the reservoir temperature is 200°F. Calculate the amount of dry gas (SCF) and condensate (STB) recovered at 3300 psia from the reservoir. The molecular weight and specific gravity of the condensate are 145 and 0.8, respectively.