An industrial outlet is discharging a 1.8 m/s waste stream with a BOD of 20 mg/L and a DO concentration of 1.5 mg/L into a river with a flow of 70 mº/s that contains 0.51 mg/L BOD and has an existing oxygen deficit of 1.2 mg/L If the saturated DO concentration is 9.50 mg/L, what is the initial deficit D. (mg/). In the Oxygen Sag Model for this situation? a. 1.37 mg/L
b. 1.0 mg/l
c. 1.2 mg/L
d. 8.0 mg/L

Fluids at rest possess no flow energy. a)- true b)- false

A3-mm-thick panel of aluminum alloy (k 177 w/m-k, c 875 j/kg-k and ? = 2770 kg/m) is finished on both sides with an epoxy coating that must be cured at or above t,-150°c for at least 5 min. the production line for the curing operation involves two steps: (1) heating in a large oven with air at ts,0-175°c and a convection coefficient of h, 40 w/m2. k, and (2) cooling in a large chamber with air at 25°c and a con- vection coefficient of he 10 w/m2.k. the heating portion of the process is conducted over a time interval te which exceeds the ime required to reach 150°c by 5 min (h = r + 300 s). the coating has an emissivity of ? = 0.8, and the temperatures of the oven and chamber walls are 175 and 25°c, respectively. if the panel is placed in the oven at an initial temperature of 25°c and removed from the chamber at a safe-to-touch tempera ture of 37°c, what is the total elapsed time for the two-step curing operation?

Air flows over a heated plate àt a velocity of 50m/s. the local skin factor coefficient at a point on a plate is 0.004. estimate the local heat transfer coefficient at this point.the following property data for air are given: density = 0.88kg/m3 , viscosity 2.286 x 10 ^-5 kgm/s , k = 0.035w/mk ,cp = 1.001kj/kgk. use colburn reynolds analogy.