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Question 4 A pipeline conveys benzene from one point to the other. A gauge attached to line reads 1 5 0 kPa. It is desired

Question 4
A pipeline conveys benzene from one point to the other. A gauge attached to line reads 150 kPa. It is desired to check the gauge reading with benzene -over-mercury U-tube manometer. Determine the expected height difference of the mercury in the manometer; if on one end the manometer is open to the atmosphere and on the other end where the gauge pressure is connected there is a 3cm height of benzene above the mercury meniscus. (benzene density is 876kgm3 and mercury 13600kgm3)
Question 5
The temperature of the earth's atmosphere drops about 5C for every 1km above the earth. If the temperature of the air on the ground is 15C and the pressure is 760mmHg. At what height above the earth is the pressure 380mmHg? Assume the air behaves as an ideal gas.
Use the following Hydrostatic equilibrium equation:
dp+gdz=0
Question 6
A cylindrical tank is vented to the atmosphere that serves as a reservoir for octane before it is piped to another location is 140ft in diameter. Determine the pressure difference between the top and bottom of the walls due to the octane when the tank is filled to a depth of 30ft(9.14m). Why is the vent necessary?
NB: Atmospheric conditions are such that the pressure is 1atm and temperature 25C. SG of octane is 0.701
Question 7
A continuous gravity decanter separates chlorobenzene from an aqueous wash liquid. If the total depth of the separator is 1m and the interphase is to be 0.6m from the vessel floor, what should the height of the heavy-liquid overflow leg be?
If the separator is to separate 1600kghr chlorobenzene from 2100kghr wash liquid, what volume of the separator is needed?
The following information is provided
The density of chlorobenzene is 1109kgm3 and that of the wash liquid 1020kgm3
The wash liquid is the continuous phase
The viscosity of the wash liquid is 0.72cP
The following equations are provided:
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