For a heat exchanger, will the overall heat transfer coefficient increase along with an increase in lmtd (log mean temperature difference) around the unit?
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which type of packing gives large interfacial area stacked or random?
How are vessel lined with glass or how are they coated?
why do tangential entry require for a cyclone separator?
What is the best way to handle bend or turns in slurry piping systems?
A cylindrical vessel of 10m height has water upto 6m and is under a pressure of 15bar.What will be the pressure at the bottom most point of the vessel?
Explain the Deacon reaction?
When specifying a cooling tower, should I look up historic wet bulb temperatures for my area or should I take measurements?
Can condensate control in a reboiler cause water hammer problems?
What are the problems that are associated with the expansion joints?
send me previous year question paper for ongc gt 2011 written exam
CHEMICAL ENERGY BALANCE - EXAMPLE 11.5 : According to Margules Equation, P = x(1) p(1) g(1) + x(2) p(2) g(2) for a two-component mixture where P is bubble pressure, x is mole fraction, p is saturation pressure, g is constant given by ln g(1) = x(2) A x(2). Find the value of A as a constant when P = 1.08 bar, p(1) = 0.82 bar, p(2) = 1.93 bar in a 50 : 50 mole fraction mixture. Estimate the pressure required to completely liquefy the 30 : 70 mixture using the same equation, by proving P = 1.39 bar. Take note that ln g(2) = x(1) A x(1), ln g(1) = x(2) A x(2).
Can anybody suggest the Methods/Procedures for estimation of oxygen, hydrogen, methane, carbon dioxide, CO, etc. in binary or complex gas mixtures?
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