PHASE SEPARATION IS NO POSSIBLE AT 313K . TEMPERATURE SHOULD MUST BE HIGHER THAN 80 DEG C OR 353 K
Please Find the solution below. AT the given temp. entire feed would be in Liquid phase. I have solved this using Excel sheet.
Question 1 hydrooarbon A mixed stream enters a flash drum at 500 kPa and 313 K....
wors are cloar and unambiguous Answer the questions in the correct order and ensure that the answors are cioarly numbered. Make sure that all pages of the assignment are numbered and stapiod together Complete the assignment cover accurately and in detail. Question A mixed hydrocarbon stream enters a flash drum stream is 325 kmeol/ assumed that equilibrium is reached i Do at least three iterations until the same value is achieved. The composition of the feed. 00 kPa and 313...
The heavier component has to be removed from a gas stream by absorption. The absorption column operates at 2 550 kPa. The entering liquid is high molecular mass oil which contains 0.45% of the heaviest component but none of the lighter components. The total molar flowrate of the oil entering the absorber is 150 kmol/hr. The effluent gas that enters the absorber at 800 kmolhr contains 20 mol% C, 46 mol% C2, 30 mol% C3, 4 mol% n-C4. There are...
A mixture containing 42% benzene and 58% toluene by mass is fed to a distillation column. A second mixture is also fed to the distillation column and has a composition of 65% toluene and 35% acetone by mass. The flowrates of the mixtures are 2500 kg h1 and 1500 kg h1 respectively. An overhead distillate exit stream of 800 kg h-1 containing 23% acetone and a bottom exit stream of 25% benzene are produced. Determine the bottom exit flowrate and...
Methane gas is burned with 30 percent excess air. This fuel enters a steady- flow combustor at 0.8 atm and 25oC and is mixed with the air. The products of combustion leave this reactor at 0.8 atm and 1600 K. Determine the equilibrium composition of the products of combustion and the amount of heat released by this combustion in kJ/kmol methane. Use data from the tables CH 25°C CO2, H3O chamber NO. O2 N2 1600 K 30% excess air 25°C...