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A cylinder contains 10 kg of gas at a pressure of 10^7 N / m^2.
Assuming the temperature of the gas to be constant ,
calculate the quantity of gas taken out of the cylinder if the final pressure is 2.5 * 10^6 N / m^2.
Weight Percentage of MTBE (methyl tert-butylether) in Gasoline : Oxygen Content, If gasoline had a hypothetical chemical formula of C8H17, and we knew the chemical formula of MTBE as CH3OC4H9, what weight (actual weight and percent by weight) of M..
The following two reactions take place in a gas phase reactor at 3000 K and 1 atmosphere pressure: 2CO2(g) 2CO(g) + O2(g) Keq.1071 O2(g) + N2(g) 2NO(g) Keq.01493
Suggest suitable materials of construction for the following applications: a. A 10,000 m3 storage tank for toluene
A large CSTR, small CSTR and PFR of fixed volume are available. In general, how wouldyou arrange them for getting maximum conversion forreactions of order >1 and1 arrangement is PFR followed by small CSTR followed by large CSTR tomaintain the reac..
Acetylene is formed as a by-product in the manufacture of ethylene. It is removed by selective hydrogenation using noble metal catalysts (see, for example, US 7,453,017). A particular catalyst achieves 90% acetylene saturation with 50% hydrogen se..
An analyst gathered the following information about the return distributions for two portfolios during the same time period:
Calculate the feed rate F and the product rate - Evaporation in Double-Effect Reverse-Feed Evaporators.
Find the air fuel ratio for stoichiometric combustion of Butane by volume. Calculate the percentage of carbon dioxide present in the DRY flue gas if 30% excess air is used
You are required to write a mini project that is structured in such a way as to answers all the questions contained within the project description.
Mass of Air Required for Combustion of Fuel. A coal fired boiler uses fuel having the following analysis by mass:
a. Estimate the feed flow rates of glycine and guaiacol that would be needed to produce 100 kg/day of the API. b. Estimate how much product is lost in the thin-film evaporator.
It is proposed to use an existing distillation column, which is fitted with a dephlegmator (reflux condenser) that has 200 vertical, 50 mm i.d. tubes, for separating benzene from a mixture of chlorobenzenes.
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