September 2023

A venturi meter is installed to measure the flow rate of water in a 178 mm diameter (ID) pipe The throat diameter is 102 mm

A venturi meter is installed to measure the flow rate of water in a 178 mm diameter (ID) pipe The throat diameter is 102 mm

Q. A venturi meter is installed to measure the flow rate of water in a 178 mm diameter (ID) pipe. The throat diameter is 102 mm. The differential pressure measured using a manometer is 154.3 kN/m2. The data given are: discharge coefficient = 0.98; water density = 1000 kg/m3. The volumetric flow rate of water

A venturi meter is installed to measure the flow rate of water in a 178 mm diameter (ID) pipe The throat diameter is 102 mm Read More »

For a chemical reaction, the ratio of rate constant at 500 K to that at 400 K is 2.5. Given R = 8.314 J

For a chemical reaction, the ratio of rate constant at 500 K to that at 400 K is 2.5. Given R = 8.314 J

Q. For a chemical reaction, the ratio of rate constant at 500 K to that at 400 K is 2.5. Given R = 8.314 J mol-1 K-1, the value of activation energy (in kJ/mol) is (A) 10.5                      (B) 12.0                      (C) 15.2                     (D) 18.4 Ans: 15.2

For a chemical reaction, the ratio of rate constant at 500 K to that at 400 K is 2.5. Given R = 8.314 J Read More »

For absorption of H2S from a mixture with hydrocarbon vapour into an aqueous alkanolamine

For absorption of H2S from a mixture with hydrocarbon vapour into an aqueous alkanolamine

Q. For absorption of H2S from a mixture with hydrocarbon vapour into an aqueous alkanolamine solution, the liquid phase mass transfer resistance is A. significantly higher than that of the gas phase B. negligible compared to that of the gas phase C. equal to that of the gas phase D. dependent on the gas phase

For absorption of H2S from a mixture with hydrocarbon vapour into an aqueous alkanolamine Read More »

Liquid phase isomerization of o-xylene to p-xylene using a zeolite catalyst was carried out in a CSTR

Liquid phase isomerization of o-xylene to p-xylene using a zeolite catalyst was carried out in a CSTR

Q. Liquid phase isomerization of o-xylene to p-xylene using a zeolite catalyst was carried out in a CSTR. Three sets of kinetic data at different temperatures and stirring speeds were obtained as shown below. The operating condition at which the reaction rate is not controlled by external mass transfer resistance is (A) T = 500

Liquid phase isomerization of o-xylene to p-xylene using a zeolite catalyst was carried out in a CSTR Read More »

Two packed towers are designed for the same mass velocity of the gas. The first has liquid and gas flow rates of 30 kg/s and 1.2 kg/s

Two packed towers are designed for the same mass velocity of the gas. The first has liquid and gas flow rates of 30 kg/s and 1.2 kg/s

Q. Two packed towers are designed for the same mass velocity of the gas. The first has liquid and gas flow rates of 30 kg/s and 1.2 kg/s, respectively, while the corresponding flow rates in the second tower are 67.5 kg/s and 1.8 kg/s. The ratio of the design diameter of the wider tower to

Two packed towers are designed for the same mass velocity of the gas. The first has liquid and gas flow rates of 30 kg/s and 1.2 kg/s Read More »

Scroll to Top