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This section includes 1443 Mcqs, each offering curated multiple-choice questions to sharpen your Chemical Engineering knowledge and support exam preparation. Choose a topic below to get started.
1201. |
From among the following, choose one which is not an exothermic process. |
A. | Methanol synthesis |
B. | Catalytic cracking |
C. | Ammonia synthesis |
D. | Oxidation of sulphur |
Answer» C. Ammonia synthesis | |
1202. |
The ratio of moles of a reactant converted into the desired product to that converted into unwanted product is called |
A. | Operational yield |
B. | Relative yield |
C. | Selectivity |
D. | None of these |
Answer» D. None of these | |
1203. |
Velocity of a reaction depends upon the |
A. | Nature of the reactants |
B. | Concentration of the reactants |
C. | Temperature at which the reaction is carried |
D. | All (A), (B) and (C) |
Answer» E. | |
1204. |
If the time required to complete a definite fraction of reaction varies inversely as the concentration of the reactants, then the order of reaction is |
A. | 1 |
B. | 2 |
C. | 3 |
D. | 4 |
Answer» C. 3 | |
1205. |
Chemical reaction rate of a component depends upon the |
A. | Composition of the component only |
B. | Temperature of the system |
C. | Pressure of the system |
D. | All (A), (B) and (C) |
Answer» E. | |
1206. |
A spherical porous catalyst particle of radius R is subjected to reactant A which reacts to form B by a zero order surface reaction A → B. Film mass transfer resistance is negligible and pore diffusion of A is rate controlling. The effectiveness factor of the catalyst is reported as 7/8. Which of the following statement is true? |
A. | Inner catalyst core of radius R/8 does not participate in reaction |
B. | Inner catalyst core of radius R/2 does not participate in reaction |
C. | Inner catalyst core of radius 7R/8 does not participate in reaction |
D. | Effectiveness factor for a zero order reaction cannot be 7/8 as it must always be 1 |
Answer» B. Inner catalyst core of radius R/2 does not participate in reaction | |
1207. |
If helium is introduced in a reactor containing O2, SO2 and SO3 at equilibrium, so that total pressure increases while volume and temperature remains constant. In this case the dissociation of SO3 (as per Le Chatelier's principle). |
A. | Decreases |
B. | Increases |
C. | Remains unaltered |
D. | Changes unpredictably |
Answer» B. Increases | |
1208. |
Specific rate constant for a second order reaction |
A. | Is independent of temperature |
B. | Varies with temperature |
C. | Depends on the nature of the reactants |
D. | Both (B) and (C) |
Answer» E. | |
1209. |
For a first order reaction carried out in a plug flow reactor, the space time is |
A. | (1/k) ln C0/C |
B. | (1/k) ln C/C0 |
C. | k ln C0/C |
D. | k ln C/C0 |
Answer» B. (1/k) ln C/C0 | |
1210. |
A space time of 3 hours for a flow reactor means that |
A. | The time required to process one reactor volume of feed (measured at specified conditions) is 3 hours |
B. | Three reactor volumes of feed can be processed every hour |
C. | It takes three hours to dump the entire volume of the reactor with feed |
D. | Conversion is cent per cent after three hours |
Answer» B. Three reactor volumes of feed can be processed every hour | |
1211. |
If n = overall order of a chemical reaction. a = initial concentration of reactant. t = time required to complete a definite fraction of the reaction. Then pick out the correct relationship. |
A. | t ∝ 1/a n |
B. | t ∝ 1/a n - 1 |
C. | t ∝ 1/a n + 1 |
D. | t ∝ a n |
Answer» C. t ∝ 1/a n + 1 | |
1212. |
A reactor is generally termed as an autoclave, when it is a |
A. | High pressure batch reactor |
B. | Atmospheric pressure tank reactor |
C. | High pressure tubular reactor |
D. | Atmospheric pressure CSTR |
Answer» B. Atmospheric pressure tank reactor | |
1213. |
For an autocatalytic reactor, the suitable reactor set up is |
A. | P.F. reactors in series |
B. | CSTR in series |
C. | CSTR followed by P.F. reactor |
D. | P.F. reactor followed by CSTR |
Answer» D. P.F. reactor followed by CSTR | |
1214. |
Which of the following factors control the design of a fluid-solid reactor? |
A. | Reaction kinetics for single particle |
B. | Size distribution of solids being treated |
C. | Flow patterns of solids and fluid in the reactor |
D. | All (A), (B) and (C) |
Answer» E. | |
1215. |
__________ explains the mechanism of catalysis. |
A. | Activated complex theory |
B. | Collision theory |
C. | Thermodynamics |
D. | None of these |
Answer» B. Collision theory | |
1216. |
If Thiele modulus is __________, then the pore diffusion resistance in a catalyst may be considered as negligible. |
A. | 0 |
B. | ∞ |
C. | < 0.5 |
D. | > 0.5 |
Answer» D. > 0.5 | |
1217. |
Rate of a chemical reaction is not influenced by the |
A. | Catalyst |
B. | Temperature |
C. | Reactants concentration |
D. | Number of molecules of reactants taking part in a reaction |
Answer» E. | |
1218. |
The irreversible reaction is a special case of reversible reaction, if the |
A. | Equilibrium constant is 1 |
B. | Conversion of the reactant at equilibrium condition is zero |
C. | Reactant concentration at equilibrium condition is zero |
D. | All (A), (B) and (C) |
Answer» D. All (A), (B) and (C) | |
1219. |
For multiple reactions, the flow pattern within the vessel affects the |
A. | Size requirement |
B. | Distribution of reaction products |
C. | Both (A) and (B) |
D. | Neither (A) nor (B) |
Answer» D. Neither (A) nor (B) | |
1220. |
A catalyst is said to be a negative catalyst, if it |
A. | Retards the rate of reaction |
B. | Reduces the value of equilibrium constant |
C. | Does not initiate the reaction |
D. | All (A), (B) and (C) |
Answer» B. Reduces the value of equilibrium constant | |
1221. |
The excess energy of reactants in a chemical reaction required to dissociate into products is termed as the __________ energy. |
A. | Activation |
B. | Potential |
C. | Binding |
D. | Threshold |
Answer» B. Potential | |
1222. |
The response curve for a step input signal from a reactor is called C-curve. The variance of C-curve in a 'tanks in series model' comprising of 'm' tanks is equal to |
A. | m |
B. | 1/m |
C. | √m |
D. | m 2 |
Answer» C. √m | |
1223. |
If the time required to change the concentration of reactant to half its original value is independent of the initial concentration, the order of reaction is: |
A. | Zero |
B. | One |
C. | Two |
D. | Three |
Answer» C. Two | |
1224. |
Rate constant 'k' and absolute temperature 'T' are related by collision theory (for bimolecular) as |
A. | k ∝ T 1.5 |
B. | k ∝ exp(-E/RT) |
C. | k ∝ √T |
D. | k ∝ T |
Answer» D. k ∝ T | |
1225. |
A back mix reactor is |
A. | Suitable for gas phase reactions |
B. | Ideal at very low conversion |
C. | Same as plug flow reactor (PFR) |
D. | Same as ideal stirred tank reactor |
Answer» E. | |
1226. |
Which of the following is a characteristic of an ideal plug flow reactor? |
A. | Axial dispersion |
B. | Flat velocity profile |
C. | Uniform mixing |
D. | None of these |
Answer» C. Uniform mixing | |
1227. |
The increase in the rate of reaction with temperature is due to |
A. | Increase in the number of effective collisions |
B. | Decrease in activation energy |
C. | Increase in the average kinetic energy of the reacting molecules |
D. | None of these |
Answer» C. Increase in the average kinetic energy of the reacting molecules | |
1228. |
What is the order of a chemical reaction in which doubling the initial concentration of the reactants doubles the half life time of the reaction? |
A. | 0 |
B. | 1 |
C. | 2 |
D. | 3 |
Answer» B. 1 | |
1229. |
Pick out the wrong statement. |
A. | Catalytic activity of enzyme catalysed reactions which is affected by temperature, pH value & chemical agents, is maximum at a temperature of about 45°C |
B. | Most of the enzyme catalysed reactions involve at least two substrates |
C. | Enzymes help in increasing the activation energy of the reaction |
D. | Equilibrium concentrations in enzyme catalysed reactions can be calculated by using the thermodynamic properties of substrates & products |
Answer» D. Equilibrium concentrations in enzyme catalysed reactions can be calculated by using the thermodynamic properties of substrates & products | |
1230. |
Helium-mercury method can be used to determine the __________ of the catalyst particle |
A. | Pore volume |
B. | Solid density |
C. | Porosity |
D. | All (A), (B), & (C) |
Answer» E. | |
1231. |
For an ideal gas mixture undergoing a reversible gaseous phase chemical reaction, the equilibrium constant |
A. | Is independent of pressure |
B. | Increases with pressure |
C. | Decreases with pressure |
D. | Increases /decreases with pressure depending on the stoichiometric co-efficients of the reaction |
Answer» C. Decreases with pressure | |
1232. |
Which of the following is the most suitable for very high pressure gas phase reaction? |
A. | Batch reactor |
B. | Tubular flow reactor |
C. | Stirred tank reactor |
D. | Fluidised bed reactor |
Answer» C. Stirred tank reactor | |
1233. |
Maximum equilibrium conversion for endothermic reaction is obtained at the __________ temperature. |
A. | Highest possible |
B. | Lowest possible |
C. | Intermediate |
D. | Room |
Answer» B. Lowest possible | |
1234. |
Half life period of a chemical reaction is |
A. | The time required to reduce the concentration of the reacting substance to half its initial value |
B. | Half of the space time of a reaction |
C. | Half of the residence time of a reaction |
D. | None of these |
Answer» B. Half of the space time of a reaction | |
1235. |
A space velocity of 5 hr-1 means that |
A. | Five reactor volumes of feed (at specified conditions) are being fed into the reactor per hour |
B. | After every 5 hours, reactor is being filled with the feed |
C. | Cent per cent conversion can be achieved in at least 5 hours |
D. | A fixed conversion of a given batch of feed takes 5 hours |
Answer» B. After every 5 hours, reactor is being filled with the feed | |
1236. |
In a continuous flow stirred tank reactor, the composition of the exit stream |
A. | Is same as that in the reactor |
B. | Is different than that in the reactor |
C. | Depends upon the flow rate of inlet stream |
D. | None of these |
Answer» B. Is different than that in the reactor | |
1237. |
The reaction A → B is conducted in an adiabatic plug flow reactor (PFR). Pure A at a concentration of 2 kmol/m3 is fed to the reactor at the rate of 0.01 m3 /s and at a temperature of 500 K. If the exit conversion is 20%, then the exit temperature (in k) is (Data: Heat of reaction at 298 K = - 50000 kJ/ kmole of A reacted Heat capacities CPA = CPB = 100kJ/kmole. K (may be assumed to be independent of temperature)) |
A. | 400 |
B. | 500 |
C. | 600 |
D. | 1000 |
Answer» D. 1000 | |
1238. |
Kinetics of a catalytic reaction can be best studied on a/an __________ reactor. |
A. | Mixed |
B. | Integral (plug flow) |
C. | Differential (flow) |
D. | Either (A), (B) and (C) |
Answer» E. | |
1239. |
Pick out the wrong statement pertaining to space velocity of flow reactors. |
A. | The unit of space velocity is (time)-1 |
B. | The space velocity of 3 hr-1 means that three reactor volumes of feed at specified conditions are being fed into the reactor every hour |
C. | The space velocity of 3 hr-1 means that one third reactor volume of feed at specified conditions are being fed into the reactor |
D. | None of these |
Answer» D. None of these | |
1240. |
Equilibrium of a chemical reaction as viewed by kinetics is a __________ state. |
A. | Dynamic steady |
B. | Static steady |
C. | Dynamic unsteady |
D. | None of these |
Answer» B. Static steady | |
1241. |
For the non catalytic reaction of particles with surrounding fluid, the same needed to achieve the same fractional conversion for particles of different unchanging sizes is proportional to the particle diameter, when the __________ is the controlling resistance. |
A. | Film diffusion |
B. | Diffusion through ash layer |
C. | Chemical reaction |
D. | Either (A), (B) or (C) |
Answer» D. Either (A), (B) or (C) | |
1242. |
A pollutant P degrades according to first order kinetics. An aqueous stream containing P at 2 kmole/m3 and volumetric flow rate 1m3 /h requires a mixed flow reactor of volume V to bring down the pollutant level to 0.5 kmole/m3 . The inlet concentration of the pollutant is now doubled and the volumetric flow rate is tripled. If the pollutant level is to be brought down to the same level of 0.5 k.mole/m3 , the volume of the mixed flow reactor should be increased by a factor of: |
A. | 7 |
B. | 6 |
C. | 3 |
D. | 7/3 |
Answer» B. 6 | |
1243. |
For every 10°C rise in temperature, the rate of chemical reaction doubles. When the temperature is increased from 30 to 70°C, the rate of reaction increases __________ times. |
A. | 8 |
B. | 12 |
C. | 16 |
D. | 32 |
Answer» D. 32 | |
1244. |
In Langmuir treatment of adsorption, |
A. | Whole surface of the catalyst does not have the same activity for adsorption and there is attraction between the adsorbed molecule |
B. | Whole surface of the catalyst is essentially uniform and the adsorbed molecule has no effect on the rate of adsorption per site |
C. | All the adsorption does not take place by the same mechanism |
D. | Extent of adsorption is more than one complete monomolecular layer on the surface |
Answer» C. All the adsorption does not take place by the same mechanism | |
1245. |
Which of the following resistances is not involved in a gas phase catalytic (gas-solid) reaction? |
A. | Ash resistance |
B. | Gas film and pore surface diffusion resistances for reactants |
C. | Surface phenomenon resistance |
D. | Gas film and pore surface diffusion resistances for products |
Answer» B. Gas film and pore surface diffusion resistances for reactants | |
1246. |
The minimum energy required to allow a chemical reaction to proceed is termed as the 'threshold energy '. Chemical reactions with low activation energy are: |
A. | Always irreversible |
B. | Insensitive to temperature changes |
C. | Mostly irreversible |
D. | Highly temperature sensitive |
Answer» C. Mostly irreversible | |
1247. |
A liquid decomposes by irreversible first order kinetics and the half life period of this reaction is 8 minutes. The time required for 75% conversion of the liquid will be __________ minutes. |
A. | 4 |
B. | 8 |
C. | 12 |
D. | 16 |
Answer» E. | |
1248. |
Threshold energy in a reaction is equal to the |
A. | Activation energy |
B. | Normal energy of reactants |
C. | Sum of (A) & (B) |
D. | Neither (A) nor (B) |
Answer» D. Neither (A) nor (B) | |
1249. |
Fluidised bed reactor is characterised by |
A. | Uniformity of temperature |
B. | Comparatively smaller equipment |
C. | Very small pressure drop |
D. | Absence of continuous catalyst regeneration facility |
Answer» B. Comparatively smaller equipment | |
1250. |
A first order irreversible reaction, A → B is carried out separately in a constant volume as well as in a variable volume reactor for a particular period. It signifies that __________ in the two reactors. |
A. | Both conversion as well as concentration are same |
B. | Conversion in both will be the same but concentrations will be different |
C. | Both the conversion as well as concentrations will be different |
D. | None of these |
Answer» C. Both the conversion as well as concentrations will be different | |