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| [ | |
| { | |
| "id": 1, | |
| "question": "What does a material balance primarily apply?", | |
| "options": ["Conservation of energy", "Conservation of mass", "Conservation of momentum", "Conservation of volume"], | |
| "answer": "Conservation of mass" | |
| }, | |
| { | |
| "id": 2, | |
| "question": "In chemical engineering, a system is defined as:", | |
| "options": ["The entire universe", "A specified portion of matter under study", "Only open processes", "Any equipment used"], | |
| "answer": "A specified portion of matter under study" | |
| }, | |
| { | |
| "id": 3, | |
| "question": "The imaginary surface that separates a system from its surroundings is called:", | |
| "options": ["Control volume", "Boundary", "Interface", "Surface tension"], | |
| "answer": "Boundary" | |
| }, | |
| { | |
| "id": 4, | |
| "question": "Which law is the basis of material balances?", | |
| "options": ["Law of conservation of energy", "Law of conservation of entropy", "Law of conservation of mass", "Law of definite proportions"], | |
| "answer": "Law of conservation of mass" | |
| }, | |
| { | |
| "id": 5, | |
| "question": "Which type of process has no mass entering or leaving during operation?", | |
| "options": ["Batch process", "Continuous process", "Semi-batch process", "Cyclic process"], | |
| "answer": "Batch process" | |
| }, | |
| { | |
| "id": 6, | |
| "question": "In a continuous process, the system operates:", | |
| "options": ["With intermittent input", "With constant inflow and outflow", "With no inflow", "Only in cycles"], | |
| "answer": "With constant inflow and outflow" | |
| }, | |
| { | |
| "id": 7, | |
| "question": "A semi-batch process is best described as:", | |
| "options": ["No inflow or outflow", "Continuous inflow and outflow", "Either inflow or outflow but not both", "No chemical reaction"], | |
| "answer": "Either inflow or outflow but not both" | |
| }, | |
| { | |
| "id": 8, | |
| "question": "The surroundings of a system include:", | |
| "options": ["Only air", "Everything external to the system boundary", "The same molecules in the system", "The equipment walls only"], | |
| "answer": "Everything external to the system boundary" | |
| }, | |
| { | |
| "id": 9, | |
| "question": "Material balance can be expressed mathematically as:", | |
| "options": ["Input + Output = Accumulation", "Input – Output + Generation – Consumption = Accumulation", "Input × Output = Accumulation", "Input + Energy = Accumulation"], | |
| "answer": "Input – Output + Generation – Consumption = Accumulation" | |
| }, | |
| { | |
| "id": 10, | |
| "question": "If a system is at steady state, then:", | |
| "options": ["Accumulation term is zero", "Input is zero", "Output is zero", "Generation is zero"], | |
| "answer": "Accumulation term is zero" | |
| }, | |
| { | |
| "id": 11, | |
| "question": "Which of the following is a closed system?", | |
| "options": ["A boiling pot with lid", "A running distillation column", "A cooling tower", "An open water tank"], | |
| "answer": "A boiling pot with lid" | |
| }, | |
| { | |
| "id": 12, | |
| "question": "An open system is also known as:", | |
| "options": ["Isolated system", "Control volume", "Closed vessel", "Batch system"], | |
| "answer": "Control volume" | |
| }, | |
| { | |
| "id": 13, | |
| "question": "The law of conservation of mass implies:", | |
| "options": ["Matter can be destroyed", "Mass remains constant in physical and chemical changes", "Mass decreases in reactions", "Energy converts into mass"], | |
| "answer": "Mass remains constant in physical and chemical changes" | |
| }, | |
| { | |
| "id": 14, | |
| "question": "In which process is there no mass transfer across boundaries?", | |
| "options": ["Open system", "Isolated system", "Continuous system", "Semi-batch process"], | |
| "answer": "Isolated system" | |
| }, | |
| { | |
| "id": 15, | |
| "question": "Which of the following is NOT an assumption in material balances?", | |
| "options": ["Perfect mixing", "Constant density", "Instantaneous reaction", "No conservation of mass"], | |
| "answer": "No conservation of mass" | |
| }, | |
| { | |
| "id": 16, | |
| "question": "In batch processes, material balances are generally performed:", | |
| "options": ["On a time-average basis", "Over the whole duration of the process", "At steady state only", "Only for gaseous systems"], | |
| "answer": "Over the whole duration of the process" | |
| }, | |
| { | |
| "id": 17, | |
| "question": "In continuous processes, balances are often performed:", | |
| "options": ["At steady state", "During shutdown only", "Only for solids", "Only in laboratory scale"], | |
| "answer": "At steady state" | |
| }, | |
| { | |
| "id": 18, | |
| "question": "Which type of system exchanges neither mass nor energy with surroundings?", | |
| "options": ["Closed system", "Open system", "Isolated system", "Semi-batch process"], | |
| "answer": "Isolated system" | |
| }, | |
| { | |
| "id": 19, | |
| "question": "The mass balance equation reduces to Input = Output when:", | |
| "options": ["At steady state with no reaction", "At unsteady state", "When generation occurs", "When accumulation occurs"], | |
| "answer": "At steady state with no reaction" | |
| }, | |
| { | |
| "id": 20, | |
| "question": "A control mass approach is generally applied to:", | |
| "options": ["Closed systems", "Open systems", "Continuous reactors", "Steady flow systems"], | |
| "answer": "Closed systems" | |
| }, | |
| { | |
| "id": 21, | |
| "question": "A control volume approach is applied to:", | |
| "options": ["Closed systems", "Open systems", "Isolated systems", "Batch processes only"], | |
| "answer": "Open systems" | |
| }, | |
| { | |
| "id": 22, | |
| "question": "If 100 kg of reactant is fed and 80 kg of product is obtained, what is the material lost?", | |
| "options": ["10 kg", "20 kg", "80 kg", "100 kg"], | |
| "answer": "20 kg" | |
| }, | |
| { | |
| "id": 23, | |
| "question": "A balance on a semi-batch reactor considers:", | |
| "options": ["No inflow or outflow", "Only energy balances", "Either inflow or outflow", "Both inflow and outflow continuously"], | |
| "answer": "Either inflow or outflow" | |
| }, | |
| { | |
| "id": 24, | |
| "question": "If accumulation is positive, it means:", | |
| "options": ["System mass is decreasing", "System mass is increasing", "Steady state is reached", "No reaction is occurring"], | |
| "answer": "System mass is increasing" | |
| }, | |
| { | |
| "id": 25, | |
| "question": "If accumulation is zero, the system is said to be:", | |
| "options": ["At steady state", "Unsteady", "Batch operated", "Reacting"], | |
| "answer": "At steady state" | |
| }, | |
| { | |
| "id": 26, | |
| "question": "A system where both input and output occur but accumulation is zero is:", | |
| "options": ["Batch", "Continuous steady state", "Semi-batch", "Isolated"], | |
| "answer": "Continuous steady state" | |
| }, | |
| { | |
| "id": 27, | |
| "question": "Which of the following is an example of a batch process?", | |
| "options": ["Fermentation tank", "Petroleum refinery", "Paper manufacturing", "Power plant"], | |
| "answer": "Fermentation tank" | |
| }, | |
| { | |
| "id": 28, | |
| "question": "Which of the following is an example of a continuous process?", | |
| "options": ["Cooking rice in a cooker", "Sugar production", "Distillation column in operation", "Pharmaceutical mixing"], | |
| "answer": "Distillation column in operation" | |
| }, | |
| { | |
| "id": 29, | |
| "question": "Which of the following is an example of semi-batch process?", | |
| "options": ["Boiler furnace", "Chlorination of water with continuous gas supply", "Refinery distillation column", "Gas turbine"], | |
| "answer": "Chlorination of water with continuous gas supply" | |
| }, | |
| { | |
| "id": 30, | |
| "question": "Which process type is more suitable for large-scale production?", | |
| "options": ["Batch", "Continuous", "Semi-batch", "Isolated"], | |
| "answer": "Continuous" | |
| }, | |
| { | |
| "id": 31, | |
| "question": "Which process type is more flexible for small-scale production?", | |
| "options": ["Batch", "Continuous", "Semi-batch", "Isolated"], | |
| "answer": "Batch" | |
| }, | |
| { | |
| "id": 32, | |
| "question": "For material balance, the general rule is:", | |
| "options": ["Mass in = Mass out + Accumulation", "Mass in = Mass out", "Mass in > Mass out", "Mass in < Mass out"], | |
| "answer": "Mass in = Mass out + Accumulation" | |
| }, | |
| { | |
| "id": 33, | |
| "question": "Which of the following requires time-dependent balance?", | |
| "options": ["Steady state", "Unsteady state", "Isolated systems", "Continuous refinery"], | |
| "answer": "Unsteady state" | |
| }, | |
| { | |
| "id": 34, | |
| "question": "In which type of system is boundary fixed in space?", | |
| "options": ["Control mass system", "Control volume system", "Isolated system", "Batch process"], | |
| "answer": "Control volume system" | |
| }, | |
| { | |
| "id": 35, | |
| "question": "Which system has a moving boundary?", | |
| "options": ["Control mass system", "Control volume system", "Isolated system", "Continuous process"], | |
| "answer": "Control mass system" | |
| }, | |
| { | |
| "id": 36, | |
| "question": "Which of the following best explains semi-batch?", | |
| "options": ["Time-independent", "Combination of batch and continuous", "Closed system", "Energy balance only"], | |
| "answer": "Combination of batch and continuous" | |
| }, | |
| { | |
| "id": 37, | |
| "question": "If output > input in a balance, then accumulation is:", | |
| "options": ["Positive", "Negative", "Zero", "Infinite"], | |
| "answer": "Negative" | |
| }, | |
| { | |
| "id": 38, | |
| "question": "If input = output, then accumulation is:", | |
| "options": ["Zero", "Positive", "Negative", "Unsteady"], | |
| "answer": "Zero" | |
| }, | |
| { | |
| "id": 39, | |
| "question": "If a reaction generates mass, which term in the balance is positive?", | |
| "options": ["Generation", "Consumption", "Input", "Output"], | |
| "answer": "Generation" | |
| }, | |
| { | |
| "id": 40, | |
| "question": "Which type of material balance is easiest to perform?", | |
| "options": ["Batch without reaction", "Continuous with reaction", "Semi-batch with accumulation", "Unsteady reactive system"], | |
| "answer": "Batch without reaction" | |
| }, | |
| { | |
| "id": 1, | |
| "question": "What does the law of conservation of mass state in material balances?", | |
| "options": [ | |
| "Mass can be created or destroyed depending on the process", | |
| "Mass can neither be created nor destroyed in a closed system", | |
| "Mass is always lost in chemical processes", | |
| "Mass depends on the type of material" | |
| ], | |
| "answer": "Mass can neither be created nor destroyed in a closed system" | |
| }, | |
| { | |
| "id": 2, | |
| "question": "In a single-unit material balance, the general form is:", | |
| "options": [ | |
| "Input = Output + Accumulation", | |
| "Input - Output = 0", | |
| "Input + Output = Accumulation", | |
| "Input = Output - Generation" | |
| ], | |
| "answer": "Input = Output + Accumulation" | |
| }, | |
| { | |
| "id": 3, | |
| "question": "Which of the following is true for a steady-state process?", | |
| "options": [ | |
| "Mass accumulation is not zero", | |
| "Mass accumulation is zero", | |
| "Energy accumulation is infinite", | |
| "Process variables change with time" | |
| ], | |
| "answer": "Mass accumulation is zero" | |
| }, | |
| { | |
| "id": 4, | |
| "question": "Which of these is an example of a single-unit operation?", | |
| "options": [ | |
| "A distillation column with recycle", | |
| "A simple mixer with two inlets and one outlet", | |
| "A process with recycle and purge streams", | |
| "A complex multi-reactor system" | |
| ], | |
| "answer": "A simple mixer with two inlets and one outlet" | |
| }, | |
| { | |
| "id": 5, | |
| "question": "In multiple-unit processes, material balances are usually solved by:", | |
| "options": [ | |
| "Writing separate balances for each unit", | |
| "Writing only an overall balance", | |
| "Ignoring the recycle streams", | |
| "Only using bypass calculations" | |
| ], | |
| "answer": "Writing separate balances for each unit" | |
| }, | |
| { | |
| "id": 6, | |
| "question": "The purpose of a recycle stream is to:", | |
| "options": [ | |
| "Increase raw material consumption", | |
| "Improve conversion and reduce waste", | |
| "Decrease product purity", | |
| "Reduce process cost always" | |
| ], | |
| "answer": "Improve conversion and reduce waste" | |
| }, | |
| { | |
| "id": 7, | |
| "question": "What is a bypass stream?", | |
| "options": [ | |
| "A stream that passes around part of a process unit", | |
| "A stream that goes through the entire process", | |
| "A stream that is purged to remove impurities", | |
| "A recycle stream from the reactor" | |
| ], | |
| "answer": "A stream that passes around part of a process unit" | |
| }, | |
| { | |
| "id": 8, | |
| "question": "Why is a purge stream necessary in recycle systems?", | |
| "options": [ | |
| "To increase the flow rate", | |
| "To remove inert or undesired materials that may accumulate", | |
| "To improve heat transfer efficiency", | |
| "To maximize energy efficiency" | |
| ], | |
| "answer": "To remove inert or undesired materials that may accumulate" | |
| }, | |
| { | |
| "id": 9, | |
| "question": "Which of these represents an unsteady-state balance?", | |
| "options": [ | |
| "Input = Output", | |
| "Input - Output = Accumulation", | |
| "Input = Output + 0", | |
| "Input + Output = Accumulation + 0" | |
| ], | |
| "answer": "Input - Output = Accumulation" | |
| }, | |
| { | |
| "id": 10, | |
| "question": "At steady-state, the accumulation term in the material balance equation is:", | |
| "options": [ | |
| "Zero", | |
| "Positive", | |
| "Negative", | |
| "Infinite" | |
| ], | |
| "answer": "Zero" | |
| }, | |
| { | |
| "id": 11, | |
| "question": "Which of the following is an example of a purge requirement?", | |
| "options": [ | |
| "Accumulation of inert gases in an ammonia synthesis loop", | |
| "Accumulation of heat in a heat exchanger", | |
| "Accumulation of reactants in a distillation column", | |
| "Accumulation of pressure in a compressor" | |
| ], | |
| "answer": "Accumulation of inert gases in an ammonia synthesis loop" | |
| }, | |
| { | |
| "id": 12, | |
| "question": "In a material balance without chemical reaction, which terms are absent?", | |
| "options": [ | |
| "Generation and Consumption terms", | |
| "Input and Output terms", | |
| "Accumulation terms", | |
| "Flow terms" | |
| ], | |
| "answer": "Generation and Consumption terms" | |
| }, | |
| { | |
| "id": 13, | |
| "question": "Which of these processes is unsteady-state?", | |
| "options": [ | |
| "Filling a tank", | |
| "Continuous distillation at constant feed", | |
| "Evaporation at constant rate", | |
| "Heat exchanger at steady operation" | |
| ], | |
| "answer": "Filling a tank" | |
| }, | |
| { | |
| "id": 14, | |
| "question": "In multiple-unit balances, the best approach is:", | |
| "options": [ | |
| "Solve each unit separately and then combine results", | |
| "Ignore intermediate units", | |
| "Write only one overall balance", | |
| "Use only trial-and-error methods" | |
| ], | |
| "answer": "Solve each unit separately and then combine results" | |
| }, | |
| { | |
| "id": 15, | |
| "question": "Recycle ratio is defined as:", | |
| "options": [ | |
| "Recycle flow rate / Fresh feed flow rate", | |
| "Fresh feed flow rate / Product flow rate", | |
| "Product flow rate / Recycle flow rate", | |
| "Recycle flow rate × Fresh feed flow rate" | |
| ], | |
| "answer": "Recycle flow rate / Fresh feed flow rate" | |
| }, | |
| { | |
| "id": 16, | |
| "question": "Which of these is NOT a reason to use recycle?", | |
| "options": [ | |
| "To improve conversion", | |
| "To save energy", | |
| "To remove inerts", | |
| "To increase raw material consumption" | |
| ], | |
| "answer": "To increase raw material consumption" | |
| }, | |
| { | |
| "id": 17, | |
| "question": "If the process is at unsteady-state, what happens to accumulation?", | |
| "options": [ | |
| "It remains zero", | |
| "It becomes non-zero", | |
| "It is undefined", | |
| "It is negative only" | |
| ], | |
| "answer": "It becomes non-zero" | |
| }, | |
| { | |
| "id": 18, | |
| "question": "Which of these operations often requires a bypass?", | |
| "options": [ | |
| "Heat exchanger for temperature control", | |
| "Mixer for uniform blending", | |
| "Reactor for maximum conversion", | |
| "Separator for purity increase" | |
| ], | |
| "answer": "Heat exchanger for temperature control" | |
| }, | |
| { | |
| "id": 19, | |
| "question": "What type of balance is applied to a tank being drained without inflow?", | |
| "options": [ | |
| "Steady-state balance", | |
| "Unsteady-state balance", | |
| "Overall balance", | |
| "Multiple-unit balance" | |
| ], | |
| "answer": "Unsteady-state balance" | |
| }, | |
| { | |
| "id": 20, | |
| "question": "In a process with a recycle and purge, the purge stream prevents:", | |
| "options": [ | |
| "Decrease in product flow", | |
| "Accumulation of inert gases", | |
| "Increase in recycle flow", | |
| "Excess energy usage" | |
| ], | |
| "answer": "Accumulation of inert gases" | |
| }, | |
| { | |
| "id": 21, | |
| "question": "For a mixing process without reaction, which equation applies?", | |
| "options": [ | |
| "Total input mass = Total output mass", | |
| "Total input mass ≠ Total output mass", | |
| "Total input = Generation + Output", | |
| "Total output = Input - Accumulation" | |
| ], | |
| "answer": "Total input mass = Total output mass" | |
| }, | |
| { | |
| "id": 22, | |
| "question": "Which of these is correct about steady-state?", | |
| "options": [ | |
| "Variables depend on time", | |
| "Mass accumulation is zero", | |
| "System is always closed", | |
| "No output exists" | |
| ], | |
| "answer": "Mass accumulation is zero" | |
| }, | |
| { | |
| "id": 23, | |
| "question": "In unsteady-state balances, time factor is:", | |
| "options": [ | |
| "Not important", | |
| "Important as variables change with time", | |
| "Always constant", | |
| "Used only in steady processes" | |
| ], | |
| "answer": "Important as variables change with time" | |
| }, | |
| { | |
| "id": 24, | |
| "question": "Which of these is an example of single-unit balance?", | |
| "options": [ | |
| "Evaporation of water in a single vessel", | |
| "Distillation with recycle", | |
| "Ammonia synthesis loop with purge", | |
| "A refinery process with multiple heaters" | |
| ], | |
| "answer": "Evaporation of water in a single vessel" | |
| }, | |
| { | |
| "id": 25, | |
| "question": "The main difference between overall and individual unit balances is:", | |
| "options": [ | |
| "Overall balance ignores internal flows", | |
| "Overall balance includes internal flows", | |
| "Unit balances are approximate", | |
| "Overall balances are less accurate" | |
| ], | |
| "answer": "Overall balance ignores internal flows" | |
| }, | |
| { | |
| "id": 26, | |
| "question": "Bypass is used mainly for:", | |
| "options": [ | |
| "Controlling process conditions", | |
| "Increasing reaction conversion", | |
| "Improving separation efficiency", | |
| "Reducing product purity" | |
| ], | |
| "answer": "Controlling process conditions" | |
| }, | |
| { | |
| "id": 27, | |
| "question": "In unsteady-state operation, accumulation can be:", | |
| "options": [ | |
| "Positive or negative", | |
| "Only positive", | |
| "Only zero", | |
| "Always infinite" | |
| ], | |
| "answer": "Positive or negative" | |
| }, | |
| { | |
| "id": 28, | |
| "question": "For a tank with inflow but no outflow, the mass balance shows:", | |
| "options": [ | |
| "Accumulation is zero", | |
| "Accumulation is equal to inflow", | |
| "Accumulation is negative", | |
| "Accumulation is undefined" | |
| ], | |
| "answer": "Accumulation is equal to inflow" | |
| }, | |
| { | |
| "id": 29, | |
| "question": "Which of these statements is true for multiple-unit systems?", | |
| "options": [ | |
| "Overall balances are sufficient to get all details", | |
| "Unit balances give more detailed stream information", | |
| "Recycle streams are not considered", | |
| "Purge streams are not important" | |
| ], | |
| "answer": "Unit balances give more detailed stream information" | |
| }, | |
| { | |
| "id": 30, | |
| "question": "When a tank is filled and then drained at equal rates, the system is:", | |
| "options": [ | |
| "At steady-state", | |
| "At unsteady-state", | |
| "Not balanced", | |
| "At accumulation only" | |
| ], | |
| "answer": "At steady-state" | |
| }, | |
| { | |
| "id": 31, | |
| "question": "Which of the following is an advantage of recycle?", | |
| "options": [ | |
| "Better raw material utilization", | |
| "Increase in waste", | |
| "Decrease in yield", | |
| "Reduction in efficiency" | |
| ], | |
| "answer": "Better raw material utilization" | |
| }, | |
| { | |
| "id": 32, | |
| "question": "What is true about purge in recycle systems?", | |
| "options": [ | |
| "It reduces product purity", | |
| "It removes accumulated inert gases", | |
| "It increases energy loss only", | |
| "It is unnecessary" | |
| ], | |
| "answer": "It removes accumulated inert gases" | |
| }, | |
| { | |
| "id": 33, | |
| "question": "In steady-state, the tank level:", | |
| "options": [ | |
| "Keeps increasing", | |
| "Keeps decreasing", | |
| "Remains constant", | |
| "Fluctuates randomly" | |
| ], | |
| "answer": "Remains constant" | |
| }, | |
| { | |
| "id": 34, | |
| "question": "In a bypass system, if 20% of feed bypasses the heater, the outlet temperature:", | |
| "options": [ | |
| "Will be lower than without bypass", | |
| "Will be higher than without bypass", | |
| "Will remain the same", | |
| "Will become unstable" | |
| ], | |
| "answer": "Will be lower than without bypass" | |
| }, | |
| { | |
| "id": 35, | |
| "question": "For a steady-state continuous process:", | |
| "options": [ | |
| "Input = Output", | |
| "Input ≠ Output", | |
| "Accumulation is infinite", | |
| "No output exists" | |
| ], | |
| "answer": "Input = Output" | |
| }, | |
| { | |
| "id": 36, | |
| "question": "Unsteady-state balances are required for:", | |
| "options": [ | |
| "Startup and shutdown processes", | |
| "Continuous operations at equilibrium", | |
| "Processes at constant flow", | |
| "Processes without feed" | |
| ], | |
| "answer": "Startup and shutdown processes" | |
| } | |
| ] | |