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You Are On Multi Choice Question Bank SET 359

17951. Shift conversion reaction





17952. The importance of diffusion in a catalyst are increased by





17953. A back mix reactor is





17954. Which one is the rate controlling step in a solid-gas non-catalytic reaction occurring at very high temperature?





17955. The rate of the heterogenous catalytic reaction A(g) + B(g) C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction is





17956. For a __________ order chemical reaction, , the half life period is independent of the initial concentration of the reactant A.





17957. The ratio of moles of a reactant converted into the desired product to that converted into unwanted product is called





17958. 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




17959. The eddy diffusivity for a liquid in plug flow must be





17960. For multiple reactions, the flow pattern within the vessel affects the





17961. The rate expression for the gaseous phase reaction, CO + 2H2 CH3OH, is given by, . Which of the following is not possible ?





17962. For the same residence time, which one will give the maximum conversion ?





17963. __________ gas is normally employed in B.E.T.method of finding out the surface area of catalyst.





17964. The exit age distribution curve E(t) for an ideal CSTR with the average residence time, τ, is given by



17965. The rate constant of a reaction depends on the





17966. For the reversible reaction A 2B, if the equilibrium constant K is 0.05 mole/litre; starting from initially 2 moles of A and zero moles of B, how many moles will be formed at equilibrium ?





17967. For identical flow rate and feed composition, X plug flow reactors (PER) in series with a total volume V gives the same conversion as single





17968. Time required for 50% decomposition of a liquid in an isothermal batch reactor following first order kinetics is 2 minutes. The time required for 75% decomposition will be about __________ minutes.





17969. For a __________ order reaction, the units of rate constant and rate of reaction are the same.





17970. In case of staged packed bed reactors carrying out exothermic reaction, use





17971. Vegetable oils are hydrogenated in a __________ reactor.





17972. Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is





17973. The rate of reaction does not decrease appreciably as the reaction proceeds in case of __________ reactions.





17974. For all positive reaction orders for a particular duty,





17975. The heat of reaction





17976. Which of the following does not produce a change in the value of rate constant of a reaction ?





17977. With increase in temperature, the equilibrium conversion of a reversible exothermic reaction





17978. In a CSTR __________ varies with time.





17979. The following gas phase reactions are carried out isothermally in a CSTR. A 2R ; r1 = k1pA ; k1 = 20mole/(sec.m3 bar) A 3S ; r2 = k2 pA ; k2 = 40mole/(sec.m3 .bar) What is the maximum possible value of FR(mole/sec.) ?





17980. As the chemical reaction proceeds, the rate of reaction





17981. Sales-Rs.1,00,000/-Profit is 25% on cost.Total cost is Rs.





17982. In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume.




17983. Photo-chemical reactions occur in presence of





17984. 'n' number of plug flow reactors (P.F.R) in series with a total volume 'V' gives the same conversion as one P.F.R. of volume





17985. Knudsen diffusion is directly proportional to





17986. Fractional conversion __________ for an exothermic reversible chemical reaction, when the temperature is maximum.





17987. Non-catalytic fluid-solid reactions are represented by __________ model.





17988. A pulse tracer is introduced in an ideal CSTR (with a mean residence time ι) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be





17989. On application of pressure to the equilibrium system, ice water ; which of the following phenomenon will occur ?





17990. Participation of __________ is involved in the occurrence of a chemical reaction.





17991. Promoter.





17992. The rate constant of a reaction is a function of the





17993. Mean residence time is equal to the space time, when





17994. If 'n' is the order of reaction, then unit of rate constant is





17995. Which accounting concept considers that the firm has an indefinite life?





17996. The value of 'n' for a chemical reaction A B, whose reaction rate is CAn, will be __________ if the rate of the reaction increases by a factor of 8, when the concentration of is doubled.





17997. With the same reaction time, initial concentration and feed rate, the reaction 2A B is carried out separately in CSTR and P.F. reactor of equal volumes. The conversion will be




17998. For any reaction, we may write conversion as a function of





17999. The use of space time is preferred over the mean residence time in the design of a/an





18000. Autocatalytic reactions are best carried out in a





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