CRE section 4 Flashcards
(50 cards)
not involved in a gas phase catalytic rxn
ash resistance
if the time required to change the concentration of reactant to its original value is independent of the initial concentration, the order is
one
a batch adiabatic reqctor at an initual temp of 373 is being used for the rxn A -> B. the temp rise after a conversion of 0.5 will be
10°C
if CA is the quantity of reactants initially present, the quantity left after n half period will be equal to
(1/2)^n.CA
a photochemical rxn is
initiated by light
the rate controlling step for the heterogeneous irreversible catalytic rxn is the surface rxn absorbed A with absorbed B to give absorbed C. the rate expression for this rxn can be written as (pic)
(pic)
optimum performance of reactors operating in parallel is obtained when the feed stream is distributed in such a way that the
space time for each parallel line is same
a catalyst is said to be a negative catalyst if it
retards the rate of rxn
for the non catalytic rxn 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
chemical rxn
pure ethanol vapor is fed to a reactor packed with alumina catalyst at the rate of 100kmole / hr. the percent conversion of ethanol in the reactor is
100
the conversion for a second order irreversible rxn in batch mode is given by (pic)
pic
wrong statement (when the rxn rate)
when the rxn rate is independent of temperature, then order rxn is said to be of zero order
a backmix reactor
is same as ideal stirred tank reactor
rate of chemicla rxn is not influenced by the
number of molecules of reactant taking part in a rxn
wrong statement (residence time)
residence time for all the elements of fluid in case of PFR need not be same
the rxn AB is conducted in an adiabatic pfr. if the exit conversion is 20% then the exit temperature is
600
which is not a theory of homogeneous rxn
none if these
a first order homogeneous rxn of the type XYZ is carried out in a CSTR, which of the following curves respectively show the variation of the conc xyz with time
iii, ii, i
in a semi- batch reactor
velocity of rxn can be controlled
most important characteristics of gas-liquid reactors are the
both a and b
controlling factor in very fast heterogeneous rxn
heat and mass transfer effects
enzymes are destroyed when the
temperature is very high
for an autocatalytic reactor, the suitable reactor setup is
cstr followed by pfr
ionic rxn occur in
solutions