Equations Giving the Molar Flow of Different Molecules Linked By a Reaction
In this article, we will explore the equations that give the molar flow of different molecules linked by a reaction. We will consider a steady-state CSTR, where the reaction:
aA + bB <--> cC
is taking place. Here, a, b, and c are the stoichiometric coefficients for the species A, B, and C, respectively. We will also use the following notations:
Fi is the molar flow of species i,
r is the rate of reaction,
V is the volume,
X is the conversion at the end of the reactor,
νi is the stoichiometric coefficient of species i, and
ξ is the extent of reaction.
Mass Balance Equation
To derive the equations giving the molar flow of species A, B, and C, we will start by writing the mass balance equation:
IN + PROD - CONS = OUT + VAR
where IN, PROD, and CONS are the molar flows of species A and B going into the reactor and the molar flow of species C produced by the reaction, respectively. OUT is the molar flow of all species leaving the reactor, and VAR is any accumulation in the reactor volume. From this equation, we can write:
FA,in + 0 - a r V = FA,out
FB,in + 0 - b r V = FB,out
FC,in + c r V - 0 = FC,out
where F[i,in] is the molar flow of species i entering the reactor, and F[i,out] is the molar flow of species i leaving the reactor.
Equations for Species A and B
Using the expression for the extent of reaction, ξ, we can write:
ξ = - r V = - X (FA,in/νA) = -X(FB,in/νB)
This gives us:
FA,out = FA,in - a r V = FA,in + a ξ = FA,in - a X (FA,in/νA) = (1 - X) FA,in
FB,out = FB,in - b r V = FB,in + b ξ = FB,in - b X (FA,in/νA) = (1 - X) FB,in
These are the equations for the molar flow of species A and B.
The Problem with Species C
Now, let’s derive the equation giving the molar flow of species C:
FC,out = FC,in + c r V = FC,in - c ξ = FC,in + c X (FC,in/νC) = (1 + X) FC,in
At first glance, this equation seems to be correct, but if we think about it, we realize that it is not. It states that if there is no C at the beginning, there is no C produced at all, which is obviously wrong. So, where did we go wrong?
The Correct Equation for Species C
The correct equation for the molar flow of species C can be derived by noting that:
Substituting this expression into the mass balance equation for species C, we get:
FC,out = FC,in + c r V = (FA,in/νA) (c/b) (1 - X)/(X) + c ξ = FC,in [1 + c/b (1 - X)/X] = FC,in(1 + X)/(1 - X b/a)
This is the correct equation for the molar flow of species C.
Conclusion
In conclusion, we have derived the equations giving the molar flow of different molecules linked by a reaction in a steady-state CSTR. We have shown that the equations for species A and B are given by (1 – X) Fi,in, while the equation for species C is given by FC,in(1 + X)/(1 – X b/a). It is important to note that the equation for species C is different from what we originally derived, and the correct equation takes into account the fact that species C can be produced even if there is no C at the beginning.
What are the Equations Giving the Molar Flow of Different Molecules Linked By a Reaction?
Equations Giving the Molar Flow of Different Molecules Linked By a Reaction
In this article, we will explore the equations that give the molar flow of different molecules linked by a reaction. We will consider a steady-state CSTR, where the reaction:
is taking place. Here,
a
,b
, andc
are the stoichiometric coefficients for the speciesA
,B
, andC
, respectively. We will also use the following notations:Fi
is the molar flow of speciesi
,r
is the rate of reaction,V
is the volume,X
is the conversion at the end of the reactor,νi
is the stoichiometric coefficient of speciesi
, andξ
is the extent of reaction.Mass Balance Equation
To derive the equations giving the molar flow of species
A
,B
, andC
, we will start by writing the mass balance equation:where
IN
,PROD
, andCONS
are the molar flows of speciesA
andB
going into the reactor and the molar flow of speciesC
produced by the reaction, respectively.OUT
is the molar flow of all species leaving the reactor, andVAR
is any accumulation in the reactor volume. From this equation, we can write:where
F[i,in]
is the molar flow of speciesi
entering the reactor, andF[i,out]
is the molar flow of speciesi
leaving the reactor.Equations for Species A and B
Using the expression for the extent of reaction,
ξ
, we can write:This gives us:
These are the equations for the molar flow of species
A
andB
.The Problem with Species C
Now, let’s derive the equation giving the molar flow of species
C
:At first glance, this equation seems to be correct, but if we think about it, we realize that it is not. It states that if there is no
C
at the beginning, there is noC
produced at all, which is obviously wrong. So, where did we go wrong?The Correct Equation for Species C
The correct equation for the molar flow of species
C
can be derived by noting that:From this, we can express
F[C,in]
as:Substituting this expression into the mass balance equation for species
C
, we get:This is the correct equation for the molar flow of species
C
.Conclusion
In conclusion, we have derived the equations giving the molar flow of different molecules linked by a reaction in a steady-state CSTR. We have shown that the equations for species
A
andB
are given by (1 – X) Fi,in, while the equation for speciesC
is given by FC,in(1 + X)/(1 – X b/a). It is important to note that the equation for speciesC
is different from what we originally derived, and the correct equation takes into account the fact that speciesC
can be produced even if there is noC
at the beginning.