463
13.1 Mean Line Analysis
So, the conventional loss is the loss the flow would be subjected to, if density were
constant.
In order to express the conventional loss with a compressible fluid, a process
average density may be defined by
In a compression process, this average density only slightly deviates from the arithmetic average density.
or
= −
−
= −
irr
irr
1
1
0 dh
dp dq
dq
dh
dp.
r
r
For = con
r
stant :
o
=
=
s
s
1
1
dh
dp,
h
p.
D
D
r
r
r
So :
=
−
=
−
irr
s
1
q
h
p
h
h .
D
D
D D
r
or
.
∆
∆
∆ =
= ∆
s
m
m
s
p
p
h
h
r
r
As
,
1 n
n
2
2
1
1
p
p ~
p
→
=
r
r
r
1/
1
2
1
2 1
it follows
1/2 (
) 1/2 (1
), with
/ .
n
r
r
r p p
r
r r
r
=
+
=
+
=
( 1)/
2
2
1
1
1
1
From
1
(
1),
−
− =
− =
−
s
s
h
h
h h
h r
h
g
g
1
1
( 1)/
( 1)/
1
( 1)
1
1
it follows
.
(
1)
1
−
−
−
−
−
=
=
−
−
m
p
p r
r
C T r
r
g
g
g
g
g
r
r g
Fig. 13.3 h-s diagram of a
compressor stage
13.1 Mean Line Analysis
So, the conventional loss is the loss the flow would be subjected to, if density were
constant.
In order to express the conventional loss with a compressible fluid, a process
average density may be defined by
In a compression process, this average density only slightly deviates from the arithmetic average density.
or
= −
−
= −
irr
irr
1
1
0 dh
dp dq
dq
dh
dp.
r
r
For = con
r
stant :
o
=
=
s
s
1
1
dh
dp,
h
p.
D
D
r
r
r
So :
=
−
=
−
irr
s
1
q
h
p
h
h .
D
D
D D
r
or
.
∆
∆
∆ =
= ∆
s
m
m
s
p
p
h
h
r
r
As
,
1 n
n
2
2
1
1
p
p ~
p
→
=
r
r
r
1/
1
2
1
2 1
it follows
1/2 (
) 1/2 (1
), with
/ .
n
r
r
r p p
r
r r
r
=
+
=
+
=
( 1)/
2
2
1
1
1
1
From
1
(
1),
−
− =
− =
−
s
s
h
h
h h
h r
h
g
g
1
1
( 1)/
( 1)/
1
( 1)
1
1
it follows
.
(
1)
1
−
−
−
−
−
=
=
−
−
m
p
p r
r
C T r
r
g
g
g
g
g
r
r g
Fig. 13.3 h-s diagram of a
compressor stage
