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8/10/2019 UH CHEE 2331 (Chemical Processes) HW1 Solutions Summer 2014
http://slidepdf.com/reader/full/uh-chee-2331-chemical-processes-hw1-solutions-summer-2014 1/3
CHEE 2331 Chemical Processing SUMMER 2014
HW 1
1.
An empirical equation is given to calculate the density of a fluid:
70.5exp8.2710
Where is density and P is pressure
.
a) What are the units for 70.5 8.27 10?
. .
b) Calculate the density in given pressure of 9 10
.
/
c) Derive a formula for as a function of
.
d) Check your solution to part (b)
2. A rectangular block of height L and horizontal cross-sectional area A floats at the
interface between two immiscible liquids, as shown below
8/10/2019 UH CHEE 2331 (Chemical Processes) HW1 Solutions Summer 2014
http://slidepdf.com/reader/full/uh-chee-2331-chemical-processes-hw1-solutions-summer-2014 2/3
3.
go
d
l
a) Deriv
final
b) Multi
appro
force
block
mercury m
as to a labone is not abl
ownstream
vel of merc
e a formula
, and t
esult)
le force bal
aches are eq
on the upp
and the buo
anometer (o
atory. Becae to see the
ressure is r
ury in the o
for , in te
e cross-sect
ances can b
ual. (i) in t
r and lower
yant force o
pen-end) is
use liquid plevel of ma
ad from a
en arm is 1
ms of fluid
onal area
e calculated
rms of the
block surfa
n the block
Type equa
connected t
aint was spiometer flui
ourdon gau
00 mm ab
densities
. (Note, all
on the bloc
eight of th
ces; and (ii)
as expresse
tion here.
a pressuri
lled on thein this ar
ge. A valu
ve the lowe
, ,
ariables m
. Prove th
block and
in terms of
by Archmi
ed pipeline
rm connect. With no
of 15 psi i
st part of th
, heights
y not appea
two follow
ydrostatic
the weight
des’ princip
which supp
d to the linas flow,
noted. The
manomete
r in
ing
f the
le.
ies
,
r.
8/10/2019 UH CHEE 2331 (Chemical Processes) HW1 Solutions Summer 2014
http://slidepdf.com/reader/full/uh-chee-2331-chemical-processes-hw1-solutions-summer-2014 3/3
a) Whe
How
conne
b) Whe
is the
No
the gas is n
igh above t
cted to the
gas is flow
gas present
pressure i
ot flowing,
he bottom o
ipe?
1
ng, the mer
(psig) at thi
tube has
he pressure
f the mano
*760/14.69
ury level i
moment?
ropped by
. g
is the same
eter would
6 + x = 120
the visible
100 mm. 1
everywhere
the mercur
0
arm drops b
5 psig – 10
in the pipe.
be in the a
y 50 mm.
mm*14.7/
m
hat
760