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Just answer one question with steps. I have process so far. I am not sure how to solve. Help and fix my problem.product
4. A liquid catalyst is used to form methanol (gas) from CO and H. The catalyst liquid is removed from the
reactor, pumped through a heat exchanger to remove the heat of reaction, and then returned to the reactor.
One thousand mol/hr of feed gas enters the reactor at 25°C and is composed of 40 mol% N, 22 mol% CO and
38 mol% H. The product gas outlet is at 100°C. The relevant specific heat of reaction is -90.68 kJ/mol CO) at
STP and all species are gases
a. If 95% of the H, fed to the reactor is converted to methanol, what is the flow rate (mol/hr) and
composition (mol%) of the product gas stream?
b. How much heat (kW) must be removed from the catalyst?
c. Assuming no heat exchange occurs in the pump, at what temperature does the catalyst enter the heat
exchanger?
I
d. The heat is absorbed by cooling water that enters the heat exchanger at 25°C and exits at 45°C. The
catalyst liquid has a C. = 0.8 Btu/(lb-°F), exits the heat exchanger at 40°C. What are the flow rates
(kg/hr) of the catalyst liquid and cooling water through the heat exchanger? The catalyst liquid and
cooling water do not mix.
XPs can earn extra credit for an individual and should be submitted individually for grading. XPs are optional
and XP 22 and 23 can be solved independently.
An average person breaths 16 times per minute. Approximately one pint of air containing 0.04 mol% CO, is
inhaled per breath. The gas exhaled contains 4.0 mol% CO,. The specific heat of reaction for C + 0, – CO, is
393 5 kulmol C) at STP and all species are gases
0 nersen. Assume that elemental carbon is
background
Clear frame
(h
(
Hin
Hou
0 –
cu HIV 10.5
2
22
schon
19
QT
z
54.5
COW 39,5
N2V) 400
OON
ine kov
COS
o Gos Teed
Oy
T. 23°c
W Produd com
STP (Tooc p-lain
0C )
Ch 243-16-e’. LMS
+0.3015 (1000
)
= 4.7.1×1
Hz: 2,64*10(16-ci + iptv 10-07-25ml
co: 23.01-3, 1000 orang-oo-o. 292k5ml
– 14 /
2 200 1 wo-o +0.2109 x 18 (10o-o)?
h goc
6 cota
② rechhod coloryal
UN 09
Yoo 0.22
20.5
2
0.63
DU
43/
3/mit to
SHasyuas) (1943)+(526X242)* OYLA) = 2.942er/hr
+(X-45)
-1918243
5.44 kW (ro)
as H₂ converted to melhanol
60
361
1000 Co.se) 360 X.25
CH3OH
CO +212
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380-CI 192
3L1 mol H₂
Imolco
w pou sagt
9. Ач
0)
– BA -)
WY
400 – LYN2
heye
>
>
361 mol Hal
180.5 tlhych0H
Imol Chon
2. W

o 90°c
po
220 – 180.5 = 30.5 used
co
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Na
10 6 4 9 + 400+ 9.5 – 89
0031

web
yeu 0.28
– 0:03
yoo. 0.06
9N2- 0.6
W: 3.4610 (5-2)* **(us-7512.047*17.1
con 80.7 ..(10)
-1120
30.5-220
180.5
2

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