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Title: Material%20Balance%20(????????????????)


1
Material Balance (????????????????)
  • ????????????? ??????????????????????????
  • ???? (System) ???? ????????????????????????
    ?????????????????????? (System Boundary)
    ??????????????????????????????

2
Quiz 6
  • Antimony (Sb) is obtained by heating pulverized
    stibnite (Sb2S3) with scrap iron and drawing off
    the molten antimony from the bottom of the
    reaction vessel.
  • Sb2S3 Fe ? 2 Sb 3 FeS
  • Sppose that 0.600 kg of stibnite and 0.250 kg of
    iron turnings are heated together to give 0.200
    kg of Sb metal. Determine
  • the limiting reactant
  • the percentage of excess reactant
  • the degree of completion
  • the percen conversion based on
  • the yield in kg Sb produced / kg Sb2S3 fed to the
    reactor.

3
??????? ????????
  • ??????????????????????? ??????????????????????????
    ????????

?????????????????????????????????????????
Q, W
Q, W


-
-
mi
me
Q W DU DKE DPE D final state initial
state
Q W DH DKE DPE D Out In
4
???????????????????????
  • ??????????????/???????
  • ???????????????????????????

5
????????
?????????????????????????????? ?????.?.2551
?????????? ????????????????? 50,000 ??
??????? 75,000 ?? ???????? 22,000 ?? ????????????
19,000 ?? ????????????????????????????????????????
??? (???????????????????????????)
6
??????
???????????????????????????
???????????????? ???????????????
???????????????? - ????????????????
50,000 22,000 75,000 -19,000 ??/??
- 22,000 ??/?? ????????????????????????????
22,000 ??/?? Ans.
7
???????? ????????????????????????????????
?????????????????????????????? ?.?. 2552 ??????
??????? ??? ???
1. ????????????????????????? 8,000.00
2. ???????? 4500.00
3. ?????????? Prin.Chem.Eng 650.00
4. ?????????? 500.00
5. ????????????????? 915.00
6. ????????? 400.00
7. ?????????/?????????? 700.00
??? 8,000.00 -7665.00
???????????????????? 335.00
8
????????????????????????
???????????????????????????
?????????????????????????????
???????????????????????????
?????????????????????????
????????????????????
9
????????????? (??????????????)
1. ?????? 2. ?????? 3. ???????????????????
(Component balance) 4. ???????????????????
5. ??????????? 6. ??????????? 7. ???????
(????????????)
10
????
  • Unsteady State Process ???? Transient Process
    ?????????????????????????????????????????????
  • Steady State Process ?????????????????????????????
    ?????????????? (???????????? ???????
    ????????????) ????????????????????????????????????
    ???????????????????????? ??????????????
    ???????????????????????????
  • ??????????????????????????????????????????????????
    ???? ?????????????????????????????????? Steady
    State

11
(No Transcript)
12
????????????? Steady State ????????????????????
?????????????????????? (1) ???????????????????
? ?????????????????????? (2) ???????? (1) ???
(2) ?????????????????????????????????????????
?????????????????????? ?????????????????????????
???
13
????????
?????????????????? ??????????????????????????????
??? (Thickener) ??????????????????????
?????????????????????? ????????????? Steady State
???????????????????? 100 kg ??????????????????????
??
14
Basis ?????????? 100 kg ??? Steady State
????????????? ???????????? ?????????? 100 kg
????????? 70 kg
??? W kg W 100 70 30 kg
???????????????????????????? 30 kg
Ans
15
??????????????????? ???????????????? 1. ??????
????????????? ? ????????? ????????????????????????
????? streamline 2. ???? Basis 3. Set ????? 4.
???????? 5. ?????????
16
????????????????????????????????
Differential balance
Integral balance
17
???????????????????????????? ??????????
Differential balance ?????????????????? ???????
?????????????????????????????????????? (??/??)
Integral balance ????????????????????????????
2 ???? ????????? kg ?? ???? ??????? ????????????
????????????????????? ???? Generation 0
??? Consumption 0 ??????????????? Steady -
state Accumulation 0
18
???????? ???????????? 300 lb ??? C 24.0 lb ??
reactor ??? 600F ????????????????????????????
???????????????? Reactor ???????? 1. ?????? C,
O2 ????????????????????? reactor 2. ???????????
C ??? O ???????????????? reactor 3. ???????????
???????????????? reactor
O2 21 N2 79
19
Basis ????? 300 lb (???? C 24.0
lb)     ???????? 2.17 8.17 10.34 lb
mol
??????????? O2 300 lb air 1 lb mol air 21 lb mol O2
??????????? O2 29.0 lb air 100 lb mol air
??????????? O2 2.17 lb mol
??????????? N2 300 lb air 1 lb mol air 79 lb mol N2
??????????? N2 29.0 lb air 100 lb mol air
??????????? N2 8.17 lb mol
??????????? C 24.0 lb C 1 lb mol C
??????????? C 12.0 lb C
??????????? C 2.00 lb mol
20
C O2 ?
CO2 ???????? (lb mol) 2.00 2.17 0 ???????(lb
mol) 0 0.17 2.00
Component IN IN OUT OUT
Component lb lb mol lb lb mol
C 24.0 2.00 0 0
O2 69.5 2.17 5.5 0.17
N2 230.5 8.17 230.5 8.17
CO2 0 0 88.0 2.00
Total 324 12.34 324 10.34
21
???????????????????? 1. N2 ??????????????????????
???????????????????????????????????????? Inert
???????????????????? (Impurities)
????????????????? ????????????????????????????????
???????? Reactor ??????????????????????? 2.
?????????????????????? ?????????????????? Reactor
?????????????????????????????????????? Reactor
??????????????????????????????????????????????????
?????? Reactor ????
22
3. ???????????????????????????????????????????????
???????? ????????????????????? ???? ?????????????
O ??? O2 , H ??? H2 ??????? ????????????????????
? ????? ???????????????????? ?????????????????????
????????? ????????????????????????????????????????
???????????????????????????????????
??????????????????????????????????????????????????
????????????????????????????????
23
3. ???????????????????????????????????????????????
???????? ????????????????????? ???? ?????????????
O ??? O2 , H ??? H2 ??????? ????????????????????
? ????? ???????????????????? ?????????????????????
????????? ????????????????????????????????????????
???????????????????????????????????
??????????????????????????????????????????????????
????????????????????????????????
24
????????????????????? ??????????? C ???????
??????????? C ??????
2.00 lb mol ??????????? O ???????
??????????? O ??????
4.34 lb mol
????? ???? ???? ???? ??? ??? ???
????? C (lb mol) CO2 (lb mol ) O2 (lb mol) C (lb mol) CO2 (lb mol) O2 (lb mol)
C 2.00 0 0 0 2.00 0
O 0 0 22.17 4.34 0 22 4 0.172 0.34
25
????????????????????? ??????????? C
??????? ??????????? C ??????
24.0 lb ??????????? O
??????? ??????????? O ??????
138.9 128 10.9
????? ???? ???? ???? ??? ??? ???
????? C (lb) CO2 (lb) O2 (lb) C (lb) CO2 (lb) O2 (lb)
C 24 0 0 0 24 0
O 0 0 22.1732 138.9 0 2232 128 0.17232 10.9
26
???????????????????????? Accumulation In Out
Generation - Consumption C balance 0 C in
C out Generation Consumption 0 2.00
lb mol C out 0 2.00 lb mol C out 2.00
- 2.00 0 O2 balance 0 O2 in O2 out
Generation Consumption 0 2.17 lb mol
O2 out 0 2.00 lb mol O2 out 2.17 -
2.00 lb mol 0.17 lb mol
27
???????????????????????? Accumulation In Out
Generation - Consumption C balance 0 C in
C out Generation Consumption 0 2.00
lb mol C out 0 2.00 lb mol C out 2.00
- 2.00 0 O2 balance 0 O2 in O2 out
Generation Consumption 0 2.17 lb mol
O2 out 0 2.00 lb mol O2 out 2.17 -
2.00 lb mol 0.17 lb mol
28
CO2 balance 0 CO2 in O2 out
Generation Consumption 0 0
CO2 out 2.00 lb mol 0 CO2 out
2.00 lb mol N2 balance N2 in N2 out
29
???????? ?????? 1000 kg/h ?? Benzene (B) ???
Toluene (T) ??????????????????????????????????? B
??????? 50 ??? T ??????? 50
?????????????????????? 2 ???? ?????? (Top Stream)
?? B 450 kg/h ???????????????? 475 kg T/h
?????????????????? Steadystate
???????????????????? ???????? flowrate
??????????
30
Basis ??????? 1000 kg / h ???? 1 hr. Overall
balance F D B Benzene balance 0.50 F
450 kg/hr q2 0.50 (1000) 450 q2
q2 50 kg
B/hr Toluene balance 0.50 F q1 475
kg/hr 0.50 (1000) q1 475
q2 25 kg B/hr. ????????????????
?? In Out 1000 (450 25) (475
50) 1000 1000
31
???????? ?????? 1000 kg/h ?? Benzene (B) ???
Toluene (T) ??????????????????????????????????? B
??????? 50 ??? T ??????? 50
?????????????????????? 2 ???? ?????? (Top Stream)
?? B 450 kg/h ???????????????? 475 kg T/h
?????????????????? Steadystate
???????????????????? ???????? flowrate
??????????
32
???????? Batch mixing process
33
Basis A 200 g, B 150 g ??? x ???? mass
fraction ??? MeOH ????? C Overall balance C
200 150 350 g CH3OH balance 200(0.4)
0.7(150) x (350) 80 105 x
(350) x 185 / 350 0.5286
?????????????????? H2O balance In Out
0.6(200) 0.3(150) (1-0.5286)(350) 165 1
65
34
??????????????????????????? ??????????????????????
??? 1. ???????????????????????????????????
?????????????????????????? ???????????? flowchart
??????????????????????????????????????????????????
???? Flowchart ????????????????????????????????
??????????? Box ???? Symbol ??? Process Unit
(Reactor, Mixer, Dryer, ) ?????????????
?????????????????????????????????????? Input ???
Output Stream ????????????????????????????????????
??????????????????? ????? Box ???? ????? ?????
??????????????????????? ??????????????????????????
?? ????????????????????????????????????????
???????????????????????????????????????????
?????????????????????????????????????? Stream
??????????????????????????????????????????????????
???? Stream ???????? F ??? Feed , T
?????????????? ??????? ??????????????????
??????????????????????? ??????????? ?????????
(Data-base) ??????????? ??????????????????????????
?
35
2. ??????? Basis ?????? flowrate ????????????
Process ?????? Basis ??????????????
????????????????????????????????????? Stream
?????? Basis ?????????? flowrate ???????????? 1
???? 100 ????????????????????????? 3.
??????????????????????????????????????????????????
???? Flowchart ???????????????????????????????
??????????????????????????????????????? Component
balance ??????????????????????????
???????????????????????? ????????????????????????
??????????? ??????????????????????????????????????
???????? (??????????????????????????? L)
36
2. ??????? Basis ?????? flowrate ????????????
Process ?????? Basis ??????????????
????????????????????????????????????? Stream
?????? Basis ?????????? flowrate ???????????? 1
???? 100 ????????????????????????? 3.
??????????????????????????????????????????????????
???? Flowchart ???????????????????????????????
??????????????????????????????????????? Component
balance ??????????????????????????
???????????????????????? ????????????????????????
??????????? ??????????????????????????????????????
???????? (??????????????????????????? L)
37
4. ????? ???????? 5. ????????? ?????????????
?????????????????????????????????
???????????????????? Redundant equation (????
total mass balance) ??????????????????????????????
??????????? ??????????????????
????????????????? ???????????????????????
38
??????? ???????????????????? ?????????????????????
??? 4 ????? ??????
???????? 4 ????? 3 unknown ???????
????????????? ??????????
0.25 NaCl 0.35 KCl 0.55 H2O 0.30 ------(1)
0.35 NaCl 0.20 KCl 0.40 H2O 0.30 ------(2)
0.40 NaCl 0.45 KCl 0.05 H2O 0.40 ------(3)
1.00 NaCl 1.00 KCl 1.00 H2O 1.00 ------(4)
??? ???????????????????? 3 ????????
???????????????? unknown ???????????? 4
????????????????? ?????????????????????????? 1
??? 3 ??????????? ???????????????????
39
???????? Determine the Number of Degree of
Freedom ??????????????????????
???????????????????????????? D ????????
??????????????????????????????????????????????????
? ????????????????????????????????????????????????
??
40
????????? ????????????? ????????????? Degree of
Freedom ?????????????????????????
???????????????????????????????????????????????
??????????????????????????????????????????????????
??? 100 ???? ???????????????????????????????????
????????????????????????????????????
????????????????????????????
Stream ?????????????????????????????????? ??????????????????????????????????
A 2 A, ?H2SO4
B 3 B, ?H2SO4 , ?HNO3 ???? B, ?H2SO4, ?H2O
C 2 C, ?HNO3 ???? C, ?H2O
D 2 ?H2SO4 , ?HNO3 ???? ?HNO3, ?H2O???? ?H2SO4 , ?H2O
Total 9
41
???????? ????????? Alcohol ???? ?????????????????
?? Alcohol ???????????? Bottom Product
??????????????????????? ??????????????????????????
?????????
42
Basis F 1000 kg ??????????????????????
?EtOH , ?H2O ????? B ????????? B, ????????? 2
?????????????????????????????????? 2 ?????
?????????????????????????????????? overall
balance F D B 1000 kg 100 kg
B B 900 kg B F D
D 1 F 1000 100 kg
D 10 F 10 100 kg
43

kg feed in - kg distillate out kg bottom product out
EtOH 0.10(1000) - (0.60)(100) 40
H2O 0.90(1000) - (0.40)(100) 860
900
Composition ????? B
kg by mass
EtOH 40 4.4
H2O 860 95.6
900 100.0
????????????????? Total Balance ?????? B
900 kg ?????? EtOH 40 kg ??? B ??????????????
???????? 900 40 kg 860
kg ??????????????????????? ?????????????????????
??????????????? ??????????????????????
44
Homework
  • 7.12
  • 7.13
  • 7.14
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