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Tin 298 K
P 1 atm
R 0.082 L.atm/K mol
Volume 1 L (asumsi)
1 CxHy 12.5 (2
Mr: 11! "2
Mencari jumlah mol campuran
n 0.0!092"228 mol
#a$an #a%a& stoi%io 1.'8
fraksi mol setiap reaktanCxHy 0.01'522!2""
2 0.20'5"02911
2 0.'9!285'
Mol reaktan
nCxHy 0.000''1509
n2 0.008!5188'2
n2 0.0"1951909
Untuk Pembakaran Sempurna (Stoikio)Pem#atas CxHy
Spesi Awal ereaksi !asil"sisa (mol)
CxHy 0.000''1509 0.000''1509 0.00000
2 0.008!5188'2 0.008!5188'2 0.00000
2 0.0"1951909 0.0"1951909
C2 0.005!09202 0.005!09202
H2 0.00'085"581 0.00'085"581
#!$"!!$ '22.!! K*/%+ */+ (Te&+an
Mencari %ntalpi Molar
&'!y &
a1 0.89'9208 0."2129"'! 0.2252!'
a2 0.02''898'1 0.00112!8'" !.9'-0"
a" 5.!"1!"-00' 5.'-0 ".!-0'
a! 2.12'00-008 1."1-09 1.2-09
a5 9.2!"""-012 8.-1" !.2"-1"
a' 1.01-0" !8"".1!1
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T 258.890'211 K
T&ial to 0 0.!"'88'18'!
u%u Ki&i 3
"8.'81 ".'92 3
"!.989 30.000 4
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Mencari Titik Nyala Adiabatis
n6ut
Result
Persamaan Reaksi
".'190!'19 2) 3 8 C2
28 !!
*ika Reaksi +uel Ric,
Pem#atas 2
Massa ak,ir Spesi Awal ereaksi !asil"sisa (mol)
0.00000 CxHy 0.000''2 0.000''2 0.00000
0.00000 2 0.008!519 0.008!519 0.00000
0.8902'5"!'1 2 0.0"1952 0.0"1951909
0.2"8005115" C2 0.005!092 0.005!09202
0.1095"'!!51 H2 0.00'085! 0.00'085"581
un+ *enis ,a$an ,a%a&)
! N
0.""8'8!25 0."298''9
1.!-0" .0!-0! 7HV 5!'0 %*/mol
2.12-0' 1."2-0'
1.!-09 1.!1-09
5.01-1" !.89-1"
".02-0! 1.02-0"
ola& -nt$al6$y 3
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u%u Kanan
"!.989
"!.989 T&ial to :e&o Te&$a;a6 T
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9 H2 !.02"81 2
18
Massa ak,ir
0
0
0.8902'5"!'1
0.2"8005115"
0.1095"'!!51
%*/mol
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Tin 298 K
P 1 atm
R 0.082 L.atm/K mol
Volume !!!.0"8801 L (asumsi)
1 CxHy 2 (2
Mr: 1' "2
Mencari jumlah mol campuran
n 181.981851 mol
#a$an #a%a& stoi%io 10.5
fraksi mol setiap reaktanCxHy 0.095022'2!!
2 0.1900!52!89
2 0.1!9"212'
Mol reaktan
nCxHy 1.2929
n2 !0.8"05 ex
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T 2529.199855 K
T&ial to 0 1''.250599
u%u Ki&i 3
1'5200.2 15""."88 3
1!982."8! 30.000 4
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Mencari Titik Nyala Adiabatis
n6ut
Result
Persamaan Reaksi
".'190!'19 2) 3 1 C2
28 !!
/= met$ane
1.1918!81 %ali li6at ;a&i se$a&usnya
*ika Reaksi +uel Ric,
Pem#atas 2
Massa ak,ir Spesi Awal ereaksi !asil"sisa (mol)
0.00000 2'.'8'!0 20.2!2'25 1.2929 1.29290
198."1200 1"05.05'02 !0.8"05 !0.8"05 0.00000
!295.81!' !295.81!'02 15".!2195 15".!2195
'0.88' C2 20."91525 20."91525
'22.5!!! H2 !0.8"05 !0.8"05
un+ *enis ,a$an ,a%a&)
! N
0.""8'8!25 0."298''9
1.!-0" .0!-0! 7HV 889 %*/mol
2.12-0' 1."2-0'
1.!-09 1.!1-09
5.01-1" !.89-1"
".02-0! 1.02-0"
ola& -nt$al6$y 3
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u%u Kanan
1!982."8!
1!982."8! T&ial to :e&o Te&$a;a6 T
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Tin 298 K
P 1 atm
R 0.082 L.atm/K mol
Volume 1 L (asumsi)
1 CxHy 12.5 (2
Mr: 11! "2
Mencari jumlah mol campuran
n 0.0!092"228 mol
#a$an #a%a& stoi%io 1.'8
fraksi mol setiap reaktanCxHy 0.01'522!2""
2 0.20'5"02911
2 0.'9!285'
Mol reaktan
nCxHy 0.002028!52 ex
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T 2!!.8198299 K
T&ial to 0 0.8!!"2""81
u%u Ki&i 3
.281 11.05 3
''.205 32.99 4
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Mencari Titik Nyala Adiabatis
n6ut
Result
Persamaan Reaksi
".'190!'19 2) 3 8 C2
28 !!
" %ali li6at ;a&i se$a&usnya
*ika Reaksi +uel Ric,
Pem#atas 2
Massa ak,ir Spesi Awal ereaksi !asil"sisa (mol)
0.008 CxHy 0.0020285 0.000''2 0.001"5
0.00000 2 0.008!519 0.008!519 0.00000
1.805"0'922 2 0.0"1952 0.0"1951909
0.!'0102"0' C2 0.005!092 0.005!09202
0.219028902 H2 0.00'085! 0.00'085"581
un+ *enis ,a$an ,a%a&)
! N
0.""8'8!25 0."298''9
1.!-0" .0!-0! 7HV 5!'0 %*/mol
2.12-0' 1."2-0'
1.!-09 1.!1-09
5.01-1" !.89-1"
".02-0! 1.02-0"
ola& -nt$al6$y 3
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u%u Kanan
'".208
'".208 T&ial to :e&o Te&$a;a6 T
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9 H2 !.02"81 2
18
Massa ak,ir
0.15!1'2!0!2
0
0.8902'5"!'1
0.2"8005115"
0.1095"'!!51
%*/mol
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