perhitungan lampiran b

7/23/2019 Perhitungan Lampiran b

1/29

LAMPIRAN B

URAIAN PERHITUNGAN

NERACA MASSA DESAIN

1. HPD (2-DA201)

Untuk masing masing komponen :

a. Carbamat Konenser (2-!A102)

Urea " 1#$$10 kg%&r ' #1$*

" $1#+,#$ kg%&r

H " 1#$$10 kg%&r ' 12+/*

" 20##001/ kg%&rC2 " 1#$$10 kg%&r ' 1#+*

" 21#$22+ kg%&r

H2 " 1#$$10 kg%&r ' 21+2*

" /$111#2 kg%&r

iuret " 1#$$10 kg%&r ' 01*

" 2,+, kg%&r

b. 3rubber (2-DA102)

H " /,#0 kg%&r ' 1##*

" 20# kg%&r

C2 " /,#0 kg%&r ' 22*

" 102 kg%&r

H2 " /,#0 kg%&r ' ,/#*

" 2+++2# kg%&r

3. 45201 (ke 4PD)

Urea " 120+2# kg%&r ' ,,*

" $0,#,+# kg%&r

H " 120+2# kg%&r ' ,1/*

" /2/+# kg%&r

C2 " 120+2# kg%&r ' 2/*" 2+$,$/# kg%&r

H2 " 120+2# kg%&r ' 2/+*

" 2+/+,0# kg%&r

iuret " 120+2# kg%&r ' 0*

" ,2# kg%&r

. HPA (2-!A/01 )

H " /2## kg%&r ' +$1*

" 1,+1$# kg%&r

C2 " /2## kg%&r ' /#,*

" 2022+,/, kg%&r

60


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H2 " /2## kg%&r ' 12,*

" #210# kg%&r

!6ACA 7AA HPD

kompone

n

7

input output

DA 102 !A102 (CC2) HPA 45201

urea ,0 0 $1#+,#$ 0 $0,#,+#

H 1 20# 20##001/ 1,+1$# /2/+#

C2 // 102 21#$22+ 2022+,/, 2+$,$/#

H20 1$ 2+++2# /$111#2 #210# 2+/+,0#

iuret 10 0 2,++ 0 ,2#

88A4 2/2 /,#0 1#$$10 /2## 120+2#

1,/,0 1,/,0

2. HPA (2-!A/01 )


9o; input " CA 10# = +0+ kg%&r

9o; 9>CA 10# " 20+ kg%&r

a. 9>CA 10#

Urea " 20+ kg%&r ' 11#*

" $20+/ kg%&r

H " 20+ kg%&r ' /1*" 2/0#1 kg%&r

C2 " 20+ kg%&r ' ,$2*

" 2,,21 kg%&r

H2 " 20+ kg%&r ' 12,*

" 12/ kg%&r

iuret " 20+ kg%&r ' 0/1*

" 2+,# kg%&r

b. HPD (2DA201)

H " /2## kg%&r ' +$1*

" 1,+1$# kg%&r

C2 " /2## kg%&r ' /#,*" 2022+,/, kg%&r

H2 " /2## kg%&r ' 12,*

" #210# kg%&r

3. HPAA ke HPA

Urea " 0,$1+ kg%&r ' 2#*

" $#1/ kg%&r

H " 0,$1+ kg%&r ' 2,*

" +$ kg%&r

C2 " 0,$1+ kg%&r ' 21#2*

" ,,01 kg%&r


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62

H2 " 0,$1+ kg%&r ' 2*

" 2$0# kg%&r

iuret " 0,$1+ kg%&r ' 100/*" 0$ kg%&r

. HPA ke HPAA

Urea " +0+ kg%&r ' ##*

" 0/, kg%&r

H " +0+ kg%&r ' 22*

" 20,1 kg%&r

C2 " +0+ kg%&r ' 21*

" 210 kg%&r

H2 " +0+ kg%&r ' 12,*" 1# kg%&r

iuret " +0+ kg%&r ' 0/1*

" 11# kg%&r

!6ACA 7AA HPA

komponen 7 input output

HPD HPAA 9>CA 10# HPAA

urea ,0 - $.#1/0 $.20+/ 0/,

H 1 1,.+2 .+$0 2/.0#1 20,1

C2 // 20.22+, ,.,01 2,.,210 2100H20 1$ #.22 .2$0# 12./0 1#

iuret 10 - 0$0 2+,# 11#

88A4 2/2 /2## 0,$1+ 20+ +0+

21,+ 21,+

. HPAA (2-!A/01 A)

9o; input "


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" 2+$ kg%&r

b. HPA ke HPAAUrea " +0+ kg%&r ' ##*

" 0/, kg%&r

H " +0+ kg%&r ' 22*

" 20,1 kg%&r

C2 " +0+ kg%&r ' 21*

" 210 kg%&r

H2 " +0+ kg%&r ' 12,*

" 1# kg%&r

iuret " +0+ kg%&r ' 0/1*

" 11# kg%&r

3. HPAA ke HPAUrea " 0,$1+ kg%&r ' 2#*

" $#1/ kg%&r

H " 0,$1+ kg%&r ' 2,*

" +$ kg%&r

C2 " 0,$1+ kg%&r ' 21#2*

" ,,01 kg%&r

H2 " 0,$1+ kg%&r ' 2*

" 2$0# kg%&r

iuret " 0,$1+ kg%&r ' 100/*

" 0$ kg%&r

. HPAA ke ?C

Urea " 2+0 kg%&r ' 0/1/*

" 12 kg%&r

H " 2+0 kg%&r ' 010*

" 0 kg%&r

C2 " 2+0 kg%&r ' 2//$*

" 1 kg%&r

H2 " 2+0 kg%&r ' +,/*

" 2+, kg%&r

iuret " 2+0 kg%&r ' 0,21*" 1$ kg%&r

!6ACA 7AA HPAA

komponen 7 input output

HPA ?C HPA ?C

urea ,0 0/, $.210, $.#1/0 12

H 1 20,1 .22 .+$0 0

C2 // 2100 ,.+$/ ,.,01 1

H20 1$ 1# .$// .2$0# 2+,

iuret 10 11# 2+$ 0$0 1$

88A4 2/2 +0+ 00,/ 0,$1+ 2+0


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0+1+ 0+1+

/. ?AH>@ C4U7 (2DA/01)

9o; input " C20 =


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e. ?C ke 4PA

Urea " 111$2 kg%&r ' 00*

" $2101 kg%&rH " 111$2 kg%&r ' 1,*

" 1#+/ kg%&r

H2 " 111$2 kg%&r ' 2,0#*

" 0#2 kg%&r

iuret " 111$2 kg%&r ' 2#*

" 2+,/ kg%&r

@ C4U7

kompone

n

7

input output

9>C 20 96C/01 HPAA P5/0

1

4PA HPAA

urea ,0 $.20+/ $.2101 12 - $.2101 $.210,

H 1 - .+ 0 ,0 1#+/ .22

C2 // - ,.+1 1 - - ,.+$/

H20 1$ 2.+$0 .1+20 2+, 220 .0#2 .$//

iuret 10

2+,# 2+,/ 1$ - 2+,/ 2+$

88A4 11/+ 00211 2+00 2$0 11.1$

2

0.0,/0

/1.$102 /1.$102

NERACA MASSA AKTUAL

6ate : +$*

asis : 1 am perasi

?aktu anaisa : 0 Bui 201# am 0$.00 ?>

1. HPD (2-DA201)



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a. Carbamat Konenser (2-!A102)

Urea " 1#$$10 kg%&r ' #1$* ' +$*

" ++,/,/,/ kg%&r

H " 1#$$10 kg%&r ' 12+/* ' +$*

" 201+012 kg%&r

C2 " 1#$$10 kg%&r ' 1#+* ' +$*

" 211#0,/2 kg%&r

H2 " 1#$$10 kg%&r ' 21+2* ' +$*

" /11/+2$+, kg%&r

iuret " 1#$$10 kg%&r ' 01* ' +$*

" 2,/#/, kg%&r

b. 3rubber (2-DA102)

H " /,#0 kg%&r ' 1##* ' +$*

" 2,0## kg%&r

C2 " /,#0 kg%&r ' 22* ' +$*

" 1002#/ kg%&r

H2 " /,#0 kg%&r ' ,/#* ' +$*

" 2++2,# kg%&r

3. 45201 (ke 4PD)

Urea " 120+2# kg%&r ' ,,* ' +$*

" #211/,# kg%&rH " 120+2# kg%&r ' ,1/* ' +$*

" #,0/#,# kg%&r

C2 " 120+2# kg%&r ' 2/* ' +$*

" 20$11$ kg%&r

H2 " 120+2# kg%&r ' 2/+* ' +$*

" /,$,$#2## kg%&r

iuret " 120+2# kg%&r ' 0* ' +$*

" /,21## kg%&r

. HPA (2-!A/01 )

H " /2## kg%&r ' +$1* ' +$*" 1,#+/#1+$ kg%&r

C2 " /2## kg%&r ' /#,* ' +$*

" 1+$2#0#0$ kg%&r

H2 " /2## kg%&r ' 12,* ' +$*

" #2,/20+ kg%&r

!6ACA 7AA HPD

kompone

n

7 input output

DA 102 !A102 (CC2) HPA 45201

urea ,0 0 ++,/,/,// 0 #211/,#

H 1 2,0## 201+012 1,#+/#1+$ #,0/#,#


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C2 // 1002#/ 211#0,/2 1+$2#0#0$ 20$11$

H20 1$ 2++2,# /11/+2$+, #2,/20+ /,$,$#2##

iuret 10 0 2,/#/, 0 /,21##88A4 2/2 /## 1##,$ /1,$/ 11$#0,#

1,01+0$ 1,01+0$

2. HPA (2-!A/01 )


9o; input " CA 10# = #0/ kg%&r

9o; 9>CA 10# " 0.$,,2 kg%&r

a. 9>CA 10#

Urea " 0.$,,2 kg%&r ' //1,* ' +$*

" .1#+$ kg%&r

H " 0.$,,2 kg%&r ' $#* ' +$*

" 2/.2221 kg%&r

C2 " 0.$,,2 kg%&r ' ,/#* ' +$*

" 2,.0$, kg%&r

H2 " 0.$,,2 kg%&r ' 2/1+* ' +$*" 1.10, kg%&r

iuret " 0.$,,2 kg%&r ' 012,* ' +$*

" +01 kg%&r

b. HPD (2DA201)

H " /2## kg%&r ' +$1* ' +$*

" 1,#+/#1+$ kg%&r

C2 " /2## kg%&r ' /#,* ' +$*

" 1+$2#0#0$ kg%&r

H2 " /2## kg%&r ' 12,* ' +$*

" #2,/20+ kg%&r

3. HPAA ke HPA

Urea " 0,$1+ kg%&r ' 111$* ' +$*

" .,2$ kg%&r

H " 0,$1+ kg%&r ' 2#1$* ' +$*


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68

" .2$ kg%&r

C2 " 0,$1+ kg%&r ' 211#* ' +$*

" ,.#$, kg%&r

H2 " 0,$1+ kg%&r ' /0#,* ' +$*

" 12.1+,/ kg%&r

iuret " 0,$1+ kg%&r ' 0/* ' +$*

" 101$ kg%&r

. HPA ke HPAAUrea " +0+ kg%&r ' 2* ' +$*

" 200 kg%&r

H " +0+ kg%&r ' 12* ' +$*

" 10#2 kg%&r

C2 " +0+ kg%&r ' 11* ' +$*

" 100 kg%&r

H2 " +0+ kg%&r ' 1* ' +$*

" 1#0# kg%&r

iuret " +0+ kg%&r ' 11* ' +$*

" 11 kg%&r

!6ACA 7AA HPA

kompone

n

7

input output

HPD HPAA 9>CA 10# HPAA

urea ,0 - .,2$ .1#+$ 200

NH3 1

1,.#+/# .2$ 2/.2221 10#2

CO2 //1+.$2#1 ,.#$, 2,.0$, 1000

H20 1$

#.2,/ 12.1+,/ 1.10, 1#0#

Bure! 10

- 101$ +01 11

TOTAL 2/2

/1.,$/ 2+.#2/ 0.$,,2 #0/

1/, 1/,

. HPAA (2-!A/01 A)


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9o; input "


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H " 2+0 kg%&r ' 1//* ' +$*

" /10 kg%&r

C2 " 2+0 kg%&r ' 2,* ' +$*" , kg%&r

H2 " 2+0 kg%&r ' 11* ' +$*

" 2 kg%&r

iuret " 2+0 kg%&r ' ,,$#* ' +$*

" 1+0 kg%&r

!6ACA 7AA HPAA

komponen 7

input output

HPA ?C HPA ?C

urea ,0 200 .,0$ .,2$ 2010

NH3 1 10#2 .,,$, .2$ /10

CO2 // 1000 ,.2,# ,.#$, ,

H20 1$ 1#0# 12.0/+1 12.1+,/ 2

Bure! 10 11 2$01 101$ 1+00

88A4

2/2 #0/ 2+.,2$ 2+.#2/ //1+0.1+/ 0.1+/

/. ?AH>@ C4U7 (2DA/01)

9o; input " C20 =


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" 2+0#1 kg%&r

b. 9>C 20

Urea " 11/+ kg%&r ' 2$0#/1* ' +$*" 1#+$ kg%&r

H " 11/+ kg%&r ' 01,1* ' +$*

" 1$1 kg%&r

H2 " 11/+ kg%&r ' 1* ' +$*

" ++,$ kg%&r

iuret " 11/+ kg%&r ' 0$* ' +$*

" +01 kg%&r

3. HPAA ke ?C

Urea " 2+0 kg%&r ' 02* ' +$*

" 2010 kg%&r

H " 2+0 kg%&r ' 1//* ' +$*" /10 kg%&r

C2 " 2+0 kg%&r ' 2,* ' +$*

" , kg%&r

H2 " 2+0 kg%&r ' 11* ' +$*

" 2 kg%&r

iuret " 2+0 kg%&r ' ,,$#* ' +$*

" 1+0 kg%&r

. P5/01

H " 2$ kg%&r ' /,+* ' +$*

" 12$$$, kg%&r

C2 " 2$ kg%&r ' 1$* ' +$*

" /++2 kg%&r

H2 " 2$ kg%&r ' 2$#* ' +$*

" $$+ kg%&r

H2 " 2$ kg%&r ' #$$* ' +$*

" 1,1# kg%&r

C " 2$ kg%&r ' 001* ' +$*

" 0002 kg%&r

CH/ " 2$ kg%&r ' 0+* ' +$*

" 0100 kg%&r

e. ?C ke 4PA

Urea " 111$2 kg%&r ' 00* ' +$*

" $0/#+ kg%&r

H " 111$2 kg%&r ' 1,* ' +$*

" 1#,1, kg%&r

H2 " 111$2 kg%&r ' 2,0#* ' +$*

" 2++12 kg%&r

iuret " 111$2 kg%&r ' 2#* ' +$*

" 2+0#1 kg%&r


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Urea " 0.0,/ kg%&r ' 11/1* ' +$*

" ,0$ kg%&r

H " 0.0,/ kg%&r ' 2,0* ' +$*" ,,$, kg%&r

C2 " 0.0,/ kg%&r ' 212* ' +$*

" ,2,# kg%&r

H2 " 0.0,/ kg%&r ' /0+0* ' +$*

" 120/+1 kg%&r

iuret " 0.0,/ kg%&r ' 0+#* ' +$*

" 2$01 kg%&r

!6ACA 7AA ?C

kompone

n

7

input output

9>C 20 96C/01 HPAA P5/01 4PA HPAA

urea ,0 1#+$ $0/#+ 201 - $0/#+ ,0$

H 1 1$1 $# /1 12$$$

,

1#,1, ,,$,

C2 // - ,2,/+ , /++2 - ,2,#

H20

H2

C

CH/

1$

2

2$

1,

++,$

-

-

-

0/$1+

-

-

-

2

-

-

-

$$+0

1,1#

0002

0100

2++12

-

-

-

120/+1

-

-

-

iuret 10

+01 2+0#1 1+00 - 2+0#1 2$01

88A4 112,/$ 2+/2,, //1+ 2/ 11/$$

1

2+,2$

/11/ /11#1

NERACA PANAS DESAIN

1) HPA (2-!A/01 )

a. HPD (2DA201)

86e


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" ,2.,$1.$112 K3a

C2 " n

TCp.dT

T Reff

" /#+$ 2#1#$,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" 2./2$.02# K3a

H2 " n

TCp.dT

T Reff

" 2+$# 2#1#$1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" 1.+$.$2+/ K3a

b. HPAA ke HPA

86e


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" /0/# 2#+1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" 1.1/.1#01 K3a

iuret " 0 2#+222, = #$#.10-28

" #.2#/ K3a

3. 9>C 10#

86e


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Urea " #1 2#10$1222, = #$#.10-28

" 11.0 K3a

H " n

TCp.dT

T Reff

" 121 2#10$1#1# =2+#/.10-28 = 0//21.10-#82 ,,$,.10-+8

" 2,0.2$#1 K3a

C2 " n

TCp.dT

T Reff

" /$ 2#10$1,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" 1#.$2+ K3a

H2 " n

TCp.dT

T Reff

" +$ 2#10$1

1$2+,/ = /212.10-2

8 1$$.10-#

82

= 11/2.10-+

8

" #.2+1 K3a

iuret " 01 2#10$1222, = #$#.10-28

" 2/2 K3a

Me"a pen"n#n $

Urea " m. Cp. 8

" $1./0# kg%am . $# K3a%kg. C . (0$ ,,)

" ,#.,2.,$$/ K3a

C? " m. Cp. 8

" 1$.000 kg%am . 0++ K3a%kg. C . (+ 0)

" 2.$.$0 K3a

H? " m. Cp. 8

" 1.000 kg%am . 0++ K3a%kg. C. (,# ##)

" 1.12.00 K3a


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Penguraian Carbamat

Dik.

H< C2 " -+/02$ kka%gmo

H< H " -110 kka%gmo

H< Carbamat " -$2/ kka%gmo

Penguraian Carbamat

H2CH/ -- 2H = C2

Hreaksi " H< prouk - Hreaktan

Hreaksi " E(2(-110) = (-+/02$)F - (-$2/) kka%gmo

Hreaksi " - ,0 kka%kgmo

H2CH/ -- 2H = C2

1 mo NH2COONH% & 'mo( CO2

G H2CH/ " n C2 HPD Hr'

G H2CH/ " 12120,$$ Kmo (-,0 kka%kgmo)

G H2CH/ " - /0+1+,0 k3a

!6ACA PAA HPAParameter G input G utput

HPD ,.0$$.11 0

HPAA K!

HPA

$./$.#+/ 0

9>C 10# 0 #.+,2.2$+

HPA K!

HPA

0 22.20

C? 2.$.$00 -

H? 1.12.000 -

Urea ,#.,2.,$$/ -

H r'

3arbamat

0 /0+.1+,.00

88A4

//#./$1.0$+ //#./$1.0+

2) HPAA (2-!A/01 A)

a. HPA ke HPAA

86e


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Urea " #1 2#10$1222, = #$#.10-28

" 11.0 K3a

H " n

TCp.dT

T Reff

" 121 2#10$1#1# =2+#/.10-28 = 0//21.10-#82 ,,$,.10-+8

" 2,0.2$#1 K3a

C2 " n

TCp.dT

T Reff

" /$ 2#10$1,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" 1#.$2+ K3a

H2 " n

TCp.dT

T Reff

" +$ 2#10$1

1$2+,/ = /212.10-2

8 1$$.10-#

82

= 11/2.10-+

8

" #.2+1 K3a

iuret " 01 2#10$1222, = #$#.10-28

" 2/2 K3a

b. ?C ke HPAA

86e


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C2 " n

TCp.dT

T Reff

" 1/#/ 2##1,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" 1/2.// K3a

H2 " n

TCp.dT

T Reff

" /1022##11$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" ,#.+#0 K3a

iuret" 2+ 2##1222, = #$#.10-28

" 1$/ K3a

3. HPAA ke ?C

86e


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H2 " n

TCp.dT

T Reff

" 1## 2#+1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" /.+01, K3a

iuret " 001# 2#+222, = #$#.10-28

" 0 K3a

. HPAA ke HPA

86e


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" #2#/ K3a

Me"a pen"n#n $

C? " m. Cp. 8

" 1.0#+ kg%am . 0++ K3a%kg. C . (+ 0)

" ,$$.++# K3a

!6ACA PAA HPAA

parameter G input G utput

HPA K! HPAA 22.20 0

?C ke HPAA 1.$1,.+1 0

HPAA U8 ke ?C 0 //.,//HPAA U8 ke HPA 0 $./$.#+/

C? ,.$$.++# -

88A4 $.#2$.2/0/ $.#2$.2/0$

NERACA PANAS AKTUAL

asis : 1 am perasi

?aktu anaisa : 0 Bui 201# am 0$.00 ?>

1) HPA (2-!A/01 )a. HPD (2DA201)

86e


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H2 " n

TCp.dT

T Reff

" 2+$# 2#1/1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" 1..+/,1 K3a

e. HPAA ke HPA

86e


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86e


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H " n

TCp.dT

T Reff

" ,2 2#10###1# =2+#/.10-28 = 0//21.10-#82 ,,$,.10-+8

" 12/.12$ K3a

C2 " n

TCp.dT

T Reff

" 2 2#10##,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" .0$ K3a

H2 " n

TCp.dT

T Reff

" $/ 2#10##1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" 2+.0,# K3a

iuret " 01 2#10##

222, = #$#.10-2

8" 2$# K3a

Me"a pen"n#n $

Urea " m. Cp. 8

" $#.+,+ kg%am . $# K3a%kg. C . (0$ ,,)

" #$.0##.//, K3a

C? " m. Cp. 8

" 11.,/0 kg%am . 0++ K3a%kg. C . (+ 0)

" 2.,.12/ K3a

H? " m. Cp. 8

" 1,+.#/0 kg%am . 0++ K3a%kg. C. (,# ##)

" 1.,$.//, K3a

Penguraian Carbamat


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Dik.

H< C2 " -+/02$ kka%gmo

H< H " -110 kka%gmo

H< Carbamat " -$2/ kka%gmo

Penguraian Carbamat

H2CH/ -- 2H = C2

Hreaksi " H< prouk - Hreaktan

Hreaksi " E(2(-110) = (-+/02$)F - (-$2/) kka%gmo

Hreaksi " - ,0 kka%kgmo

H2CH/ -- 2H = C2

1 mo NH2COONH% & 'mo( CO2

G H2CH/ " n C2 HPD Hr'

G H2CH/ " 11#+, Kmo (-,0 kka%kgmo)

G H2CH/ " - +1##,,## k3a

!6ACA PAA HPA

parameter G input G utput

HPD #.$,.#//, 0

HPAA K! HPA +.21./2#/ 09>C 10# 0 .$$/.2,

HPA K! HPA 0 1,.,212

C? 2.,.12/ -

H? 1.,$.//,0 -

Urea #$.0##.//, -

H r' 3arbamat 0 +1.##.,,##

88A4 /2#.#$.#,0/ /2#.#$.#,0

2) HPAA (2-!A/01 A)

a. HPA ke HPAA

86e


26/29

85

" 12/.12$ K3a

C2 " n

TCp.dT

T Reff

" 2 2#10##,11 = /2.10-28 2$$.10-#82= /,/.10-+8

" .0$ K3a

H2 " n

TCp.dT

T Reff

" $/ 2#10##1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" 2+.0,# K3a

iuret " 01 2#10##222, = #$#.10-28

" 2$# K3a

b. ?C ke HPAA

86e


27/29

86

H2 " n

TCp.dT

T Reff

" ,,+/ 2##1$2+,/ = /212.10-28 1$$.10-#82= 11/2.10-+8

" ,/+.$$ K3a

iuret" 2 2##222, = #$#.10-28

" 1$,$ K3a

3. HPAA ke ?C

86e


28/29

87

" .122 K3a

. HPAA ke HPA

86e


29/29

88

!6ACA PAA HPAA

Parameter G input G utput

HPA K! HPAA 1,.,212 0?C ke HPAA 2.1$/.+1 0

HPAA U8 ke ?C 0 /,.0$,/

HPAA U8 ke HPA 0 +.21./2#/

C? ,.+0,.+# -

88A4 +.2#+.#11, +.2#+.#12

perhitungan lampiran b

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