Neraca Massa Fwko 2

Neraca massa pada FWKO existng

Volume minyak erproduksi = = Massa minyak erproduksi =

1kg

2.2! l" Flu Fluida ida #$% = ,as = Minyak = $ir = adaan =

= 1&' 1&''( '(..)! kg* kg*+am +am )&2.-2 kg *+am !'''.() kg *+am 11!1.-& kg *+am 21.'2 kg *+am FWKO Efisiensi 81.93 %

conds

!'''.&(-(!

/ #adaan% =

Neraca massa total Massa masuk = Massa keluar

$

= 0  1&''(.)! '(&.22 kg *+am kg*+am 1&''(.)! 1&''(.)! kg *+am kg*+am

Neraca massa komponen Masuk #uida $% =

,as

=

.))

3

Minyak =

).4&

3

$ir

=

4).!&

3

adaan =

.2

3

Keluar

=

0 ,as = 5 Minyak = $ir = 6 Minyak =

$ir =

'(&.22 kg*+am

)'&.1 kg*+am 1(')'.1' kg*+am

4-'.(' kg*+am

('1-&.!' kg*+am

'1 0op7 x .1- m'*+am

e8siensi =

).4- m'*+am ).4- m'*+am x ((1.! kg*m' )'&.1 kg*+am 0= ,as =

'(&.22 kg*+am '(&.22 kg*+am

5= ,as = Minyak = $ir =

6= $ir = Minyak =

21.'2 kg*+am

 6  / 22&4(.!) ()1'1.'& kg*+am kg*+am kg*+am

22&4(.!)) (!.) )'&.1 1(')'.1''

()1'1.'-& kg*+am ('1-&.!') kg*+am 4-'.(' kg*+am

5

pers. ).' p 21.'2

Tabel Neraca Massa Komponen di FWKO Exisng

Komponen Masuk (kg/jam ,as Minyak $ir adaan 9u" oal Total

)&2.-2 !'''.() 11!1.-& 21.'2 1&''(.)! $%&'')*+

! '(&.22

'(&.22

Keluar (kg/jam " # (!.) )'&.1 4-'.(' 1(')'.1'' ('1-&.!') 22&4(.!)) ()1'1.'-& $%&'')*+

roduk

x 1 3

:mpan (1.4' 3 .(2

kg*+am kg*+am kg*+am kg*+am

 

uline

E

21.'2 21.'2

Fluida A = 236681

lb/h

Gas = 1042 lb/h Minyak= 11761 lb/h Air = 223831 lb/h Padatan= 47 lb/h

Fluida #$% ;umla7 ,as Kar"on
1&''(.)! )&2.-21'2 kg*+am .(' '42.2( .11 !1.44 .2 4.)! .2! 11.(2 .1! &.4 )&2.-2

Minyak $ir adaan

!'''.() 11!1.-& 21.'2

).4& 4).!& .2

Fluida #

%$ /8siensi

/8siensi

/8siensi

Neraca massa pada FWKO existng

Volume miny Massa minya

1kg

2.2! l" Fluida #$% = ,as = Minyak = $ir = adaan =

kg*+am kg*+am kg*+am kg*+am kg*+am kg*+am conds

1&''(.)! )&2.-2 !'''.() 11!1.-& 21.'2

!'''.&(-(!

Neraca massa total Massa masuk = Massa keluar

Neraca massa komponen Masuk #uida $% = 1&''(.)!

Massa gas Massa umpan

,as = Kar"on
Minyak =

$ir

=

adaan =

Keluar = (1.4'

.(14'

x

0 ,as = Kar"on
,as $

(!.) )&2.-2 Kar"on
(1.4'

,as masuk '42.2( !1.44 4.)! 11.(2 &.4

>

,as keluar " '21.'4 )2.!4 &.&) 4.-( !.(1

.(14' Minyak $ $ir masuk 11!1.-&

Minyak masuk !'''.() (1.4'

'(&.22

.(14'

>

>

!'''.() air keluar 6 ('1-&.-4

minyak keluar 5 )'&.2 $ir $

5 ,as Kar"on
Minyak = $ir =

6 Minyak =

$ir = 11!1.-&

k erproduksi =

'1 0op7 x .1- m'*+am =

).4- m'*+am ).4- m'*+am x ((1.! kg*m' )'&.1 kg*+am

erproduksi = = kg*+am kg*+am kg*+am kg*+am kg*+am

FWKO Efisiensi 81.93 %

/ #adaan% =

21.'2 kg*+am

$

= 0  5  6  / 1&''(.)! '(&.22 22&4(.'4 ()1'1.!1 kg*+am kg*+am kg*+am kg*+am kg*+am 1&''(.)! 1&''(.)) kg*+am kg*+am

.)) '42.2( !1.44 4.)! 11.(2 &.4 )&2.-2

3

).4&

3

.'-! .)( .4 .11 .& .))

3 3 3 3 3

21.'2

4).!&

3

.2

3

'(&.22 kg*+am '21.'4 kg*+am )2.!4 kg*+am &.&) kg*+am 4.-( kg*+am !.(1 kg*+am

Komponen 22&4(.) (!.) &.(( kg*+am 4.'4 kg*+am 1.&1 kg*+am 2.1) kg*+am 1.2( kg*+am

)'&.2 kg*+am 1(')2.4( kg*+am

4-'.(' kg*+am

('1-&.-4 kg*+am ()1'1.!1

,as

Kar"on
e8siensi =

roduk

x 1 3

:mpan (1.4' 3 .(2 0= ,as =

'(&.22 kg*+am '(&.22 kg*+am

5= ,as = Minyak = $ir =

6= $ir = Minyak =

22&4(.'(((- kg*+am (!.) kg*+am )'&.1 kg*+am 1(')2.4&&)& kg*+am

()1'1.!1)'1&! kg*+am ('1-&.-4 kg*+am 4-'.(' kg*+am

Fluida 0 Kar"on
Fluida 5 ,as Kar"on
pers. ).' pauline Fluida 6

Masuk (kg/jam , '42.2( !1.44 4.)! 11.(2 &.4 !'''.() 11!1.-& 21.'2 1&''(.)! $%&'')*+

Keluar (kg/jam ! '21.'4 )2.!4 &.&) 4.-( !.(1

'(&.214

" &.(( 4.'4 1.&1 2.1) 1.2( )'&.2 1(')2.4(

#

E

4-'.(' ('1-&.-4

22&4(.) ()1'1.!1 $%&'')*+

21.'2 21.'2

'(&.22 .(' .11 .2 .2! .1!

'21.'4 kg*+am )2.!4 kg*+am &.&) kg*+am 4.-( kg*+am !.(1 kg*+am '(&.22 kg*+am

(!.) .(' .11 .2 .2! .1!

&.(( kg*+am 4.'4 kg*+am 1.&1 kg*+am 2.1) kg*+am 1.2( kg*+am (!.) kg*+am