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HE6 cooler

Laju alir massa umpan = 3705 Kg/jam 1.02915 Kg/s

Data fisik

CH3Cl Inlet Mean Outlet

132 115 84

Spesific Hea !"p# 119.005915$$25 108.4$$9 97.92785015$9K%n&u' i(i as ermal 0.145424359$ 0.1$12 0.17$9$90919

)ensi as !'g/m3# 0.3$199$3$48 0.3708 0.3795530402

*is'%si as !'g/m.s# 1.199319581481+,00$ 0.0000011 9.92150509277311+,007

CH2Cl2 Inlet Mean Outlet

132 108.0 84.0

Spesific Hea !"p# 124.55$8953$25 118.3228 112.1

K%n&u' i(i as ermal 0.12$8728371 0.134893500$ 0.14291

)ensi as !'g/m3# 0.501919$38$ 0.513$5$94$7 0.52539

*is'%si as !'g/m.s# 7.48192$975309+,007 0.000000$7 0.00000059

CHCl3 Inlet Mean Outlet132 108.0 84.0

Spesific Hea !"p# 133.3994342$25 127.$992 122.0

K%n&u' i(i as ermal 0.1119139$42 0.1158449829 0.11977$

)ensi as !'g/m3# 0.4389884851 0.4511159482 0.4$3243

*is'%si as !'g/m.s# $.392017913580+,007 0.231$2203 0.4$3243411

H2O Inlet Mean Outlet

30 $0.0 90.0

Spesific Hea !"p# 4.183 4.20$0 4.2290

K%n&u' i(i as ermal 0.$109 0.$4555 0.$802

)ensi as !'g/m3# 998 980.35 9$2.7000

*is'%si as !'g/m.s# 0.0001131 0.00007188 0.000031

a. -enen uan jenis H+

pe= S ell an& u e

,S ell= %n%mer

, u e = H20

eng i ung laju alir s eam

e an s eam ! # = $$087.33 Kj/jam $2122 u/

Laju alir -en&ingin = 0.73 i /s 24.413981448$ p

empera ur ! 0"#

empera ur ! 0"#

empera ur ! 0"#

empera ur ! 0"#

PERHITUNGAN DE AIN COOLER

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1. enen u'an nilai L )

L ) = 47.7489497204 85.94810949$7

6 = 0.0498$

S = 0.0588235294

)ari nilai 6 &an S &i'e a ui pe H+ ang sesuai a&ala spli fl% s ell 2 u e pass

= 0.92

) m = 43.9290337428 79.0722$0737

:rgani' S%l(en , s eam = 500 , 1000 ;/m2."

< = 90 u/ .f 2% 511.02 ;/m2.%"

3. enen u'an luas permu'aan ransfer panas

Luas permu'aan panas ! # 8.729299507 f 2 0.8112731884 m2

4. enen u'an panjang &an &iame er u e

splli ring fl%a ing ea& e>c anger 'arena le i efisien mu&a &icuci&iame er luar u e !&%# 1$ mm 0.01$ m

all ic'ness 1.$ mm 0.001$ m

&iame er &alam u e !&i# 1$ mm 0.01$ m

panjang u e !l# 1 m

susunan u e e?uila eral riangular

pi c 20 mm 0.02 m

5. @umla u e

Luas 1 u e ! #= 0.05024 m2

jumla u e !A #= 173.751980$324

= 180 u e !-em ula an#

u e per pass = 90 u e

" ec' e u e,si&e (el%ci a is s age % see if i l%%'s reas%na le.

luas u e,sec i%nal aea 0.0002009$ m2

luas per pass 0.01808$4 m2

laju (%lume ri' s eam 0.000744$32 m3/s

u e si&e (el%ci !< # 0.0411708255 m/s

$. un&le an& S ell )iame er

%uler a el 12.4 f%r 2 u es passes ! riangular#

K1 = 0.249

n1 = 2.207

)iame er un&le !) # = 315.9197542094 mm

0.3159197542 m

%r a spli ,ring fl%a ing ea& e>c anger e pical s ell clearance fr%m igure 12.10

= 80 mm

)s= 395.9197542094 mm

0.3959197542 m

%" %

%" %

2. enen u'an '%efisien ransfer panas overall er&asar'an a el 8 'ern !Hea( %rgani',s eam#

s% es!ell insi"e "ia#eter$

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7. enen u'an '%efisien u e si&e ransfer panas

Are= 8984.2$$8503494 aliran la#inar

-r= 0.4$83251181 Ae

L/&i= $2.5 < 0.0494049907

@ = 0.0020 Are 10781.1202204

@ 2.00+,03

Au= 13.9892134717 Au 1$.78705$1$$1i= 5$4.4210472923 ;/m2 " i $77.30525$751

8. enen u'an '%efisien s ell ransfer panas

) 292.$9$$285103 mm '1 0.175

)s 348.$9$$285103 mm n1 2.285

rial )s/5 $9.7393257021 mm

s 48$3.573549379 mm2 0.0048$35735 m2

&e = 11.3$08 mm 0.0113$08 m

(%lume ri' fl% ra e %n s ell,si&e 9992.42929$$498

s ell,si&e (el%ci 2054544.70775419 m/6e 13458$.258$$5$8 aliran tur%ulen

-r 208.3508421394

uffle cu 25B

@ 0.002

s 1894$.$2$$272421 ;/m2 "

9. %(erall '%efisien

i& ! u e,si&e# = 0.0025

%& !s ell,si&e# = 0.0002

' = 3$ s eel

%& !c%effisien # = 5000 ;/m2 "

i& !c%effisien # = 5000 ;/m2 "

1/

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Aum er %f -asses 2 pass

emp :perasi 47.7489497204

inimum ic'nes 1.$ mm

"%rr%si%n ll% ance 4 mm

% al minimum ic'nes 150 mm

affle Spacing $9.7393257021 mm

Ser(ice lui& S eam ,-r%ces lui& %n%mer ,

u e *el%ci 0.0411708255 m/s

-ressure )r%p 3.003077374$0705+,005 ar

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1. Physical Propertiespropertis Hot Fluid

Temperature = ` 117 CHot Fluid BM Massa x p

air 18 108. 1! 0.00!001 117 .1"#$cetic $cid #0 %1#71.!8 0. & 1%10.7#

Total %1780.! 1 %"8 . 0!

propertis Hot Fluid Temperature = ` "0 CHot Fluid BM Massa x pair 18 108. 1! 0.00!001 1%&&.888$cetic $cid #0 %1#71.!8 0. & 1%81.781

Total %1780.! 1 %!%#.##

propertis Hot Fluid Temperature = ` 7".! CHot Fluid BM Massa x pair 18 108. 1! 0.00!001 1%1%.01%$cetic $cid #0 %1#71.!8 0. & 1%.%7!

Total %1780.! 1 %&!8.%87

Temperature %8 && #0Heat Capacity 0.7#887 0.% 8"% 8 .8%778'o(du'ti)itas 1.10 % " 1.1&071 1.17%1%8*is'ositas 0.0018"& 0.0018%8 0.0018%%+e(sitas 1%."# 1%&0.07 1%"".7

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;/m2 "

a m

ar

A/m 2 !-ascal#

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, ' Cp p.x '.x Cp.x , .x

0.00%" 8 1."&"% 8&.&8 71 !.8 #"!8 0.00#718 0.&%%& 7 1.%0- 00!0.001 77 0.&818% 7&.!1!&7 1%0&.71! 0.&7 &1 7&.1&%8& 0.001 #70.00&"7! 1.8%!%8% 1! .00!% 1%10.#11 0.&8#1%8 7&.!#!"& 0.001 7

, ' Cp p.x '.x Cp.x , .x0.0018% 1.11770# 0.##&&8 #.%%!1!# 0.00!!8 0.&!""7! .10- 00#

0.001&!& 0.& !107 11.&&!1! 1%7!."71 0.& %#"1 11."87 % 0.001&&70.00"%7& 1.#1%81" 10%.10 # 1%81.! 7 0.& 8%%1 11.8&1% 0.001&!#

, ' Cp p.x '.x Cp.x , .x0.00%10 1.%"0!8& 87.!771 #.0#07!7 0.00#1!& 0.&"7 "# 1.0!- 00!0.00171# 0.&88& &%. 80"1 1%&0.0&" 0.&8#0%1 &%.7#!"8 0.0017070.00"8%& 1.71 0&7 1"0.!!7& 1%.10& 0.& %17! &".%0""% 0.001718

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+ata +e(sitas / m" 117 oCsen a a n

2ater 18.00 117 0.3471 0.274 0.28571$cetic $cid $0.00 117 0.35182 0.2$954 0.2$843

Data )iscositas *k( s+ cen ip%ise

K%mp%sisi ase " +2ater

3i4uid,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0!

$cetic $cid ".8 "7 7.8!-50% #.#7- 0" 7.!#- 0#

"p = D D " E2 D ) E3 6oule mol x BM = / / ./

K%mp%sisi ase " +ater3i4uid

9.21+D01 ,4.00+,02 %.11- 0& 1.80- 0#$cetic $cid 18. && 1.10-500 %.8 - 0" %. "- 0#

ermal '%n&u' i(i i Li?ui& an& S%li& lo 10 '= $5B91 T C:;% 7K%mp%sisi ase " l%g '

ater3i4uid

,2.7$+,01 4.$1+,03 !.!&- 0# 2.95+,01$cetic $cid 1.%8"# 0.!8 " ! %.71 ,7.30+,01

Cooler - 101

+ata +e(sitas / m" #0 oCsen a a n

2ater 18.00 $0 0.3471 0.274 0.28571

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"p = D D " E2 D ) E3 6oule mol x BM = / / ./ K%mp%sisi ase " +

ater 3i4uid 9.21+D01 ,4.00+,02 %.11- 0& 8.# - 0"

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+ata +e(sitas / m" % 0 oCsen a a n

2ater 18.00 290 0.3471 0.274 0.28571-ta(ol 4$.00 290 0.2$57 0.2$395 0.23$7$cetaldehyde 44.00 290 0.28207 0.2$004 0.277$

Hidro e( 2.00 290 %.0 & 7 0." 0.%8!71-thyl $cetat 88.00 290 0.30$54 0.2585$ 0.278$cetic $cid $0.00 290 0.35182 0.2$954 0.2$843


K%mp%sisi ase " Cp

2ater

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1. - 01

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+ata +e(si/ m" "0 oCc &ensi as sen a a

$47.13 1179.13$1142458 2ater 18.00 30 0.3471592.71 1210.7$93$94149 $cetic $cid $0.00 30 0.35182

117 Data )iscosita *k( s+ cen ip%ise*isc%si as T K%mp%sisi ase

0.0023977403 117 2ater3i4uid

,1.02+D01 1.79+D03

0.00197$951 117 $cetic $cid ".8 "7 7.8!-50%

117 oC "p = D D " E2 D ) E3 6oule mol

"p T K%mp%sisi ase87.3774175$9 117 ater

3i4uid9.21+D01 ,4.00+,02

74.5154$51575 117 $cetic $cid 18. && 1.10-500

2 m / 117 oC ermal '%n&u' i(i i Li?ui& an& S%li& lo 10 '=' T K%mp%sisi ase

1."&"%0!&% 117 ater3i4uid

,2.7$+,01 4.$1+,030.&8181 7%7" 117 $cetic $cid 1.%8"# 0.!8 "

+ata +e(si/ m" "0 oCc &ensi as sen a a

$47.13 1222.$1258$$589 2ater 18.00 30 0.34711540

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#0oC "p = D D " E2 D ) E3 6oule mol"p T K%mp%sisi ase

19$$.0919797$ #0 ater3i4uid

9.21+D01 ,4.00+,02

359.1 #0

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+ata +e(si/ m" %!0 oCc &ensi as sen a a

$47.13 1034.85808$$53 2ater 18.00 250 0.347151$.25 794.7985$$95 -ta(ol 4$.00 250 0.2$57

4$1 784.4050343$2$ $cetaldeh 44.00 250 0.28207

# 0%.8% #881.!11!00#" Hidro e( 2.00 250 %.0 & 7523.3 0".1#0781117 -thyl $cet 88.00 250 0.30$54

592.71 1051.3077$7$309 $cetic $cid $0.00 250 0.3518211&!0.0&17"7"

% 0 Data )iscosit *k( s+ cen ip%ise*isc%si as 'g/m.s T K%mp%sisi ase

8.#%%1#- 00# % 0 2ater

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Cooler - %0"

$irn c &ensi as %8 &!

0.274 0.28571 $47.13 1244.8881438792 1%."# 1%"".70.2$954 0.2$843 592.71 1281.7810915992

"0" + *isc%si as T

1.77- 0% 1.%#- 0! 0.001819$959 "0 0.0018"& 0.0018%%#.#7- 0" 7.!#- 0# 0.0014543175 "0

x BM = / / ./ "0 oC

" + "p T%.11- 0& 1.!0- 07 90.$$042058 "0 90.7$88$848 8 .8%778%.8 - 0" %. "- 0# 11.4451525 "0

5B91 T C:;% 7 2 m / "0 oC" l%g ' ' T

!.!&- 0# 1.11+,01 1.11770# "0 1.10 % " 1.17%1%8! %.71 ,7.03+,01 0.& !107 "0

$irn c &ensi as %8 &!

0.274 0.28571 $47.13 1244.8881438792 1%."# 1%"".73183

"0" + *isc%si as T

1.77- 0% 1.%#- 0! 0.001819$959 "0 0.0018"& 0.0018%%1.025 "0

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x BM = / / ./ "0 oC" + "p T

%.11- 0& &.&!- 0! 89.4$355 "0 90.7$88$848 8 .8%778345.9 "0

5B91 T C:;% 7 2 m / "0 oC

" l%g ' ' T!.!&- 0# 1.11+,01 1.11770# "0 1.10 % " 1.17%1%8

0.1!01 "0

n c &ensi as

0.274 0.28571 $47.13 1145.2008$25359

0.2$395 0.23$7 51$.25 899.99943$$738

1#0" Cp *isc%si as 'g/ T

1.#%- 0! 0.003139928 ".1&- 00# 1#0&.&!- 0! 0.0049545938 &. !- 00# 1#0

x BM = / / ./ 1#0 oC" + + "p T

%. - 0! 1.78- 08 ".# - 1% 33.28102$90$$ 1#01.10- 0& 1.!0- 07 &.##- 11 4$.9982482714 1#0

CT;% 2 m / 1#0 oC" K T

&. #- 08 8.0$+,03 1#08.!0- 08 1.42+,03 1#0

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n c &ensi as

0.274 0.28571 $47.13 1070.2$5$$0759

0.2$395 0.23$7 51$.25 829.758$04$18

0.2$004 0.277$ 4$1 834.1219887495

0." 0.%8!71 # 0%.8% #8 !.#" !7 10.2585$ 0.278 523.3 &8.1"!!1# !0.2$954 0.2$843 592.71 1091.02513510$9

11##8. &8!

%!0" Cp *isc%si as 'g/m.s T

4.29+,01 1.#%- 0! 0.00$94115 #. &11!- 00# %!0".07- 01 &.&!- 0! 0.00755715$3 7.!!71#- 00# %!0".0%- 01 &.%&- 0! 0.007303575 7."0"!8- 00# %!0%.1%- 01 ".%8- 0! 0.0078708 7.8708- 00# %!0".07- 01 7.11- 0! 0.00$3111$88 #."1117- 00# %!0%."!- 01 %.%1- 0& 0.0043919375 &." 1 &- 00# %!0

&.0"7!8- 00!

6oule mol x BM = / / ./ %!0 oC" + + "p T

,8.42+,03 %. - 0! 1.78- 08 ".# - 1% 33.43338$719 %!01.11- 01 1.10- 0& 1.!0- 07 &.##- 11 59.407722$5$ %!0&.00- 0% 1.!#- 0& 1.#&- 07 &.7%- 11 51.53128125 %!0%.0%- 0% ".8!- 0! ".1 - 08 8.7#- 1% 28.498099$09 %!08.%"- 0% ".7%- 0& &.11- 07 1.%&- 10 107.713$3281 %!0".7#- 0% %.8"- 0& ".08- 07 .%#- 11 57.505429$88 %!0

""8.08 #

'= $5BT5CT;% 2 m / %!0 oC" K T

4.71+,05 &. #- 08 1.23+,02 %!0&."#- 0! 8.!0- 08 5.35+,03 %!0%.1%- 0! 8.0%- 08 3.49+,03 %!0&.! - 0& #.& - 08 1.54+,01 %!0&.8#- 0# 1.1%- 07 8.5$+,04 %!0#.#0- 0# 1.1#- 07 $.91+,04 %!0

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1.77- 01

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Heater H 10%

+ata +e(sitas / m"sen a a

2ater 18.00-ta(ol 4$.00

$cetaldehyde 44.00?+-?@-A / %01

+ata +e(sitas / m"sen a a

2ater 18.00-ta(ol 4$.00$cetaldehyde 44.00

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Hidro e( 2.00-thyl $cetat 88.00$cetic $cid $0.00

Data )iscositas *k( s+

K%mp%sisi ase2ater

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Heater H %0%

+ata +e(si/ m" 1#0sen a a

2ater 18.00 1$0

-ta(ol 4$.00 1$0

Data )iscosita *k( s+ cen ip%ise

K%mp%sisi ase2ater

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"0 oC air 100n c &ensi as

30 0.3471 0.274 0.28571 $47.13 1244.8881439 11 %.%7%30 0.2$57 0.2$395 0.23$7 51$.25 987.9391322

30 0.28207 0.2$004 0.277$ 4$1 1058.0137087"0 0.34908 0.24902 0.1541 723 1389.18$$77$

cen ip%ise "0" + *isc%si as T

,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0! 0.001819$959 "0 0.00%%71#.&& 1.1%-50" 1."7- 0% 1.!!- 0! 0.001$3922$1 "0

#.#171 #.81-50% %.00- 0% %.!#- 0! 0.0015399$$8 "018.%1!% &.%"-50" %.87- 0% 1.#7- 0! 0.002174$328 "0

6oule mol x BM = / / ./ "0 oC" + "p T

9.21+D01 ,4.00+,02 %.11- 0& #. 0- 0& 109.29$2$5 "0 8!. &7&! ."&% ".#&-501 1.1%- 0" 1.80- 0# 1149.121241 "0&!.0!# &.& - 01 1.##- 0" %.70- 0# 57.09017 "0

lo 10 '= $5B91 T C:;% 7 2 m / "0 oC" l%g ' ' T

,2.7$+,01 4.$1+,03 !.!&- 0# 1.11+,01 1.11770!!7!8 "0 1."10%%#1."17% 0.# 87 !1#.%! ,$.30+,01 0.!"%&0!!&& "01.&8%# 0. 8%1 ,5.19+,01 0.! & !#""1 "0

118 oCn c &ensi as

118 0.3471 0.274 0.28571 $47.13 1178.358$934

118 0.2$57 0.2$395 0.23$7 51$.25 929.8340$311

118 0.28207 0.2$004 0.277$ 4$1 975.48889414

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118 %.0 & 7 0." 0.%8!71 # 0%.8% # &%.0"118 0.30$54 0.2585$ 0.278 523.3 1080.!&7118 0.35182 0.2$954 0.2$843 592.71 1209.924$485

cen ip%ise 118" Cp *isc%si as 'g/m.s T

,3.$8+D01 4.29+,01 1.#%- 0! 0.0013570431 0.000001"!7 1181.& ".07- 01 &.&!- 0! 0.0037154054 ".71!&0!&&- 00# 1180.0# ".0%- 01 &.%&- 0! 0.00351$9292 ".!1# % %"- 00# 118

%7.7!8 %.1%- 01 ".%8- 0! 0.0052317293 !.%"17% %8- 00# 118".07- 01 7.11- 0! 0.002$00$935 %.#00# "!%- 00# 118

%8.## %."!- 01 %.%1- 0& 0.0002157194 %.1!71 "88- 007 118

6oule mol x BM = / / ./ 118" + + "p T

3.39+D01 ,8.42+,03 %. - 0! 1.78- 08 ".# - 1% 33.3274453$7 118%7.0 1 1.11- 01 1.10- 0& 1.!0- 07 &.##- 11 41.42337$984 118

"&.1& &.00- 0% 1.!#- 0& 1.#&- 07 &.7%- 11 40.778201885 118%!." %.0%- 0% ".8!- 0! ".1 - 08 8.7#- 1% 27.29392950$ 118# .8&8 8.%"- 0% ".7%- 0& &.11- 07 1.%&- 10 84.08$121271 118

"&.8! ".7#- 0% %.8"- 0& ".08- 07 .%#- 11 42.744341985 118

'= $5BT5CT;% 2 m / 118 oC" K T

5.30+,04 4.71+,05 &. #- 08 $.09+,03 1180.00!!# &."#- 0! 8.!0- 08 ,4.13+,04 1180.00181 %.1%- 0! 8.0%- 08 $.90+,04 1180.0" !1 &.! - 0& #.& - 08 9.37+,02 1180.00%07 &.8#- 0# 1.1%- 07 1.50+,03 1180.00%"& #.#0- 0# 1.1#- 07 1.5$+,03 118

:( = .

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oC +ata +e(sin c &ensi as sen a a

0.3471 0.274 0.28571 $47.13 1145.2008$25359 2ater

0.2$57 0.2$395 0.23$7 51$.25 899.99943$$738 -ta(ol

1#0" Cp *isc%si as 'g/ T

4.29+,01 1.#%- 0! 0.003139928 ".1&- 00# 1#0".07- 01 &.&!- 0! 0.0049545938 &. !- 00# 1#0

6oule mol x BM = / / ./ 1#0 oC

" + + "p T,8.42+,03 %. - 0! 1.78- 08 ".# - 1% 33.28102$90$$ 1#0

1.11- 01 1.10- 0& 1.!0- 07 &.##- 11 4$.9982482714 1#0

'= $5BT5CT;% 2 m / 1#0 oC" K T

4.71+,05 &. #- 08 8.0$+,03 1#0&."#- 0! 8.!0- 08 1.42+,03 1#0

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air #0 +ata +e(si/ m" #0 oCsen a a

1%%%.#1%!8### 2ater 18.00 $0 0.3471 0.274-ta(ol 4$.00 $0 0.2$57 0.2$395

$cetaldeh 44.00 $0 0.28207 0.2$004


K%mp%sisi ase "0.001 %71187 2ater 3i4uid ,1.02+D01 1.79+D03 1.77- 0%

-ta(ol #.&& 1.1%-50" 1."7- 0%$cetaldehyde #.#171 #.81-50% %.00- 0%

"p = D D " E2 D ) E3 6oule mol x BM =K%mp%sisi ase "

88.8 #11% ater3i4uid

9.21+D01 ,4.00+,02 %.11- 0&-ta(ol ! ."&% ".#&-501 1.1%- 0"$setaldehid &!.0!# &.& - 01 1.##- 0"

ermal '%n&u' i(i i Li?ui& an& S%li& lo 10 '= $5B91 T C:K%mp%sisi ase "

1.%1#! 1801" ater3i4uid

,2.7$+,01 4.$1+,03 !.!&- 0#-ta(ol 1."17% 0.# 87 !1#.%!$setaldehid 1.&8%# 0. 8%1

+ata +e(sitas / m" 0 oCsen a a n c

2ater 18.00 90 0.3471 0.274 0.28571 $47.13-ta(ol 4$.00 90 0.2$57 0.2$395 0.23$7 51$.25$cetaldehyde 44.00 90 0.28207 0.2$004 0.277$ 4$1

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Hidro e( 2.00 90 %.0 & 7 0." 0.%8!71 # 0%.8%-thyl $cetat 88.00 90 0.30$54 0.2585$ 0.278 523.3$cetic $cid $0.00 90 0.35182 0.2$954 0.2$843 592.71

Data )iscositas *k( s+ cen ip%iseK%mp%sisi ase " Cp2ater

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/ m" %#0 oCn c &ensi as

18.00 2$0 0.3471 0.274 0.28571 $47.13 10$1.5517$

4$.00 2$0 0.2$57 0.2$395 0.23$7 51$.25 821.27878182


K%mp%sisi ase " Cp *isc%si as 'g/2ater

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+ata +e(si/ m"n c &ensi as sen a a

0.28571 $47.13 1222.$1258$7 2ater 18.000.23$7 51$.25 9$8.718$0919 oC

0.277$ 4$1 1030.$399282Data )iscosita *k( s+

K%mp%sisi ase2ater 3i4uid

#0+ *isc%si as T

1.%#- 0! 0.0019271187 #0 "p = D D " E2 D ) E31.!!- 0! 0.0017952231 #0 K%mp%sisi ase%.!#- 0! 0.0018913137 #0 ater 3i4uid

ermal '%n&u' i(i i Li?ui&/ / ./ #0 oC K%mp%sisi ase

+ "p T ater 3i4uid.00-501 19440088.89$ #01.80- 0# 2237.173$88 #0%.70- 0# $$.57248 #0

;% 7 2 m / #0 oCl%g ' ' T1.9$+,01 1.%1#! % #0

,$.43+,01 0.!%!8!" #0,5.39+,01 0.!8"&1! #0

air %8 C $ir #0 C&ensi as &ensi as 1%."# 1%"0.081 +ata +e(si/ m"

1199.9295233 *iscos 0.0018"& 0.0018! sen a a 948.91098478 Cp 90.7$88$848 8 .!%778 2ater 18.001002.5120714 / 1.10 % " 1.1878

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# !1.8"8 Data )iscosita *k( s+110#."# K%mp%sisi ase

1233.31$228$ 2ater 3i4uid

"p = D D " E2 D ) E3

K%mp%sisi ase

ater 3i4uid$ir %8 C

0 ermal '%n&u' i(i i Li?ui&*isc%si as 'g/ T K%mp%sisi ase1.#!- 007 0 ater 3i4uid%.88- 00# 0%.# - 00# 0&.##- 00# 01.78- 00# 0

!.7- 007 0

0oC+ "p T

".# - 1% 33.404812499 0&.##- 11 37.821389152 0&.7%- 11 38.8913$9891 08.7#- 1% 2$.925438975 01.%&- 10 79.97$583891 0

.%#- 11 40.311318074 0

2 m / 0 oC T

000000

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%#0 T

%#0%#0

%#0

"p T33.4$9395352 %#0$0.80940242$ %#0

%#0 T

%#0%#0

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%8 oC +ata +e(sin c &ensi as sen a a

28 0.3471 0.274 0.28571 $47.13 124$.3595022 2ater

cen ip%ise %8 Data )iscosita" + *isc%si as T K%mp%sisi

,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0! 0.00183377$8 %8 2ater

6oule mol x BM = / / ./ %8 oC "p = D D" + "p T K%mp%sisi

9.21+D01 ,4.00+,02 %.11- 0& 0.00-500 90.7$88$848 %8 8!. &7& ater

n& S%li& lo 10 '= $5B91 T C:;% 7 2 m / %8 ermal '%n&" l%g ' ' T K%mp%sisi

,2.7$+,01 4.$1+,03 !.!&- 0# 1.04+,01 1.10 % " %8 ater

!0oCn c &ensi as

50 0.3471 0.274 0.28571 $47.13 1230.081378

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cen ip%ise !0" + *isc%si as T

,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0! 0.0018503135 !0

6oule mol x BM = / / ./ !0" + "p T

9.21+D01 ,4.00+,02 %.11- 0& 0.00-500 89.527775 !0

n& S%li& lo 10 '= $5B91 T C:;% 7 2 m / !0" l%g ' ' T

,2.7$+,01 4.$1+,03 !.!&- 0# 1.72+,01 1.1878 !0

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/ m" &0 oCn c &ensi as

18.00 40 0.3471 0.274 0.28571 $47.13 1237.50$1$82

*k( s+ cen ip%ise &0ase " + *isc%si as T

3i4uid ,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0! 0.0018039$15 &0

" E2 D ) E3 6oule mol x BM = / / ./ &0 oCase " + "p T

3i4uid 9.21+D01 ,4.00+,02 %.11- 0& 0.00-500 90.117232 &0

' i(i i Li?ui& an& S%li& lo 10 '= $5B91 T C:;% 7 2 m / &0ase " l%g ' ' T

3i4uid ,2.7$+,01 4.$1+,03 !.!&- 0# 1.44+,01 1.1!!" &0

Pompa P %0"+ata +e(si/ m" 11! oC

sen a a n2ater 18.00 115 0.3471 0.274 0.28571-ta(ol 4$.00 115 0.2$57 0.2$395 0.23$7$cetaldeh 44.00 115 0.28207 0.2$004 0.277$Hidro e( 2.00 115 %.0 & 7 0." 0.%8!71

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-thyl $cet 88.00 115 0.30$54 0.2585$ 0.278$cetic $cid $0.00 115 0.35182 0.2$954 0.2$843


K%mp%sisi ase " +

Hi&r%gen 7.01!& &.08-501 %."7- 01 ,4.08+,03ir ,1.02+D01 1.79+D03 1.77- 0% 1.%#- 0!

+ an%l #.&&0# 1.1%-50" 1."7- 0%sam se a ".8 "7 7.8!-50% #.#7- 0" 7.!#- 0#se al&e i& #.#171 #.81-50% %.00- 0% %.!#- 0!

+ il se a ".#8#1 !.!%-50% 8.00- 0" ,1.04+,05

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$ir80 &0

1%07.!"8 1%"7.!0#

0.00%10& 0.00180&

87.!0#17 0.117%"

1.%##777 1.1!!"

c &ensi as

$47.13 1180.$893529

51$.25 931.90722734

4$1 978.42282521# 0%.8% # &".08

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523.3 108"."&!592.71 1212.45$$847

11!*isc%si as T

0.0034992453 11!0.002383$1$8 11!0.0022702497 11!

0.0019$3041 11!0.0024245983 11!0.0020328$18 11!

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-ta(ol 10$.12 390 0.2$57 0.2$395 0.23$7 51$.25

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54/285

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55/285

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$90.05238$82

1070.9837007

$28.5894894$

772.93259323#8.0!

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,6- PERHITUNGAN HEATER *H.,/,+ungsi = emanas'an air

1. - sical -r%per ies pr%per is "%l& lui&

= 28 "Hot 0lui" assa > p , '

air 18.00 154099 1 124$.4 2+,03 1.10 % %# Total 1!&0 1 1%.& %- 0" 1.10 % %#

p.> '.> "p.>1%."! ! 1.10 % %# 0.7#88#8

pr%per is "%l& lui& = $0 "

Hot 0lui" assa > p , ' air 18.00 154099 1 1%"7.!0#% 0.00180& 1.1!!"

Total 1!&0 1 p.> '.> "p.>

1%"7.!0#% 1.1!!" 0.117%"% pr%per is H% lui& "7!".7#87 ".!#%&!%! %10.%7"!&

= 44 "Hot 0lui" assa > p , ' air 18.00 154099 1 1%&1. "%8 0.001818 1.1"%"&1"

Total 1!&0 1 p.> '.> "p.>

1%&1. "%8 1.1"%"&1" 0.&&"0!"8% .% % %.!8!!1%# %78.8##07

p = &ensi as Kg/m3G = (is'%si as 'g/m.s' = ermal K%n&u' i(i"- = Hea "apaci K@/Kg "

-r%per is H% lui&

80 $0 40"- 87.50$1$8 88.8117 90.117232K 1.27 1.2110834238 1.1553899844, 0.00210408 0.001954021 0.0018039$15

1207.54 1222.522077 1237.50$1$82

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)esign +,101ungsi

en&ingin'an asil &ari i&r%lisa se elum masu' 'e rea' %r fermen %r

enen u'an laju alir s eam44$30.41 Kg/jam

12.39733721 Kg/s

s eam = 3.4+D0$ K@/ 31492$8.4854 u/930$34.8952 @/s 1237.$$25148 H-

enen u'an @enis H+H+ = S ell an& u eS ell = ir -en&ingin

u e = S eam

K%n&isi %perasia. lui&a panas

82.4

140 . lui&a &ingin

17$

104

I L ) =

I L ) = 28.189$5872

6 = 0.8 S = 0.7$923077

)ari igure 12.20 !2 s ell passes 4 u e passes# % ler &an Sinn% al 818 &iper%le arga = 0.77

21.70$0372

enen u'an I L )

empera ur masu' ! 1 # %

empera ur 'eluar ! 2# %


empera ur 'eluar ! 2 # %

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)ari a el 12.1 % ler &an Sinn% al 797 &iper%le arga

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64/285

$. un&le an& S ell )iame er % ler a el 12.4 f%r 4 u es passes ! riangular#

K1 = 0.175n1 = 2.285

) = 387.$2389$7 mm

0.387$23897m%r a spli ,ring fl%a ing ea& e>c anger e pical s ell clearance fr%m igure 12.10

e pical S ell clearance is 54 mm

)s= ) D &is

)s= 441.$2389$7 mm0.441$23897m


6e = 1290$.49207 le i esar &ari 2100 ma'a aliran a&ala ur ulen-r = 143.293107$

l/&i = 337.15441$7fr%m figure 12.23 &i&apa j = 4.0+,03

&engan " u/ laru an (isc%si as ren&a a&ala

Au = 2$5.7189$9$

i = 21$99.78$88 ;/m2. "

8. enen u'an K%efisien S ell,si&e ransfer panasK1 = 0.175n1 = 2.285

) = 387.235792 mm

0.387235792 mm&is fr%m figure 12.10 c emical engineering &esign

&is = $3 mm)s = 450.235792 mm

0.450235792m uffle spacing = )s/5 = 90.0471584 mm

91mm (pembulatan )s = 8190.84988 mm2

0.00819085 m2&e = 2.71703097 mm

0.00271703 m1.1 9/ ;%G0.1 7. ;%:

. := ##! . (& /

1 :=% ( /' ;91 1:/

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s = 0.10294083 m3/s(s = 10.$82$1$5 m/s6e= 14973.9123 aliran le i &ari 2100 a&al-r = 8+D02

uffle cu 25 Bfr%m figure 12.29 j = 5.3+,03

s = $87393.919 ;/m2"

meng i ung c%eficien %(erall ! < # = 21$99.78$88 ;/m2."

s = $87393.9187 ;/m2."i& = 0.0003 ;/m2."%& = 0.0002 ;/m2."

&i = 0.01483 m&% = 0.01905m

' = 45 ;/m."

< = 1429.9$3938 ;/m2."

eng i ung -ressure )r%p u e si&e&i = 0.01483 m jf fr%m figure 12.24 = 5.3+,03( = 1.391039734 m/s6e = 1290$.49207-asses 2

-ressure )r%p u e = " 7"0.!#7# 0." 7"0!7 ar

Para#eter Nilai&'eteran(an atuan

ipe S ell an& u e ,

@umla u e 171 ua

-anjang 5 m

)iame er S ell 450.2357919952 mm

Aum er %f -asses u e 4 pass

emp :perasi 28.189$587212



% al minimum ic'ne 150 mm

affle Spacing 91 mm

A/m 2 !-ascal#

%"

* = ( .% :

, = :.("/% . - .* ;0.""

=1 9991 :5 : 5 l( :: 51 5 :, , % % /% (% (% /% "$ , , %

I .1= =

& 98 . :5%.!:. .= .1# ( /% ( ;%: %

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Ser(ice lui& s eam ,

-r%ces lui& ;a er ,

u e *el%ci 1.3910397339 m/s

-ressure )r%p 0.397305$758 ar

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"p0.7#88#80.7#88#8

, .x0.0018""8

- 0"

"p0.117%"%

, .x0.00180&

7- 0"

"p0.&&"0!

, .x0.001818

7- 0"

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JB =,$ =

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72/285

-a&a s ell a&ala flui&a panas &an u e a&ala flui&a &in

5. eng i ung jumla u e)ari a el 10 Kern al 843 &ipili pipa J

:) = 1.50C) = 1.37;F = 1$

l% area/ u e !a # = 1.47

= 0.3925-anjang !L# = 12@umla u e ! A # =

L.= 11$.$0987= 29248

jumla u e per pass = 3$5$

)ari Kern a el 9 al 841 &ipili spesifi'asi 3/4 in :) s-a&a u e J

:) =;F =

s?uare pi c =

Karena 200 f2

ma'a ipe H+ ang &iguna'an a&alaa&ala flui&a panas &an u e a&ala flui&a &ingin.

Surface per line !a %#

:

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-anjang =-a&a s ell J

C) s ell = 39uffle = 0 5 C) s ell

= 19.5-ass = 2

$. eng i ung nilai &an

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Are = F . )e ur ulen G

Are = M6+ N > 0.114137$70.00000000

= M6+ NM6+ N

)ari figure 24 Kern al 834 er&asar'an nilai Are &i &apa nilai jH ai jH 700

i = jH ' "p.G)e '

= 700 > 0.000 0.+D000.114 0.000

= M)C*/0Na'a nilai i% Ji% = 0.000 i C

:= M)C*/0N > 1.37

0.75

= M)C*/0N

8. -a&a s ell un u' flui&a panasa. eng i ung fl% area ! as #

as = C)." .

Ke erangan Jas =C) = )iame er &alam s ell ! in #

= @ara' uffle ! in #= pinc ! in #

" == 1.125 in

as = 39 > 1.125144 >

= 3.1$9

. Kecepa an massa flui&a panas

u/ .f 2.%

u/ .f 2.%

144.-

Luas aliran flui&a ! f 2 #

-

clereance ! - , :) #

f 2

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Fs =a

= 03.1$9

= 0

c. eng i ung arga %"p = 0' = 0.000G = 0.000 l /f .)e = 0.950 in

= 0.07917 f

Are = Fs. )eG

Are = 0.0 >0.000

= M)C*/0N)ari figure 28 Kern al 838 er&asar'an nilai Are &i &apa nilai jH ai

jH 1000

i = jH

' ")e

= 1000 > 0.000 00.079 0.000

= M)C*/0N

&. eng i ung nilai

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= M)C*/0N ,M)C*/0N >

= M)C*/0N)ari u'u Kern al 845 &iper%le nilai 6& min ai uS ara isa &iguna'an J

6& 6& minM)C*/0N 0.0005

Ailai 6& memenu i s ara

9. eng i ung penurunan e'anana. -a&a u e

F = M6+ NL = 12 fn = M6+ N

C) = 1.37 in = Are = M6+ N

)ari figure 2$ al 83$ &iper%le nilai f ai u

I-s =

0.0002 > M6+ N > 125.+D10 > 0.114 > 1

= M6+ N psia

= 4n >s 2g

-a&a figure 27 Kern al 837 un u' nilai F M6+ N0.0025

= 0.072g

= 4 > M6+ N1

= M6+ N psi

l / .f 2

eng i ung p 'arena panjang pipa

f > F 2 > L > n5.22 10 10> C) >

eng i ung p 'arena u e passes- r * 2

* 2

- r

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= D= M6+ N= M6+ N

O 10 psi ma'a s ara

. -a&a s ellFs = 0L = 12

= 19.500= 1.$25

)e = 0.950= 0.079

Are = M)C*/0N

)ari figure 29 al 839 &iper%le nilai f ai u

an a'n a cr%sses AD1 = 12 L

an a'n a cr%sses AD1 = 12

an a'n a cr%sses AD1 = 88.$2

=

0.0011 > 0.0 1.$255.+D10 > 0.0791 > 1

= 0.000 psi

O 2 psi ma'a s ara

6ing'asan c%%ler !"% , 02#ungsi J men&ingin'an 'eluaran mi>er ,102ipe J S ell an& u e ea e>c anger

Luas ransfer panas ! # J 137758.08

K%efisien %(erall ea ransfer !

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S ell si&eC) s ell J 39

uffle J 19.5u e si&e

:) J 0.75;F J 1$

S?uare pi c J 1.88@umla u e J 29248-anjang J 12

J M6+ NI-s J 0.000

I-

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- 0"

0.00# 1!%

0.00# 7%"

7/24/2019 HE, pompa

80/285

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in.

inin

f

a%u eu e

u e

uare pi c &iper%le J

0.75 in1$

1.875 in

hell and tube. -a&a s ell

in2

f 2/f

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12f

in

in

)

f 2

m2

7/24/2019 HE, pompa

83/285

u

P

0

)

> 19.51.875

1,&3

1,&3

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s

0.07917

u

.G

0.000

M)C*/0NM)C*/0N

l / .f 2

E1/3

E1/3

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1.0531.053

0.0005

0.114 f

0.0002

> M6+ N

&iper%le J

> 0.07

f 2/in2

l / .f 2

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D M6+ N psi

erpenu i.

finfinf

0.0011

> 121.$25

> 88.$2> 2

erpenu i.

;/m2 "

l / .f 2

f 2/in2

f 2

u/ .f 2. %

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inin

in

in

f

psi psi

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PERHITUNGAN COO ER E.,/,ungsi = en&ingin'an -r%&u'

1. - sical -r%per ies pr%per is H% lui&

$0 "Hot 0lui" assa > p ,air 18.00 1$25$9 0.88 1222.$ 2+,03 p ,air 18.00 109 0.00500057 1%&&.8881&& 0.0018%

lucose 180.00 21$72 0.99499943 "18" 1.0%! Total %1780 1

p.> '.>#.%%!1!#"1& 0.00!!8

"1#7.08"17 0.1& "&"17"."08"%7 0.1!& "

pr%per is H% lui&empera ure = Q 45 "

Hot 0lui" assa > p ,air 18.00 109 0.00500057 1%"".7!0"#! 0.00187"

lucose $0.00 21$72 0.99499943 %"#1.! 1.0%&! Total %1780 1

p.> '.>#.1# 0.00!8"#%"& .# 11&" 0.1!#"%"!!.8#0#0& 0.1!%&

p = &ensi as Kg/m3G = (is'%si as 'g/m.s' = ermal K%n&u' i(i"- = Hea "apaK@/Kg "

-r%per is H% lui&empera ure 28 3$.5 45

Hea "apaci 85.9474 87.42175$ 88.89$112

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'%n&u' i(i as 1.31 1.2$34089271 1.21$5918*is'%si as 0.0022713355 0.0020992271 0.00192712)ensi as 1192.27 1207.4421$78204 1222.$1259

)esign +,101

ungsi en&ingin'an asil &ari i&r%lisa se elum masu' 'e rea' %r fermen %r

enen u'an laju alir s eamLaju lir s eam 8$484.39 Q

24.0234428425 Kg/s s eam = 1.9+D0$ K@/ 1820045.2 u/

537838.4159$771 @/s 715.2777$3 H-enen u'an @enis H+

H+ = S ell an& u eS ell = ee& 6ea' %r ! %rgani' #

u e = ir -en&ingin

K%n&isi %perasia. lui&a panas

140

8$

. lui&a &ingin82.4

113

I L ) =

I L ) = 11.$134$21$74

6 = 1.7$47058824 S = 0.53125

)ari igure 12.20 !2 s ell passes 4 u e passes# % ler &an Sinn% al 818 &iper%le arga = 0.$4

2. enen u'an I L )

empera ur masu' ! 1 # % a(e =empera ur 'eluar ! 2# %

a(e =


empera ur 'eluar ! 2 # %

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90/285

7.432$1579

)ari a el 12.1 % ler &an Sinn% al 797 &iper%le arga

7/24/2019 HE, pompa

91/285

$. un&le an& S ell )iame er % ler a el 12.4 f%r 4 u es passes ! riangular#

K1 = 0.175n1 = 2.285

) = $59.525$839032 mm

0.$59525$839m%r a spli ,ring fl%a ing ea& e>c anger e pical s ell clearance fr%m igure 12.1

e pical S ell clearance is $3 mm

)s= ) D &is

)s= 722.525$839032 mm0.722525$839m


6e = $913.430553$451 le i 'ecil &ari 2100 ma'a aliran a&ala ur ulen-r = 0.14525$311$

l/&i = 337.15441$7229fr%m figure 12.23 &i&apa j = 3.9+,03

&engan " u/ laru an (isc%si as ren&a a&ala

Au = 14.2$47040493

i = 1215.249793547 ;/m2. "

8. Me(e(tu'a( /oeKsie( @hell side tra(s er pa(as/1 = 0.17!(1 = %.%8!

+ = #! .&7"1008&7 mm

0.#! &7"1008 mm&is fr%m figure 12.10 c emical engineering &esign

&is = $3 mm)s = 722.473100847 mm

0.7224731008m uffle spacing = )s/5 = 144.494$201$94 mm 145 mm

s = 20942.920378 mm20.0209429204 m2

&e = 2.7170309$75 mm0.002717031m

1.1 9/ ;%G0.1 7. ;%:

. := ##! . (& /

1 :=% ( /'

;91 1:/

=

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s = 9.245239708$ m3/s(s = 441.4494035 m/s6e= 2.772+D03 aliran &ari-r = 2380.421975

uffle cu 25 Bfr%m figure 12. 1.3+,02

s = 2$297.555354 ;/m2"

meng i ung c%eficien %(erall ! < # = 1215.249793547 ;/m2."

s = 2$297.555354177 ;/m2."i& = 0.00042 ;/m2."%& = 0.0002 ;/m2."

&i = 0.01483 m&% = 0.01905 m

' = 45 ;/m."

< = 529.7795218848 ;/m2."

eng i ung -ressure )r%p&i = 0.01483 m jf fr%m figure 12.24 =( = 0.81048$0472 m/s6e = $913.430553$451-asses 2

-ressure )r%p = 1""%1.% " #7% 0.1""%1"Karena pressure &r%p 'urang &ari 0.8 ar ma'a la a' &iguna'an

Para#eter Nilai&'eteran(an atuan

ipe S ell an& u e ,

@umla u e 57$ ua

-anjang 5 m

)iame er S ell 722.473100847 mm

Aum er %f -asses u 4 pass

emp :perasi 11.$134$21$74



% al minimum ic' 150 mm

affle Spacing 145 mm

A/m 2 !-ascal#

%"

* = ( .% :

, = :.("/% . - .* ;0.""

.=

1 9991 :5 : 5 l( :: 51 5 :, , % % /% (% (% /% "$ , , %

0& 98 . :5%.!:. .= .1# ( /% ( ;%: %

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' "p1.%1#! % 1 ##.0 %

0.1&&! "! .11."#10 % %"%!.1 %

"p.> , .x17"0.1#1 0.001# #

&".0 % 0.1%%881- 01

' "p1.11770# 8 ."!!

0.1!01 "&!.

"p.> , .x0.&&7"# .10- 00#"&&.170" 1.01 87&"&&.#177 1-500

' "p1.1#71& 10%7.778

0.1&7" "!%.!

"p.> , .x!.1" &8 ."7- 00#

"!0.7"7" 1.01 "77"!!.87#8 1-500

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-a&a s ell a&ala flui&a panas &an u e a&ala flui&a

5. eng i ung jumla u e)ari a el 10 Kern al 843 &ipili pipa J

:) = 1.50C) = 1.37;F = 1$

l% area/ u e !a # = 1.47

= 0.3925-anjang !L# = 12@umla u e ! A # =

L.= 393.$19543= 29248

jumla u e per pass = 3$5$

)ari Kern a el 9 al 841 &ipili spesifi'asi 3/4 in :)m2 -a&a u e Jm2 :) =m3/s ;F =m/s s?uare pi c =

Karena 200 f2

ma'a ipe H+ ang &iguna'an a&alas ell a&ala flui&a panas &an u e a&ala flui&a &ingin

Surface per line !a %#

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-anjang =-a&a s ell J

C) s ell = 39uffle = 0 5 C) s ell

= 19.5-ass = 2

$. eng i ung nilai &an

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Are = F . )e2100 a&ala ur ulen G

Are = M6+ N > 0.114137$70.00000000

= M6+ NM6+ N

)ari figure 24 Kern al 834 er&asar'an nilai Are &i &apa nilai jH jH 700

i = jH ' "p.G)e '

= 700 > 0.000 0.+D000.114 0.000

= M)C*/0Na'a nilai i% Ji% = 0.000 i C

:= M)C*/0N > 1.37

0.75

= M)C*/0N5.3+,03

8. -a&a s ell un u' flui&a panasa. eng i ung fl% area ! as #

as = C)." .

ar

as =C) = )iame er &alam s ell ! in #

= @ara' uffle ! in #= pinc ! in #

" == 1.125 in

as = 39 > 1.125144 >

= 3.1$9

. Kecepa an massa flui&a panas

u/ .f 2.%

u/ .f 2.%

144.-

Luas aliran flui&a ! f 2 #

-

clereance ! - , :) #

f 2

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Fs =a

= 03.1$9

= 0

c. eng i ung arga %"p = 0' = 0.000G = 0.000 l /f .)e = 0.950 in

= 0.07917 f

Are = Fs. )eG

Are = 0.0 >0.000

= M)C*/0N)ari figure 28 Kern al 838 er&asar'an nilai Are &i &apa nilai jH

jH 1000

i = jH

' ")e

= 1000 > 0.000 00.079 0.000

= M)C*/0N

&. eng i ung nilai

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= M)C*/0N ,M)C*/0N >

= M)C*/0N)ari u'u Kern al 845 &iper%le nilai 6& min ai uS ara isa &iguna'an J

6& 6& minM)C*/0N 0.0005

Ailai 6& memenu i s ara

9. eng i ung penurunan e'anana. -a&a u e

F = M6+ NL = 12 fn = M6+ N

C) = 1.37 in = Are = M6+ N

)ari figure 2$ al 83$ &iper%le nilai f ai u

I-s =

0.0002 > M6+ N > 125.+D10 > 0.114 > 1

= M6+ N psia

= 4n >s 2g

-a&a figure 27 Kern al 837 un u' nilai F M6+ N0.0025

= 0.072g

= 4 > M6+ N1

= M6+ N psi

l / .f 2

eng i ung p 'arena panjang pipa

f > F 2 > L > n5.22 10 10> C) >

eng i ung p 'arena u e passes- r * 2

* 2

- r

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= D= M6+ N= M6+ N

O 10 psi ma'a s ara

. -a&a s ellFs = 0L = 12

= 19.500= 1.$25

)e = 0.950= 0.079

Are = M)C*/0N

)ari figure 29 al 839 &iper%le nilai f ai u

an a'n a cr%sses AD1 = 12 L

an a'n a cr%sses AD1 = 12

an a'n a cr%sses AD1 = 88.$2

=

0.0011 > 0.0 1.$255.+D10 > 0.0791 > 1

= 0.000 psi

O 2 psi ma'a s ara

6ing'asan c%%ler !"% , 02#ungsi J men&ingin'an 'eluaran mi>er ,102ipe J S ell an& u e ea e>c anger

Luas ransfer panas ! # J 137758.08

K%efisien %(erall ea ransfer !

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S ell si&eC) s ell J 39

uffle J 19.5u e si&e

:) J 0.75;F J 1$

S?uare pi c J 1.88@umla u e J 29248-anjang J 12

J M6+ NI-s J 0.000

I-

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1- 01

1.01 88&

1.01 "8#

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ingin.

inin

f

a%u eu e

u e

s?uare pi c &iper%le J

0.75 in1$

1.875 in

shell and tube. -a&a.

in2

f 2/f

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12f

in

in

)

f 2

m2

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ai u

P

0

)

> 19.51.875

1,&3

1,&3

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s

0.07917

ai u

.G

0.000

M)C*/0NM)C*/0N

l / .f 2

E1/3

E1/3

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1.7781.778

0.0005

0.114 f

0.0002

> M6+ N

&iper%le J

> 0.07

f 2/in 2

l / .f 2

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D M6+ N psi

erpenu i.

finfinf

0.0011

> 121.$25

> 88.$2> 2

erpenu i.

;/m2 "

l / .f 2

f 2/in 2

f 2

u/ .f 2. %

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inin

in

in

f

psi psi

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Klter pressu( si L me(yari( a u dari molases

e(is L plate a(d rameaha( 'o(stru'si L stai(less steal

umlah L 1 uah

de(sitas Kltrat L 1! & ' m" 9 3ampira( $. $lira( 1 :de(sitas slud e L 711.%1 ' m" 9 ea(coplis %00":la u alir Kltrat L 81% ! ' hla u alir slud e L 1#&78 ' h

perhitu( a( pera(ca( a( Klter pressa. 3uas pe(yari( a(

3uas pe(yari( a( ya( e e'ti dihitu( de( a( persamaa(

3 x $ 91 -: ps = 9* 5 - x 3 x $: x p 92 91 2:: 9 ea(coplis %00"

dima(a L3 = te al ca'e pada rame 9m:$ = 3uas pe(yari( a( e e'ti 9m%:ps = de(sitas slud e 9' m":- = porositas parti'el = 0."%p = de(sitas Kltrat 9' m":2 = ra'si masa slud e pada umpa(* = )olume ra'si hasil pe(yari( a( 9m":

+ire(ca(a'a( operasi selama 1 am L)olume pe(yari( a( = la u alir Kltratde(sitas Kltrat

= 81% ! ' h1! & ' m"

= !0. 8! m" h

diestima'si'a( te al slud e pada rame adalah Lsehi( a L

2 = la u alir slud ela u alir eed

= 1#&77.7!# "8%087 ' h81% !."#%07118#1 ' h

= 0.%0"

ila dire(ca(a'a( setiap plate mempu(yai luas = % m%te al slud e = % cm = 0.0% mma'a

0.0% x $ 91 0 "%: x 711 = !0. 8!"0 & 5 90 "% x 0 0!$: 1! & x 990 #7!: 91 0 #7

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.#7%!1 $ = !0. 8!"0 & 5 %.! &%1& $$ = 7 m%

umlah plate 9(: = 7%

= & uah

sehi( a umlah plate = umlah rame = & uah

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lat screeninmasu' 9/ 'eluar 9/ am:

BM 1 2 2A

a

180 lu'osa 17#&1.0 & 17#&1.0"&% su'rosa %77 &.88& %77 &.88

18 air %1!"!.1&1 1 "81.#" %1!".!1

10# a u 1&"%&.%&" 1&"%&.%su total 81% !."#% #&817.#1 1#&77.8total 81% !."#% 81% !."#

alat scree(i( masu' 9/ 'eluar 9/ am:1 % %$ ' a

lu'osa 1.!& cm"su'rosa 1.#0# cm"air 1 cm"

: a u9?a%C>": %.!"" cm"

su total #.#7total

N9O erat x Ji: 1! &.&8# ' m"

+e(sitas @lud e 711.%1 ' m"

!:

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G !c-# O !'g/m3# ln G

0.%%0."&0.%#

0.181

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Klter pressu( si L me(yari( a u dari molases

e(is L plate a(d rameaha( 'o(stru'si L stai(less steal

umlah L 1 uah

de(sitas Kltrat L 87 ' m" 9 3ampira( $. $lira( 1 :de(sitas slud e L #.7# ' m" 9 ea(coplis %00":la u alir Kltrat L ' hla u alir slud e L "%7 ' h

perhitu( a( pera(ca( a( Klter pressa. 3uas pe(yari( a(

3uas pe(yari( a( ya( e e'ti dihitu( de( a( persamaa(

3 x $ 91 -: ps = 9* 5 - x 3 x $: x p 92 91 2:: 9 ea(coplis %00"

dima(a L3 = te al ca'e pada rame 9m:$ = 3uas pe(yari( a( e e'ti 9m%:ps = de(sitas slud e 9' m":- = porositas parti'el = 0."%p = de(sitas Kltrat 9' m":2 = ra'si masa slud e pada umpa(* = )olume ra'si hasil pe(yari( a( 9m":

+ire(ca(a'a( operasi selama 1 am L)olume pe(yari( a( = la u alir Kltrat

de(sitas Kltrat= ' h

87 ' m"= "7"."& m" h

diestima'si'a( te al slud e pada rame adalah Lsehi( a L

2 = la u alir slud ela u alir eed

= "%#. #&" ' h"#8&7". 7%1 ' h

= 0.0 &

ila dire(ca(a'a( setiap plate mempu(yai luas = % m%te al slud e = % cm = 0.0% mma'a

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0.0% x $ 91 0 "%: x = "7"."& 5 90 "% x 0 0!$: 87 x 990 #7!: 91 0 #7#."&7 7# $ = "7"."& 5 0.#!!1#001 $

$ = ## m%

umlah plate 9(: = ##%

= "" uah

sehi( a umlah plate = umlah rame = "" uah

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ko# onen M *k(&'#o ol *'#ol+suk *k(&5a

air 18 "&" %!saccar%m ces %"&.& &

e an%l 4$ %"%!1.&

ase al&e i& 44 "&". %!gliserin 92 71 .11#su % al "#8&7&total "#8&7&

air 1000 ' m": saccar%m ces 1008 ' m"

e an%l 78 ' m"ase al&e i& 788 ' m"gliserin 1%&0 ' m"

N9O erat x Ji: 8#. #11

+e(sitas @lud e #.7#"

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!:

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keluar *k(&5a#+7 8 B

"&" " "0 !"" 0.93337$702%"&.& & 0.000#"#&

0.0#"1010.000 ""&

%"%!1 0.001 !1#

"&". %!71 .11#

"%7 """8&7"#8&7& 1

J.P.Kizito 1, K.L. Barlow 1, E.S. Nelson 2, F.M.Donovan 3, N.D. Searby , D. !an"en"ries#$e . 1National %enter &or Mi

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#ro'ravity (esear#$ &or Fl)i"s an" %o*b)stion, an" 2N+S+ lenn (esear#$ %enter, %levelan", - / 3Lo#0$ee"

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Martin an" N+S+ +*es (esear#$ %enter, Mo&&ett Fiel", %+.

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+ata +e(si/ m" "0 oCsen a a n c &ensi as

2ater 18.00 30 0.3471 0.274 0.28571 $47.13 1244.8881439-ta(ol 4$.00 30 0.2$57 0.2$395 0.23$7 51$.25 987.9391322$cetaldeh 44.00 30 0.28207 0.2$004 0.277$ 4$1 1058.0137087

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$cetaldehyde #.#171 #.81-50% %.00- 0% %.!#- 0! 0.0015399$$8lycerol 18.%1!% &.%"-50" %.87- 0% 1.#7- 0! 0.002174$328

+ata +e(si/ m" 7 oCsen a a n c &ensi as

2ater 18.00 79 0.3471 0.274 0.28571 $47.13 1208.29$1745-ta(ol 4$.00 79 0.2$57 0.2$395 0.23$7 51$.25 95$.24$00541$cetaldeh 44.00 79 0.28207 0.2$004 0.277$ 4$1 1012.9192079Hidro e( 2.00 79 %.0 & 7 0." 0.%8!71 # 0%.8% # !!.#8"

-thyl $cet 88.00 79 0.30$54 0.2585$ 0.278 523.3 111#."&!$cetic $cid $0.00 79 0.35182 0.2$954 0.2$843 592.71 1242.3$39339

Data )iscosita *k( s+ cen ip%ise 7K%mp%sisi ase " Cp *isc%si as 'g/ T2ater

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c &ensi as 88 !0 #099 $47.13 1193.0397873 1%01.&!! 1%"0.081 1%%%.#1"99 51$.25 942.8849$955 7!.187#99 4$1 993.9$949884

99 723 1358.7913118

99*isc%si as T 88 !0 #02.2$29$48391 8. & %.17"%" 1.8503134958 1. %7112.1477$85995 8. & 1.70$72247512.29$2741$39 8. &2.48908$0$74 8. &

+ata +e(si/ m" "0 oCsen a a n

rea 30 0.23$89 0.25471 0.2887$sam @ul at 30 0.421$9 0.1935$ 0.2857


K%mp%sisi ase " +rea

3i4uid,8.59+D00 8.75+D02 %.#8- 0% ".#1- 0!

$sam @ul 18.70&! ".!0-50" "."1- 0% 1.70- 0!

air 100 air #0&ensi as

12.448881439 11 %.%7% 1%%%.#1"9.879391322

10.580137087

1389.18$$77$

"0 T

"0 0.00%%71 0.001 %7"0

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"0"0

+ata +e(si/ m" 0 oCsen a a n c

2ater 18.00 90 0.3471 0.274 0.28571 $47.13-ta(ol 4$.00 90 0.2$57 0.2$395 0.23$7 51$.25$cetaldeh 44.00 90 0.28207 0.2$004 0.277$ 4$1Hidro e( 2.00 90 %.0 & 7 0." 0.%8!71 # 0%.8%

-thyl $cet 88.00 90 0.30$54 0.2585$ 0.278 523.3$cetic $cid $0.00 90 0.35182 0.2$954 0.2$843 592.71


K%mp%sisi ase " Cp2ater

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c &ensi as

405.$5 902.54923

925 2145.31$4572

"0*isc%si as T1.$579$97151 "02.109240$309 "0

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&ensi as

1199.9295233

948.91098478

1002.5120714# !1.8"8

110#."#1233.31$228$

0*isc%si as 'g/ T1.#!- 007 0%.88- 00# 0%.# - 00# 0&.##- 00# 01.78- 00# 0

!.7- 007 0

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'ompo(e( BM

etha(ol air 18

liseri( %asetaldehid &&

lu'osa 180su'rosa "&%

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AMPIRAN 3D A AT TRAN PORTA I

-: - ,101

ungsi J en ransp%r asi a an a'u 'e screener

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.33 a m 13708.1001932 Kg/m2 2807.719298378 C f/f 2Su u %u pu 31

-6:-+6 C+S

K%mp%nen *is'%si as !c-# m%l >

glu'%sa 8338.73 221.20112 0.51$8723 0.217

su'r%sa 13138.30 5$5.58359$11 0.82288492 M6+ N 0.3419

air 10179.40 285.005$$53012 0.4820374471 0.2$49

a u $770.90 44$.33792888 0.448$821994 0.17$2

jumla 38427.33 1518.128310291 2.27047$9 M6+ N 1

Laju alir cairan 38427.329228 'g/jam 8471$.89001589 l m/jam 1411.948 l m/meni

&ensi as 1518.1283103 94.7737141549 l m/f 3

(is'%si as 2.27047$8$$5 c- 0.0001525$92 l m/f .s 2.542820$+,00$ l m/menie'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = 14.898 f 3/meni 111.438 gpm 7.031 L/s

*%lume fl% ra e !?f# 10B &ari laju alir un u' 'eamanan

?f = 0.248301$484 f 3/se'%n

. )iame er :p imum

) %p imum 3.7$5085$08 in 0.095$331744 m 9.5$33174444 cm

se ingga &iguna'an pipa se agai eri'u

suc i%n pipes

C-S 4 in sc 80

panjang 20 m $5.$1$ f

C) 5.7$1 in 0.4800833333 f 0.14$3311794 m

:) $.$25 in 0.5520833333 f 0.1$827704$2 m

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

13804580

983 f op q D =

W Q f =

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a 2$.053459985 in2 0.18092$8055 f 2 0.01$809059 m2

&isc arge pipes

C-S 4 in sc 80

panjang 30 m 98.424 f

C) 5.7$1 in 0.4800833333 f

:) $.$25 in 0.5520833333 fa 2$.053459985 in2

". -er i ungan pa&a Suc i%nsuc i%n (el%ci

* = 1.3723872909 f /s

4940.594247381 f / r

6e n%l& Aum er

Are 409274.09027 ur ulen

ma erial ang &iguna'an ai u c%mmercial s eel pipe

R 0.00004$ m 0.00015091$8 f

R/) 0.0003143554

0.0034 immer %us pg. 482 fig 14,1

s'in fric i%n l%ss Hfs

H fs 0.0544132103

su&&en c%n rac i%n l%ss Hfc

Hfc 0.0117093371

su&&en e>pan i%n fric i%n l%ss Hfe

asumsi Sa=S ma'a Ke = 0H fe 0

fi ing D (al(e fric i%n l%ss Hff

1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.0497$4$828 f l f/l

: L S

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: L H+ ) 2.4$880$3$87 f 0.752$848$85 m

). -er i ungan pa&a &isc arge

&isc arge (el%ci

* = 1.3723872909 f /s

4940.594247381 f /6e n%l& Aum er

Are = 409274


R 0.00004$ m 0.00015091$8 f

R/) 0.0003143554 = 0.0034


Hfs 0.08


Hfc 1.+,02


asumsi Sa=S ma'a Ke = 0Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 5.+,02

: L S

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+. : L H+ )

= 24.$73877453 f 7.520$892991 m 752.0$89299113 cm

. +A+6FC +K ACK

;s 32.2291780151 f C f/C

F. A-SHeng i ung e'anan uap mengguna'an persamaan an %ine

K: -:A+A " ) +glu'%sa $.$7 12$1.34 221.97 303su'r%sa $.17 103$.0$ 28.10 303air 8.107#! 17!0.%8# %"! 303a u 8.01 1$00.02 291.81 303

K: -:A+A -!a m#

glu'%sa 0.094110$7$2su'r%sa 0.027392939$air 0.1$88088725a u 0.03473$8421

% al 0.3250493304 = 0.3250493304 a m

e'anan uap pa&a &isc arge

K: -:A+A " ) +glu'%sa $.$7 12$1.34 221.97 304su'r%sa #.1#!01 10"#.0!# %8.0 7 304

air 8.107#! 17!0.%8# %"! 304a u 8.01 1$00.02 291.81 304

K: -:A+A -!a m#glu'%sa 0.0945415$9su'r%sa 0.027$522$75air 0.1$9830857$ = 0.32$7$153$3 a ma u 0.03473$8421 = 0.0017122059 A/m2

% al 0.32$7$153$3

ns 10$.$$2$7477Hs(A 13.332834347 m A-SHr 20.00 m

n 750 rpm A-SHa 3.84 m

H. + CSC+ASC -: -

e'anan uap pa&a su u 235 %"

- pa&a su u 30 %"

- pa&a su u 31 %" Q-

Me( hitu( (s=( 9I;0.!:9H;0.7!:dari data ta el diperoleh'oeKsie( 'a)itasi 9o:Ma'a Hs)(=o x HPada ta el diperoleh ?P@hr=1.!Hs)(

?P@Ha R ?P@Hr

7/24/2019 HE, pompa

142/285

Kapasi as 14.898098904 f 3/mn 111.4377797982 gpm 0.41714$7$93 m3/min

V 0.7

C. -% er p%mpa

)a a 1.9$9953$28$ pV m% %r 0.84

= 2.3451828912 p $-arame er Ailai/Ke erangan Sa uan

K%&e -,10$ ,

pe "en rifugal pump ,

Kapasi as 111.44 gpm

-% er $.00 p

%perasi 31 %"

0.0000001$$ a m

)iame er 0.10 m% al Hea& 24.$7 f

+fisiensi p%mpa 78 B

A-SH 20.00

a'a )a a -%r%s = )a a/ S m% %r

Q-

.1

&e/ .550..

"

lb ft &

Q f

f f

7/24/2019 HE, pompa

143/285

lu'osa 1.!&su'rosa 1.#0#air 1a u9?a%C> %.!""

4.238034+,008 l m/ r

0.2731318132 f 3/s

7/24/2019 HE, pompa

144/285

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

145/285

7/24/2019 HE, pompa

146/285

LA - - !mm g#

4.27+D00 71.52411392$

3.04+D00 20.818$3408$

4.85+D00 128.29474311

5.32+D00 2$.4

247.03749113

3358.409$82 Kg/m2

LA - - !mm g#

4.27+D00 71.8515924$

3.05+D00 21.015723331

4.8$+D00 129.071451815.32+D00 2$.4

248.3387$7$

1.$58793+,007 a m

7/24/2019 HE, pompa

147/285

0.00$95244$2 m3/s

p

281.37389817

7/24/2019 HE, pompa

148/285

cm"cm"cm"cm"

7/24/2019 HE, pompa

149/285

7/24/2019 HE, pompa

150/285

7/24/2019 HE, pompa

151/285

7/24/2019 HE, pompa

152/285

7/24/2019 HE, pompa

153/285


-: - ,102

ungsi J en ransp%r asi air pr%ses 'e ea er

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.17 a m 1208$.$9242115 Kg/m2 2475.$19457558 C f/f 2Su u %u pu 31

-6:-+6 C+S


ir 154099.21 1%&&.8881& 2.2$29$48391 85$1.0$$9993 1

jumla 154099.21 1244.888143879 2.2$29$48 85$1.0$$9993 1

Laju alir cairan 154099.20599 'g/jam 339727.1095197 l m/jam 5$$2.118 l m/meni

&ensi as 1244.8881439 77.71587704$1 l m/f 3

(is'%si as 2.2$29$48391 c- 0.0001520$44 l m/f .s 2.5344075+,00$ l m/meni

e'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = 72.857 f 3/meni 544.9$8 gpm 34.385 L/s


?f = 1.2142775083 f 3/se'%n

. )iame er :p imum

) %p imum 7.4950399$1 in 0.190374015 m 19.037401501 cm


suc i%n pipes

C-S 12 in sc 30


C) 12.09 in 1.0075 f 0.3070897342 m

:) 12.75 in 1.0$25 f 0.3238539381 m

a 114.7419585 in2 0.79$81915$3 f 2 0.0740287223 m2

&isc arge pipes

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

SUCTION

DISCHARGE

13804580983 f op q D =

W Q f =

7/24/2019 HE, pompa

154/285

C-S 12 in sc 30


C) 12.09 in 1.0075 f

:) 12.75 in 1.0$25 f

a 114.7419585 in2

". -er i ungan pa&a Suc i%n

suc i%n (el%ci* = 1.52390$019 f /s

548$.0$1$$84$9 f / r 6e n%l& Aum er

Are 784$$$.8425 ur ulen


R 0.00004$ m 0.00015091$8 f

R/) 0.00014979330.0028 immer %us pg. 482 fig 14,1


H fs 0.02$3280099


Hfc 0.014437$099


asumsi Sa=S ma'a Ke = 0

H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.0$13598421

: L S

7/24/2019 HE, pompa

155/285

: L H+ ) 2.$42$470782 f 0.805$850848 m


&isc arge (el%ci

* = 1.52390$019 f /s

548$.0$1$$84$9 f /

6e n%l& Aum er

Are = 784$$7ma erial ang &iguna'an ai u c%mmercial s eel pipe

R 0.00004$ m 0.00015091$8 f

R/) 0.0001497933 = 0.0028


Hfs 0.04


Hfc 1.+,02



Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff $.+,02

: L S

7/24/2019 HE, pompa

156/285

eng i ung e'anan uap mengguna'an persamaan an %ine

K: -:A+A " ) +ir 8.11 1750.29 235.00 303

K: -:A+A -!a m#

ir 0.1$88088725% al 0.1$88088725 = 0.1$88088725 a m


K: -:A+A " ) +ir 8.11 1750.29 235.00 304

K: -:A+A -!a m#ir 0.1$9830857$

% al 0.1$9830857$ = 0.1$9830857$ a m

ns 235.$9321384 = 0.0010219851 A/m2Hs(A 29.4$1$5173 m A-SHr 44.19 m

n 750 rpm A-SHa $.09 m

H. + CSC+ASC -: -

Kapasi as 72.85$$50497 f 3/mn 544.9$77457157 gpm 2.03998$2139 m3/min

V 0.9C. -% er p%mpa

)a a 5.$318404538 p

V m% %r 0.8$

= $.548$51$905 p 15

-arame er Ailai/Ke erangan Sa uan

K%&e -,102 ,pe "en rifugal pump ,

Kapasi as 544.97 gpm

-% er 15.00 p

%perasi 31 %"

0.0000001 a m

)iame er 7.50 in

% al Hea& 24.70 f



-sa pa&a su u 235 %"


Q-

a'a )a a -%r%s = )a a/ S m% %r

Q-


?P@Ha ?P@Hr

.1

&e/.550..

"

lb ft

&Q

f

f f

7/24/2019 HE, pompa

157/285

A-SH 44.19

7/24/2019 HE, pompa

158/285

4.224012+,008 l m/ r

1.3357052591 f 3/s

7/24/2019 HE, pompa

159/285

f l f/l

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

160/285

7/24/2019 HE, pompa

161/285

LA - - !mm g#

4.85+D00 128.29474311

128.29474311

1744.1332709 Kg/m2

LA - - !mm g#

4.8$+D00 129.07145181

129.07145181

0.000000099 a m

0.0339997702 m3/s

p

11!%. 1%#

7/24/2019 HE, pompa

162/285

7/24/2019 HE, pompa

163/285


-: - ,103

ungsi J en ransp%r asi 'eluaran pr%&uc 6,101 'e H+,201

@umla J 2 ua

Su u inpu $0 333 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.31 a m 1352$.110$3955 Kg/m2 2770.443849945 C f/f 2Su u %u pu $1

-6:-+6 C+S


ir 1$25$9.18 1075.89907$2$ 1.9914090584 9031.$208818 0.88

Flu'%sa 221$8.52 31$.87848 0.2577322319 481.9244344 0.12

jumla 184737.70 1392.77755$2$ 2.2491413 9513.54531$2 1

Laju alir cairan 184737.$9985 'g/jam 407272.7330983 l m/jam $787.879 l m/meni

&ensi as 1392.77755$3 8$.9483172822 l m/f 3

(is'%si as 2.2491412904 c- 0.0001511355 l m/f .s 2.5189258+,00$ l m/menie'anan uap 1 a m

empera ur $0 " 75 333 K

. Kapasi as p%mpa

f = 78.0$8 f 3/meni 583.948 gpm 3$.844 L/s

*%lume fl% ra e !?f# 10B &ari laju alir un u' 'eamanan?f = 1.3011328831 f 3/se'%n

. )iame er :p imum

) %p imum 7.8453$77232 in 0.1992723402 m 19.92723401$9 cm


suc i%n pipes

C-S 10 in sc $0


C) 9.75 in 0.8125 f 0.247$530115 m

:) 10.75 in 0.8958333333 f 0.2730533203 m

a 74.$240$25 in2 0.518222$5$3 f 2 0.048145$311 m2

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

SUCTION

DISCHARGE

13804580983 f op q D =

W Q f =

7/24/2019 HE, pompa

164/285

&isc arge pipes

C-S 10 in sc $0


C) 9.75 in 0.8125 f

:) 10.75 in 0.8958333333 f

a 74.$240$25 in2

". -er i ungan pa&a Suc i%nsuc i%n (el%ci

* = 2.5107$03217 f /s9038.7371582$9 f / r

6e n%l& Aum er

Are 1173$08.3341 ur ulen


R 0.00004$ m 0.00015091$8 fR/) 0.0001857438

0.00$ immer %us pg. 482 fig 14,1


H fs 0.1899009253


Hfc 0.03919128



H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.1$$5$29401

: L S

7/24/2019 HE, pompa

165/285

7/24/2019 HE, pompa

166/285

7/24/2019 HE, pompa

167/285

%perasi $1 %"

0.0000001 a m

)iame er 0.20 m

% al Hea& 24.51 f


A-SH 4$.01

Q-

7/24/2019 HE, pompa

168/285

0.000000042 l m/ r

1.43124$1715 f 3/s

7/24/2019 HE, pompa

169/285

f l f/l

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

170/285

7/24/2019 HE, pompa

171/285

LA - - !mm g#

5.03+D00 152.34$9$18$

4.40+D00 81.444122155

233.79108401

3178.3282$32 Kg/m2

LA - - !mm g#

5.03+D00 153.174253$8

4.40+D00 81.777748451

234.95200214

0.000000148 a m

0.03$4317207 m3/s

p

# #.&"#

7/24/2019 HE, pompa

172/285

7/24/2019 HE, pompa

173/285


-: - ,104

ungsi J en ransp%r asi a an a'u Saccar%m cess 'e &alam 6,103

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.07 a m 11042.0$43782 Kg/m2 22$1.$5$743944 C f/f 2Su u %u pu 31

-6:-+6 C+S


saccar%m cec 110.84 4$.92307$9231 0.$304715$42 2.409$22172 0.384$15384$

7/24/2019 HE, pompa

174/285

&isc arge pipes

C-S 1 1/4 in sc 40


C) 1.38 in 0.115 f

:) 1.$$ in 0.1383333333 f

a 1.494954 in2". -er i ungan pa&a Suc i%n

suc i%n (el%ci* = 1.7$81312252 f /s

$3$5.272410$73 f / r

6e n%l& Aum er

Are 1$25$.$432178$ ur ulen

ma erial ang &iguna'an ai u c%mmercial s eel pipeR 0.00004$ m 0.00015091$8 f

R/) 0.00131232

0.007 immer %us pg. 482 fig 14,1


H fs 0.77$2790$5


Hfc 0.01943$04$2



H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.082$0319$3

: L S

7/24/2019 HE, pompa

175/285

: L H+ ) 10.5458755947 f 3.215205974 m


&isc arge (el%ci

* = 1.7$81312252 f /s$3$5.272410$73 f /

6e n%l& Aum er

Are = 1$257


R 0.00004$ m 0.00015091$8 f

R/) 0.00131232 = 0.007


Hfs 1.1$


Hfc 2.+,02



Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 8.+,02

: L S

7/24/2019 HE, pompa

176/285

7/24/2019 HE, pompa

177/285

= 1.9$80$59842 p 5


K%&e -,104 ,


Kapasi as 8.24 gpm

-% er 5.00 p

%perasi 31 %"0.0000001 a m

)iame er 0.02 m% al Hea& 23.94 f


A-SH 5.5$

a'a )a a -%r%s = )a a/ S m% %r

Q-

7/24/2019 HE, pompa

178/285

3.3404$2+,008 l m/ r

0.020191$829 f 3/s

7/24/2019 HE, pompa

179/285

f l f/l

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

180/285

7/24/2019 HE, pompa

181/285

LA - - !mm g#

,2.0023171$21 0.13502205253.9393414792 51.384752228

,3.2723522738 0.037917130$

51.557$91411

$99.077$57$5 Kg/m2

LA - - !mm g#

,1.9$41885$8 0.1402$9$597

3.95221$881$ 52.050$2911

,3.220$1$249$ 0.039930443$

52.230829213

0.000000103 a m

0.0005139701 m3/s

7/24/2019 HE, pompa

182/285

p

17.&%8&%

7/24/2019 HE, pompa

183/285


-: - ,105

ungsi J en ransp%r asi % %m pr%&uc %u pu 6,103 'e 6,104

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.17 a m 1208$.$9242115 Kg/m2 2475.$19457558 C f/f 2Su u %u pu 31

-6:-+6 C+S


saccar%m cec 110.84 . & 1.081 $.1579233285 1

jumla 110.84 9.94 1.0810000 $.1579233285 1

Laju alir cairan 110.842$1991 'g/jam 244.3$3$39859 l m/jam 4.073 l m/meni

&ensi as 9.94 0.$2053432 l m/f 3

(is'%si as 1.081 c- 0.000072$4 l m/f .s 1.210$$$0+,00$ l m/meni

e'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = $.5$3 f 3/meni 49.093 gpm 3.098 L/s


?f = 0.109387$4$5 f 3/se'%n

. )iame er :p imum

) %p imum 1.35412852$5 in 0.0343948$4$ m 3.43948$4573 cm


suc i%n pipes

C-S 3/4 in sc 80


C) 0.742 in 0.125 f 0.0381004$33 m

:) 1.05 in 0.1583333333 f 0.0482$058$8 m

a 1.7$$25 in2 0.0122$5$25 f 2 0.001139541$ m2

&isc arge pipes

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

SUCTION

DISCHARGE

13804580983 f op q D =

W Q f =

7/24/2019 HE, pompa

184/285

C-S 3/4 in sc 80


C) 0.742 in 0.125 f

:) 0.742 in 0.1583333333 f

a 1.7$$25 in2

". -er i ungan pa&a Suc i%n

suc i%n (el%ci* = 8.91822850$1 f /s

32105.$22$2194 f / r 6e n%l& Aum er

Are 9523.1107819 ur ulen


R 0.00004$ m 0.00015091$8 f

R/) 0.00120733440.00$ immer %us pg. 482 fig 14,1


H fs 15.5735318$1


Hfc 0.4944$5$493



H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 2.1014790094

: L S

7/24/2019 HE, pompa

185/285

: L H+ ) 14$.70040925 f 44.7257345288 m


&isc arge (el%ci

* = 8.91822850$1 f /s

32105.$22$2194 f /

6e n%l& Aum er

Are = 9523ma erial ang &iguna'an ai u c%mmercial s eel pipe

R 0.00004$ m 0.00015091$8 f

R/) 0.0012073344 = 0.00$


Hfs 23.3$


Hfc 5.+,01



Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 2.+D00

: L S

7/24/2019 HE, pompa

186/285


K: -:A+A " ) +saccar%m cec 8.11 1750.29 235.00 303

K: -:A+A -!a m#

saccar%m cec 0.1$88088725% al 0.1$88088725 = 0.1$88088725 a m


K: -:A+A " ) +saccar%m cec 8.11 1750.29 235.00 304

K: -:A+A -!a m#saccar%m cec 0.1$9830857$

% al 0.1$9830857$ = 0.1$9830857$ a m

ns 155.09411371 = 0.0010219851 A/m2Hs(A 19.38$7$4213 m A-SHr 29.08 m

n 750 rpm A-SHa 819.24 m

H. + CSC+ASC -: -

Kapasi as $.5$32587912 f 3/mn 49.0931757582 gpm 0.18377124$2 m3/min

V 0.019C. -% er p%mpa

)a a 4.105043$5$4 p

V m% %r 0.82

= 5.00$1508005 p 4


K%&e -,105 ,pe "en rifugal pump ,

Kapasi as 49.09 gpm

-% er 4.00 p

%perasi 31 %"

0.0000001 a m

)iame er 0.03 m

% al Hea& 8.$7 f





Q-

a'a )a a -%r%s = )a a/ S m% %r

Q-


?P@Ha ?P@Hr

.1

&e/.550..

"

lb ft

&Q

f

f f

7/24/2019 HE, pompa

187/285

A-SH 29.08

7/24/2019 HE, pompa

188/285

2.017777+,008 l m/ r

0.12032$4112 f 3/s

7/24/2019 HE, pompa

189/285

f l f/l

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

190/285

7/24/2019 HE, pompa

191/285

LA - - !mm g#

4.85+D00 128.29474311

128.29474311

1744.1332709 Kg/m2

LA - - !mm g#

4.8$+D00 129.07145181

129.07145181

0.000000099 a m

0.0030$28541 m3/s

p

%#.#%8&!

7/24/2019 HE, pompa

192/285

7/24/2019 HE, pompa

193/285


-: - ,10$

ungsi J en ransp%r asi %u pu 6,104 'e ',102

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.$8 a m 17398.5108109$ Kg/m2 35$3.59$25903$ C f/f 2Su u %u pu 31

-6:-+6 C+S


M6+ N 10990.$$ $2.3408579$95 1.$3922$0$$9 M6+ N 0.0$31019219

1$25$9.18 11$1.949590531 1.819$95912 0.93337$7024

339.92 2.7111448221 2.174$3281$$ 0.001951$058

saccar%m ces 110.84 0.$414843518 1.081 0.000$3$3932

M6+ N 1$2.57 0.98752534$4 1.5399$$8273 M6+ N 0.00093337$7

jumla 174173.17 1228.$30$03021 8.254521$ M6+ N 1

Laju alir cairan 174173.1$$59 'g/jam 383982.1$30$82 l m/jam $399.703 l m/meni

&ensi as 1228.$30$03 7$.7009512854 l m/f 3

(is'%si as 8.254521$228 c- 0.000554$791 l m/f .s 9.244$515+,00$ l m/menie'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = 83.437 f 3/meni $24.109 gpm 39.378 L/s


?f = 1.390$178499 f 3/se'%n

. )iame er :p imum

) %p imum 7.9530225$04 in 0.20200$773 m 20.200$773035 cm


suc i%n pipes

C-S 12 in sc 30


C) 12.09 in 1.0075 f 0.3070897342 m

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

13804580983 f op q D =

W Q f =

7/24/2019 HE, pompa

194/285

:) 12.75 in 1.0$25 f 0.3238539381 m

a 114.7419585 in2 0.79$81915$3 f 2 0.0740287223 m2

&isc arge pipes

C-S 8 in sc 80

panjang 50 m 1$4.04 f

C) 12.09 in 1.0075 f:) 12.75 in 1.0$25 f


suc i%n (el%ci

* = 1.7452113$82 f /s

$282.7$0925$75 f / r

6e n%l& Aum er

Are 243137.554$4 ur ulen


R 0.00004$ m 0.00015091$8 f

R/) 0.0001497933

0.0032 immer %us pg. 482 fig 14,1


H fs 0.0394$29$18


Hfc 0.018935422$

su&&en e>pan i%n fric i%n l%ss Hfeasumsi Sa=S ma'a Ke = 0

H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.0804755459 f l f/l

: L S

7/24/2019 HE, pompa

195/285

: L H+ )

: L H+ ) 2.7039309099 f 0.8243$91798 m


&isc arge (el%ci

* = 1.7452113$82 f /s$282.7$0925$75 f /

6e n%l& Aum er

Are = 243138


R 0.00004$ m 0.00015091$8 f

R/) 0.0001497933 = 0.0032


Hfs 0.10


Hfc 2.+,02



Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 8.+,02

: L S

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% al ea& 27 f

+. : L H+ )

= 24.$81$01$1$ f 7.523043$527 m 752.3043$52$$4 cm

. +A+6FC +K ACK

;s 43.88892$0299 f C f/C

F. A-SH


K: -:A+A " ) +M6+ N 8.11 1592.8$ 22$.18 303

8.11 1750.29 235.00 303#.1#!01 10"#.0!# %8.0 7 303

M6+ N 8.01 1$00.02 291.81 303

K: -:A+A -!a m#M6+ N 0.21$2853822

0.1$88088725

0.027392939$

0.2$7732712$

% al 0.$8021990$9 = 0.$8021990$9 a m


K: -:A+A " ) +M6+ N 8.11 1592.8$ 22$.18 304

8.11 1750.29 235.00 304#.1#!01 10"#.0!# %8.0 7 304

8.01 1$00.02 291.81 304

K: -:A+A -!a m#M6+ N 0.21751$8014

0.1$9830857$

0.027$522$75 = 0.$839441358 a m

0.2$89442092 = 0.0037242289 A/m2% al 0.$839441358

ns 252.3$238185

Hs(A 31.545297731 m A-SHr 47.32 m

n 750 rpm A-SHa 1.8$ m


- pa&a su u 30 %"

- pa&a su u 31 %" Q-

Me( hitu( (s=( 9I;0.!:9H;0.7!:dari data ta el diperoleh'oeKsie( 'a)itasi 9o:Ma'a Hs)(=o x HPada ta el diperoleh ?P@hr=1.!

?P@Ha R ?P@Hr

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H. + CSC+ASC -: -

Kapasi as 83.437070995 f 3/mn $24.1092910447 gpm 2.33$2379879 m3/min

V 0.9

C. -% er p%mpa

)a a 9.457107043$ p

V m% %r 0.87= 10.870237981 p 24


K%&e -,10$ ,


Kapasi as $24.11 gpm

-% er 24.00 p

%perasi 31 %"

0.0000003$1 a m)iame er 0.20 m

% al Hea& 24.$8 f


A-SH 47.32

a'a )a a -%r%s = )a a/ S m% %r

Q-

s)(

.

1

&e/ .550..

"

lb ft &

Q f

f f

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1.540775+,007 l m/ r

1.529$79$349 f 3/s

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199/285

f l f/l

f l f/l

f l f/l

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200/285

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201/285

LA - - !mm g#

5.10+D00 1$4.37$89043

4.85+D00 128.29474311

3.04+D00 20.818$3408$

5.32+D00 203.47$8$157

51$.9$712921

7028.032077$ Kg/m2

LA - - !mm g#

5.11+D00 1$5.3127$908

4.8$+D00 129.071451813.05+D00 21.015723331

5.32+D00 204.39759898

519.7975432

3.$08050+,007 a m

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202/285

0.0389372998 m3/s

p

1"%0."&1"

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203/285


-: - ,107

ungsi J en ransp%r asi %u pu ',102 'e ,210

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.$8 a m 17398.5108109$ Kg/m2 35$3.59$25903$ C f/f 2Su u %u pu 31

-6:-+6 C+S


M6+ N 10990.$$ $2.3408579$95 1.$3922$0$$9 M6+ N 0.0$31019219

1$25$9.18 11$1.949590531 1.819$95912 0.93337$7024

339.92 2.7111448221 2.174$3281$$ 0.001951$058

saccar%m ces 110.84 0.$414843518 1.081 0.000$3$3932

M6+ N 1$2.57 0.98752534$4 1.5399$$8273 M6+ N 0.00093337$7

jumla 174173.17 1228.$30$03021 8.254521$ M6+ N 1

Laju alir cairan 174173.1$$59 'g/jam 383982.1$30$82 l m/jam $399.703 l m/meni

&ensi as 1228.$30$03 7$.7009512854 l m/f 3

(is'%si as 8.254521$228 c- 0.000554$791 l m/f .s 9.244$515+,00$ l m/menie'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = 83.437 f 3/meni $24.109 gpm 39.378 L/s


?f = 1.390$178499 f 3/se'%n

. )iame er :p imum

) %p imum 7.9530225$04 in 0.20200$773 m 20.200$773035 cm


suc i%n pipes

C-S 12 in sc 30


C) 12.09 in 1.0075 f 0.3070897342 m

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

13804580983 f op q D =

W Q f =

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:) 12.75 in 1.0$25 f 0.3238539381 m

a 114.7419585 in2 0.79$81915$3 f 2 0.0740287223 m2

&isc arge pipes

C-S 8 in sc 80


C) 12.09 in 1.0075 f:) 12.75 in 1.0$25 f


suc i%n (el%ci

* = 1.7452113$82 f /s

$282.7$0925$75 f / r

6e n%l& Aum er

Are 243137.554$4 ur ulen


R 0.00004$ m 0.00015091$8 f

R/) 0.0001497933

0.003 immer %us pg. 482 fig 14,1


H fs 0.03$99$52$7


Hfc 0.018935422$

su&&en e>pan i%n fric i%n l%ss Hfeasumsi Sa=S ma'a Ke = 0

H fe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1 7

H ff 0.0804755459 f l f/l

: L S

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: L H+ )

: L H+ ) 2.7014$44748 f 0.823$172179 m


&isc arge (el%ci

* = 1.7452113$82 f /s$282.7$0925$75 f /

6e n%l& Aum er

Are = 243138


R 0.00004$ m 0.00015091$8 f

R/) 0.0001497933 = 0.003


Hfs 0.07


Hfc 2.+,02



Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 8.+,02

: L S

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206/285

% al ea& 27 f

+. : L H+ )

= 24.$840$8051 f 7.5237954312 m 752.3795431227 cm

. +A+6FC +K ACK

;s 43.8$42$1$788 f C f/C

F. A-SH


K: -:A+A " ) +M6+ N 8.11 1592.8$ 22$.18 303

8.11 1750.29 235.00 303#.1#!01 10"#.0!# %8.0 7 303

M6+ N 8.01 1$00.02 291.81 303

K: -:A+A -!a m#M6+ N 0.21$2853822

0.1$88088725

0.027392939$

0.2$7732712$

% al 0.$8021990$9 = 0.$8021990$9 a m


K: -:A+A " ) +M6+ N 8.11 1592.8$ 22$.18 304

8.11 1750.29 235.00 304#.1#!01 10"#.0!# %8.0 7 304

8.01 1$00.02 291.81 304

K: -:A+A -!a m#M6+ N 0.21751$8014

0.1$9830857$

0.027$522$75 = 0.$839441358 a m

0.2$89442092 = 0.0037242289 A/m2% al 0.$839441358

ns 252.3434$955

Hs(A 31.542933$94 m A-SHr 47.31 m

n 750 rpm A-SHa 1.87 m


- pa&a su u 30 %"

- pa&a su u 31 %" Q-

Me( hitu( (s=( 9I;0.!:9H;0.7!:dari data ta el diperoleh'oeKsie( 'a)itasi 9o:Ma'a Hs)(=o x HPada ta el diperoleh ?P@hr=1.!

?P@Ha R ?P@Hr

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H. + CSC+ASC -: -

Kapasi as 83.437070995 f 3/mn $24.1092910447 gpm 2.33$2379879 m3/min

V 0.9

C. -% er p%mpa

)a a 9.4517924135 p

V m% %r 0.87= 10.8$4129211 p 24


K%&e -,104 ,


Kapasi as $24.11 gpm

-% er 24.00 p

%perasi 31 %"

0.0000003$1 a m)iame er 0.20 m

% al Hea& 24.$8 f


A-SH 47.31

a'a )a a -%r%s = )a a/ S m% %r

Q-

s)(

.

1

&e/ .550..

"

lb ft &

Q f

f f

7/24/2019 HE, pompa

208/285

1.540775+,007 l m/ r

1.529$79$349 f 3/s

7/24/2019 HE, pompa

209/285

f l f/l

f l f/l

f l f/l

7/24/2019 HE, pompa

210/285

7/24/2019 HE, pompa

211/285

LA - - !mm g#

5.10+D00 1$4.37$89043

4.85+D00 128.29474311

3.04+D00 20.818$3408$

5.32+D00 203.47$8$157

51$.9$712921

7028.032077$ Kg/m2

LA - - !mm g#

5.11+D00 1$5.3127$908

4.8$+D00 129.071451813.05+D00 21.015723331

5.32+D00 204.39759898

519.7975432

3.$08050+,007 a m

7/24/2019 HE, pompa

212/285

0.0389372998 m3/s

p

1"%0."&1"

7/24/2019 HE, pompa

213/285


-: - ,108

ungsi J en ransp%r asi %u pu ,210 'e )s,101

@umla J 2 ua

Su u inpu 30 303 K

- inpu 1 a m 10332 Kg/m2 211$.22 C f/f 2

-%u pu 1.$8 a m 17398.5108109$ Kg/m2 35$3.59$259 C f/f 2Su u %u pu 31

-6:-+6 C+S


M6+ N 10990.$$ 987.9391322014 1.$3922$0$$9 M6+ N 0.0$9$4$92$$

14$312.2$ 1244.888143879 1.819$95912 0.9271$88571

339.92 1389.18$$77$41 2.174$3281$$ 0.0021540287

1$2.57 1058.013708$55 1.5399$$8273 0.001030187$

jumla 157805.41 4$80.027$$2377 7.173521$ M6+ N 1

Laju alir cairan 157805.40$38 'g/jam 347897.7989157 l m/jam 5798.297 l m/meni

&ensi as 4$80.027$$24 292.1$47$$90$9 l m/f 3

(is'%si as 7.173521$228 c- 0.0004820391 l m/f .s 0.000008034 l m/menie'anan uap 1 a m

empera ur 30 " 37.5 303 K

. Kapasi as p%mpa

f = 19.84$ f 3/meni 148.448 gpm 9.3$$ L/s


?f = 0.3307$$3$34 f 3/se'%n

. )iame er :p imum

) %p imum 4.95884837 in 0.125954748$ m 12.5954748$ cm


suc i%n pipes

C-S 8 in sc 80


C) 7.$25 in 0.$3541$$$$7 f 0.193$773551 m

:) 8.$25 in 0.71875 f 0.219077$$4 m

%"

%"

SS!Kg/jam#

)ensi as!'g/m3#

'g/m 3

13804580

983 f op q D =

W Q f =

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: L H+ ) 1.837831$$35 f 0.5$03145315 m


&isc arge (el%ci

* = 1.043$00979 f /s

375$.9$3524235 f /6e n%l& Aum er

Are = 401919


R 0.00004$ m 0.00015091$8 f

R/) 0.0002375084 = 0.002$


Hfs 0.05


Hfc 7.+,03


asumsi Sa=S ma'a Ke = 0Hfe 0


1 ga e (al(e D 2 el % 90= 0 2 D 2T!0.75#= 1.7

Hff 3.+,02

: L S

HE, pompa

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