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PAP 2

“PROSES PEMISAHAKOMPONEN KIMIA PA

INDUSTRI TERPENTINNAMA : MOHAMAD ROHMAN (5213413021)

MUHAMMAD FAHMI SIHAB (5213413077)

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KOMPONEN KIMIA (FEED)

 ALPHA-PINENE C10H16-D2 64,6 % TD = 16,1 C CAMPHENE C10H16-E1 2,!" % TD = 160, C

 #ETA-PINENE C10H16-D$ 2,16 % TD = 166 C

 D-LIMONENE C10H16-D1 $,4! % TD = 1"6, C

 AMMA-TERPINENE C10H16-E 2,1 % TD = 1&$ C

 TERPINOLENE C10H16-D4 1,6$ % TD = 1& C

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'ARIA#E

1. Proses disi!"si ( F!o# S$ee ) 2. Pers"%""& 'er%odi&"%i"

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Proses disi!"si ( F!o# S$ee )

1

2

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+o%,osisi Feed

  NR': F!o#s$ee (1) d"& F!o#s$ee (2)

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NR': He"er

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desi!"si

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NR': Disi!"si D1  F!o# S$ee 1   F!o# S$ee 2

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NR': Sre"% Res! D1

  F!o# S$ee 1   F!o# S$ee 2

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NR': Disi!"si D2

  F!o# S$ee 1   F!o# S$ee 2

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NR': Sre"% Res! or D2

  F!o# S$ee 1   F!o# S$ee 2

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NR': Disi!"si D3  F!o# S$ee 1   F!o# S$ee 2

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NR': Sre"% Res! D3

  F!o# S$ee 1   F!o# S$e

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NR': Oer"!! Res!NO K*+. F/ S* 1 F/ S

1 A!,$"Pi&e&e   0,997443 0,951928

2 Be" Pi&e&e   0,990777 0,999516

3 6"%,e&e   0,605777 0,884434

4 'o"! 'r"   337,527 647,729

5 8. Re. 'o"!   29154,49 cal/sec 37957,69 ca

- 8.+o&. 'o"! 28069 cal/sec 36872,35 ca

De&/"& 2 9e&is %eode ,e%is"$"& ( F!o#s$ee "&/ Bered" ) ed" &" %di%"&" "!,$" ,i&e&e %i& ( 075) ed" ;o#S$ee %e%e&$i d"& Be" Pi&

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d"& 8&er/i "&/ di /&""& 9/" ei$ sedii di "&di&/ FS

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 P8RSAMAAN '8RMODINAMINR' *AN AAR

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R8SU' SUMMAR= FO<SH8(1)

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R8SU' SUMMAR= FO<SH8(1)

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8> P"d" D3

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R8SU' SUMMAR= FO<SH8(2)

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R8SU' SUMMAR= FO<SH8(2)

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8> P"d" D3

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Res!

NO K*+. F/ S* 1 F/ S*NR' *"& ""r NR' *"&

1 A!,$"Pi&e&e 07443   0,997443 0512   0,95

2 Be" Pi&e&e 00777   0,990778 051-   0,99

3 6"%,e&e 0-05777   0,605772 04434   0,88

 'er9"di Pered""& de&/"& Per/"&i"& Mode! 'er%odi&"%i" "i *"& ""r (*(8oS)

D"!"% ,e&e&"& 9%!"$ r" d"& 8&er/ &"%& d"!"% i&/" e%r&i"& *"& ""r (*iri"!) d"& NR' (8oS)

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TERIMA KASI