Analisis de Performance de Rehervidor Kettle Edr

 

ANÁLISIS DE PERFORMANCE DE REHE RE HERRVI VIDO DORR KETT KETTLE LE CURSO: SIMULACIÓN Y DIMENSIONAMIENTO DE INTERCAMBIADORES DE CALOR CAPÍTULO 4

Ingeniero de Procesos - Luis Torres Melc hor

05/11/2016

1

 

ASPEN ASP EN EX EXCHANGE CHANGERR DESIGN DESIGN & RATIN RATING G FFAMIL AMILY Y

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

2

 

ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

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ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

KE KEY Y DESI DESIGN GN PAR ARAM AMET ETER ERSS ON KE KETT TTLE LE RE REBO BOIL ILER ERSS

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  RECIRCULATION RATIO:

THE THE RATIO RATIO OF THE THE RECIR RECIRCU CULA LATIN TING G FLOW FLOW ARO AROUN UND D THE THE BU BUNDL NDLEE AN AND D THE THE INL INLET ET

FLOW •

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  QUALITY AT THE TOP OF THE BUNDLE:

BECA BEC AUSE OF RE RECI CIRC RCULA ULATI TION, ON, TH THEE QUA QUALIT LITY Y AT THE BU BUNDL NDLEE EXIT EXIT WI WILL LL BE DIFF DIFFER ERENT ENT FRO FROM M TH THEE QU QUALI ALITY TY OF THE THE STRE STREAM AM LEA LEAVI VING NG THE THE EXCH EXCHANG ANGER ER

  ENTERTAINMENT FRACTION:

Ingeniero de Procesos - Luis Torres Melchor

THE THE MA MASS SS OF LIQ LIQUID UID EN ENTR TRAIN AINED ED IN TTHE HE VAPOR APOR PE PERR U UNIT NIT MA MASS SS OF VAPOR APOR

05/11/2016

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ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

OBJECTIVE •

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TO SIMU SIMULA LATE TE A K KETT ETTLE LE REBO REBOILER ILER TO ANA ANALLYZE THE PERF PERFORM ORMANC ANCEE OF THE EXCHA EXCHANGE NGERR EVALU EVALUA ATE THE REC RECIRCU IRCULA LATIO TION N RATIO RATIO AND ENT ENTRAIN RAINMENT MENT FRA FRACTIO CTION N

CONT CO NTAI AINS NS TH THEE FO FOLL LLO OWI WING NG TA TASK SKSS •

SIMULATE SIMULA TE A K-SHELL

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ENTERR LIQU ENTE LIQUID/V ID/VAPO APORR ONL ONLY Y OUT OUTLET LET NOZZ NOZZLES LES DET DETAILS AILS

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

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ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

UNITS UNI TS OF ME MEASU ASURE: RE: SI

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CALCULATION CALCULA TION MODE: SIMULA SIMULATION TION

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HOTT FLUID HO FLUID:: TU TUBE BE SID SIDEE (ST (STEAM EAM))

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COLD COL D FLU FLUID: ID: SHE SHELL LL SI SIDE DE (HE (HEXAN XANE) E)

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HOT SIDE APPLICA APPLICATION: TION: CO CONDENSA NDENSATION TION

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COLD SIDE APPLIC APPLICA ATION: VAPORI APORIZA ZATION TION

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VAPORI APORIZER ZER TYPE: KETTLE KETTLE

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

6

 

ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

PHYSIC PHY SICAL AL PRO PROPER PERTY TY DA DATA TA •

HOT STREAM •

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SELECT “COMTHERM SELECT “COMTHERMO” O” PHYSICAL PHYSICAL PROPERTY PROPERTY PKG SELECTT WAT SELEC ATER ER

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SELECT SEL ECT PENG PENG ROBINS ROBINSON ON AS THE PROPER PROPERTY TY METHO METHOD D

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SPECIFY SPEC IFY A TEMPERA TEMPERATURA TURA RANGE RANGE FROM 160°C 160°C TO 1 100°C 00°C

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

7

 

ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

PHYSIC PHY SICAL AL PRO PROPER PERTY TY DA DATA TA •

COLD COL D STRE STREAM AM •

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SELECT “COMTHERM SELECT “COMTHERMO” O” PHYSICAL PHYSICAL PROPERTY PROPERTY PKG SELECTT HEXANE SELEC HEXANE

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SELECT SEL ECT PENG PENG ROBINS ROBINSON ON AS THE PROPER PROPERTY TY METHO METHOD D

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SPECIFY SPEC IFY A TEMPERA TEMPERATURA TURA RANGE RANGE FROM 100°C 100°C TO 1 160°C 60°C

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

8

 

ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

GEOMETR GEOME TRY Y SUMMA SUMMARY RY •

SELEC SEL ECTT TH THEE TE TEMA MA TTYP YPEE AS ““AK AKU” U”

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

9

 

ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

EXCHANGE EXC HANGERR GEOME GEOMETR TRY Y •

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KETTLE KET TLE ID: 175 1750MM 0MM N° SUPP SUPPORTS ORTS:: 6 TUBESIDEE NOZZLES: 320 TUBESID 320MM, MM, 220MM 220MM,, 400MM SHELL SIDE NOZZLES NOZZLES:: 345MM, 152MM

RUN CONTROL •

CL CLIC ICK K RU RUN N

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SAVE SAVE CASE: “3_KETT “3_KETTLE_REBOI LE_REBOILER” LER”

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

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ASPEN ASP EN SHELL SHELL & TUBE TUBE EX EXCHA CHANGE NGERR CASEE 2: ANAL CAS ANALYZE YZE THE PER PERFOR FORMAN MANCE CE OF A KETT KETTLE LE REB REBOIL OILER ER •

RESULT RESU LT SUM SUMMAR MARY Y •

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REVIEW REVI EW WARNI ARNING NG AND ME MESSA SSAGES GES RECORD RECO RD TH THEE FOLL FOLLOW OWING ING RESU RESULT LTSS

BAFFLE BAF FLE SUPP SUPPORT ORT •

ADD ADD “U” BEND BEND SUPPOR SUPPORTT

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CHEC CH ECK K IF YOU HA HAVE VE VI VIBR BRA ATION TION WAR ARNI NING NG YE YETT

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SET ADEQUA ADEQUATE TE SHELL AND TTUBE UBE TEMPERA TEMPERATURA TURA RATING RATING TTO O ELIM ELIMINA INATE TE WARNING MESSA MESSAGES GES 1636 AND 1 1637 637

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REVIE REV IEW W TH THEE OPE OPERA RATI TION ON WARN ARNING ING 13 1387 87,, WH WHA AT CH CHAN ANGE GESS WO WOULD ULD YOU DO DO??

Ingeniero de Procesos - Luis Torres Melchor

05/11/2016

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