20._Mar-3 - Sfeagrmfim :@ ffoMQz/i HA7. 0:. , 7%.6’ ’Z...

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Unformatted text preview: Sfeagrmfim :@ ffoMQz/i HA7. 0:. , 7%.6’ ’Z Iva @ MW uhmm _~ 010,01 4::— @ out-punk SW .03“: :00 <==a CO / ( [Mir-I‘D) ”" WW = \0‘1»). lb‘Dx 0079:073 was *&:fi“wk 7m ( < (ea/uh“ an” t w i n § nu 40%}1 ‘gcl‘he n Ibo 0,:44— 26loz ma: Iooxoflac? amflwk 09-‘5’ “’in brew/x “W’W oyzm M an: M X viz car/W'W 974%»- wfiw" are (45 fie. cw § 754,, {$4 W} ’71‘ awayév/I’BW (3-6., low/MIT MDMJM (Le M Ari/‘fi‘any, ® NDO'N‘L Spde 3 mbMS'WYDJ < ,nco, “mo, nu; ) .3 WWW 4AM»; pram (or—1.0 J _ O nan—MW Malawian/MW Q C 7.80 (ML: (7:— -— oqaomflc 9-:<?> '- n6: 2 Mia “cpl: 61mg =- L“) H N'Drrwtc balm/ML: Wzbifgfi I 4-H 4-H mnflé —’—‘ : 3:18th ——“> .n D( 4‘ K730 (CH4 4‘ 7 [I (W 4-1 ; nm = “+0 mole (TI?) 0 Wow-L Imflmve MM 2994-wa 92% (.330) =‘— (h + ILAML + H1111.) + an“ M km» % n0;:§.7rflwa£€_ wnmA'mHon :— @ Malcwlpw SW QM. M £0 Var-:8“ 7"“ I 3 Wm; ( nae I I'M—ha, 0.9;) 4’ .1 M19an4” (WWW — s“ FhA-afmeweo (044, to, 09;, my») MLW (moire M WE — 0 MW qwfiww airway \AA—st n; {Wm-i -E_\ (JQAAIKEI—ai“) +5, + £1 (kid-23,.) 724? g7; O.w-S,—3,_ MAHSE—JL ‘5. §L 13"9-132. 72f nl'of- noi— mun}— mm. n+9;- fled; ample 1+0”). W53an Jr gawk Dehydmgenation of Propane Propane is dehydrogenated to form propylene in a catalytic reactor: (.2ng —-“ {331—15 ‘— H3 spa) The process is to be designed [or a 95% overall conversion of no one. The reaction products are separated into two streams: the first. which contains [[1. Calla, and 0.55.5 “it: of thc to auto that .9ch) leaves the reactor. is taken off as product; the second stream. which contains the balance of thC unreacted 1'0 one and 5% of themte in the first stream, is recycled to the reactor. Calculate S. a) not. the tatlo mo es t'ecyclcd)fi(moltmtzi), and thc single-pass f the composition of the prod conversion. [)6wa of M);6{0QIQVDW (w PW!) Cfl/QAW W gin/0:sz JAY/(X #MW [9) My»? Tévvjq 6v Mn? (1;) av Sofamk MA WHOM/[6 wax/ac,de VZE’WV‘S. EMMA/rib 4.715 [QM/{75m +fléy04. + )0qu Recycle and Purge in the Synthesis of Methanol Methanol is produced in the reaction of carbon dioxide and hydrogen: (:0; + 3H; —-"' + Bag The fresh food to the process contains hydro cn. carbon d' ' c a mole “it: inerts {I}. The reactor effluent passes to a cwser that removes essentially all of the methanol and water formed and none of the reactants or inerts. The latter substances are recycled to the reactor. To avoid buildup of the inerts in the system: a purge stream is withdrawn from the recycle. ThW2Liflot the fresh feed to the process) contains 281] rnole "a (20;, r -/ Tilt] rnolc‘it: 1-1;. and Elli] molest: inerta The single-pass conversion of hydrogen is titlll'io. Cal— culate the molar flow rates and molar compositions of the fresh feed, the total feed to the reactor: the recycle stream? and the purge stream for a methanol production rate of155 kmol CHgflHl’h. Qfig W M 344% (region!) M L It“.th r———’—fi (MW —————7 [pnMSGW‘ all 1254M: ...
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20._Mar-3 - Sfeagrmfim :@ ffoMQz/i HA7. 0:. , 7%.6’ ’Z...

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