HEMISKI Zbirka re{eni zada~i REAKTORI 3

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[esti del Industriski <strong>re</strong>aktori
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HEMISKI REAKTORI 3 Zbirka re{eni za
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Skopje, 2010
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Predgovor . . . Hemiskiot reaktor e
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lot da se stekne so ve{tina da gi k
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~ite }e mu ovozmoì preku niv da go
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5. TOPLINSKI BILANSI ..............
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XIV êtvrti del IDEALEN CEVEN REAKT
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Zada~a 4. Adijabatski PBR so pretho
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1. STEHIOMETRIJA 1.1. Prost reakcio
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Prv del. Definicii, koncepti, stehi
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2. TOPLINA NA REAKCIJA I HEMISKA RA
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3. IZRAZI ZA BRZINA NA REAKCIJA 3.1
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Molskite koncentracii vklu~eni vo b
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kako ravenkata (52). Razlikata e vo
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Ravenkite za dizajn na cevniot reak
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Ravenkata za dizajn na ceven reakto
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Za presmetka na brojot na reaktorit
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28 Po~eten uslov za re{avawe na sis
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Toplinski bilansi za adijabatska ra
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32 T H ( r ) V r A a, vlez Ta, vle
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Toplinski bilansi za izotermna rabo
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Osnovnata ravenka na toplinskiot bi
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38 H / L Q q dz Ua ( T T ) dz ;
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Vtor del [arèn reaktor
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Re{enie: a) Za izotermna rabota na
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POLYMATH Results Calculated values
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Explicit equations as entered by th
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Jasno e deka vremeto potrebno za re
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Zada~a 2 64 [arèn reaktor i CSTR s
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Rezultatot e deka so eden {arèn re
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Vo ravenkata za dizajn (48) gi zame
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a) Brojot na {arìte koj }e go obez
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Kone~nata forma na brzinskiot izraz
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76 Mi % (w/w) 1 3 Cio smesa kmol/m
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Re{enie: Samo so primena na ravenka
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data e so sè pomali temperaturni r
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) Za varijantata na razmena na topl
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( H r )( rA ) V TW , vlez T
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Vkupnata koli~ina toplina {to }e se
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) Za presmetka na vremeto na reakci
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( 1 X ) To C A C Ao ; (1) ( 1 0, 5
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11620 X T To . (6) 38, 73 12, 91X
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96 t r t r C P dP dP C Ao ; 0, 5(
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a) Od kineti~kite podatoci da se op
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100 C C W n C Wo / V Wo W rastvor
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A B ; ( rA) k1C A k2C B ; 7 1 k
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) Vremeto na reakcija za 80% konver
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presmetki za izotermna rabota na re
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Zada~a 1 Hidrogenacija na etilen vo
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Tret del. Proto~en reaktor od rezer
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1 Tret del. Proto~en reaktor od rez
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POLYMATH Results Tret del. Proto~en
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F F X X A1 B1 1 1 Tret del. Proto~e
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C B2 0, 1056 F F X 2 A2 B2 2 Tre
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Zada~a 8 Tret del. Proto~en reaktor
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Explicit equations [1] R = 0 [2] T
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X * XMB XEB X*; XMB; XEB 1 0.8 0.6
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XMB XEB 1 0.8 0.6 0.4 0.2 Zada~a 10
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( C C A1 ( C C A2 ( C C A3 A Tret d
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1 Tret del. Proto~en reaktor od rez
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Zada~a 15 Tret del. Proto~en reakto
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C C C C Bo Bo Wo Wo Tret del. Proto
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dT dt Tret del. Proto~en reaktor od
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Zada~a 1 Endotermna reakcija vo gas
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êtvrti del. Idealen ceven reaktor
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Re{enie: êtvrti del. Idealen ceven
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A (NO) B (O2) C (NO2) I (N2) êtvrt
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X 0 0, 2 êtvrti del. Idealen ceve
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Re{enie: a) Izotermna rabota: êtvr
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T (K) k (T) izraz (4) êtvrti del.
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( r êtvrti del. Idealen ceven reak
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0,22 êtvrti del. Idealen ceven rea
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Zada~a 16 êtvrti del. Idealen ceve
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V PFR k F Ao êtvrti del. Idealen c
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Ropt=1,5 Vmin=1884litri êtvrti del
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Petti del Kataliti~ki reaktor so fi
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ili 318 - diferencijalen oblik, kak
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Od izve{tajot i od rezultatite od p
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Grafi~ka prezentacija na site rezul
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Ponatamu podgotvuvame brzinski izra
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Zada~a 3 326 Reakcija vo gasna faza
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Iako brzinskiot izraz e prili~no go
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330 Fio Fi() Fi(X) pi = yiP = (Fi/F
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332 A FAo B Bo Fio Fi() Fi(X) F 2F
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Ako reakcijata se odviva vo pove}ec
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Isto taka, dobro e da znaeme kolku
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Page 357 and 358: 340 Yexp X Ycalc 6087E-12 0.105 8.0
Page 359 and 360: Re{enie: Rabota so razmena na topli
Page 361 and 362: 344 dT dV dT dT dT FT CP 65, 9 6,
Page 363 and 364: Kako {to moè da se vidi od dobieni
Page 365 and 366: Komentari: 1) So adijabatska rabota
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Page 369 and 370: 352 W (kg) W (kg) (-rA) = f(W) W (k
Page 371 and 372: 354 - toplina na reakcijata: Hr = 1
Page 373 and 374: 356 dT dV ( H r )( r C A ) smes
Page 375 and 376: 358 Potrebniot broj reaktorski cevk
Page 377 and 378: 360 C TS r a, T kT pT Cv K
Page 379 and 380: POLYMATH Results Calculated values
Page 381 and 382: 364 Za brzinski izraz preku konverz
Page 383 and 384: 366 0, 2 0 h f ( X ) dX 3 0, 2 0
Page 385 and 386: 368 Sega go pi{uvame bilansot na ak
Page 387 and 388: Re{avawe na ravenkata (8) zna~i pre
Page 389 and 390: Analizata za razli~ni vrednosti na
Page 391 and 392: Re{enie: 1) Ravenkata za dizajn na
Page 393 and 394: [8] Po = (1-X)*P/(2-X) [9] Ph = (1-
Page 395 and 396: 1 ( rO ) f ( W ) ili D f ( X )
Page 397 and 398: 380 f 9, 375 ( 1, 75 0, 0585 ?) 9
Page 399 and 400: Za da zaklu~ime dali ovoj volumen e
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Page 408 and 409: Zada~a 1 Krekuvawe na aceton vo PFR
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Page 414 and 415: 0.25 0.2 X 7 0.15 6 5 4 3 0.1 0.05
Page 416 and 417: Explicit equations as entered by th
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Page 420 and 421: [esti del. Industriski reaktori O~i
Page 422 and 423: [esti del. Industriski reaktori v)
Page 424 and 425: POLYMATH Results Calculated values
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Page 428 and 429: [esti del. Industriski reaktori na
Page 430 and 431: C C C i C P P, i C P, B P, A C
Page 434 and 435: [esti del. Industriski reaktori ‡
Page 436 and 437: [esti del. Industriski reaktori Bar
Page 438 and 439: [esti del. Industriski reaktori C6H
Page 440 and 441: [esti del. Industriski reaktori ba
Page 444 and 445: [esti del. Industriski reaktori K P
Page 446 and 447: [esti del. Industriski reaktori Kak
Page 448 and 449: [14] B2 = -13020/T [15] B3 = 5.051*
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Page 452 and 453: B 4 [esti del. Industriski reaktori
Page 454 and 455: [esti del. Industriski reaktori dF
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[esti del. Industriski reaktori r1
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[esti del. Industriski reaktori To
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Y Y Y S / E B / E T / E j j
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[esti del. Industriski reaktori Adi
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( r A ) k ( T ) C [esti del. Indus
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[esti del. Industriski reaktori rat
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X * ad.=0,404 X izlez=0,274 [esti d
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[esti del. Industriski reaktori Vle
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[esti del. Industriski reaktori se
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[esti del. Industriski reaktori FB
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[esti del. Industriski reaktori vre
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Tretiot segment: POLYMATH Results C
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[esti del. Industriski reaktori Exp
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[esti del. Industriski reaktori Toi
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[esti del. Industriski reaktori Ako
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X 0.4 0.32 0.24 0.16 0.08 [esti del
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[esti del. Industriski reaktori pri
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C C C G, 2 P, 2 P, 2 C P, 1 [esti
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[esti del. Industriski reaktori Pri
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Zada~a 6 [esti del. Industriski rea
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[esti del. Industriski reaktori Za
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[esti del. Industriski reaktori Ste
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[esti del. Industriski reaktori [4]
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[esti del. Industriski reaktori Kon
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[esti del. Industriski reaktori Kin
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p p B C [esti del. Industriski reak
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[esti del. Industriski reaktori ‡
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[esti del. Industriski reaktori Od
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X 1 0.8 0.6 0.4 0.2 [esti del. Indu
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C C P, SO3 P, N2 35, 64 26, 167 [
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F Bo I y 1; A I Bo F y F To B
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[esti del. Industriski reaktori So
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[esti del. Industriski reaktori Top
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[esti del. Industriski reaktori T (
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X 1 0.8 0.6 0.4 0.2 [esti del. Indu
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2) Toplina na reakcija [esti del. I
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[esti del. Industriski reaktori Kak
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[esti del. Industriski reaktori (to
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ODE Report (RKF45) [esti del. Indus
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FB(V) r2(V) [esti del. Industriski
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[esti del. Industriski reaktori Zab
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[esti del. Industriski reaktori umo
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[esti del. Industriski reaktori Cpa
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[esti del. Industriski reaktori So
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[esti del. Industriski reaktori [3]
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[esti del. Industriski reaktori Y =
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[esti del. Industriski reaktori FC(
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W W kat kat V 1000 [esti del. In
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FB(W) FC(W) [esti del. Industriski
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[esti del. Industriski reaktori Ne
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[esti del. Industriski reaktori - R
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[esti del. Industriski reaktori Sog
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[esti del. Industriski reaktori - i
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[esti del. Industriski reaktori Gra
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[esti del. Industriski reaktori [to
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Toplinskiot bilans: [esti del. Indu
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ODE Report (RKF45) Differential equ
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[esti del. Industriski reaktori dC
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[esti del. Industriski reaktori 4-2
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[esti del. Industriski reaktori ODE
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[esti del. Industriski reaktori 4-3
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[esti del. Industriski reaktori Izr
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[esti del. Industriski reaktori Rav
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[esti del. Industriski reaktori Top
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[esti del. Industriski reaktori Exp
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[esti del. Industriski reaktori pro
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Zada~a 12 [esti del. Industriski re
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A (N2) B (H2) p p A C [( 4 [( 4 C
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[esti del. Industriski reaktori gra
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Stepen na konverzija na N2 Stepen n
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[esti del. Industriski reaktori - d
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[esti del. Industriski reaktori 12)
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[esti del. Industriski reaktori H r
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Temperatura (K) Stepen na konverzij
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[esti del. Industriski reaktori Kak
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[esti del. Industriski reaktori Ana
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HEMISKI Zbirka re{eni zada~i REAKTORI 3

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