S Quy Trnh Dng Pro/II

Pro/II

buingocpha@hcmut.edu.vn

CHNG 2: CC THAO TC THNG DNG THIT B PHN NGNi dungI. Giao din ca PRO/II - Qui c ban uII. Ca s PRO/IIIII. Cc thao tc thng dng trong m phng bng PRO/II1. M mt chng trnh m phng mi (Opening a New Simulation)2. M mt chng trnh m phng c (Opening an Existing Simulation)3. Ghi mt file m phng ang hin hnh (Saving the Current Simulation)4. Xa mt chng trnh m phng (Deleting a Simulation)5. Sao chp mt chng trnh m phng (Copy a Simulation)6. Thay i dng ng vin cc dng (Modifying the Flowsheet Stream Border Style)7. Hin th tnh cht ca dng trn s m phng8. S dng Flash Hot-key Tool9. Xut mt s m phng ra ca s lu tr tm (Exporting the PFD to the Windows Clipboard)10. Nhp mt file PRO/II c sn11. Xc nh cc tnh cht v cn bng lng-hi ca cc h 2 cu t (Display BVLE) IV. THIT B PHN NG TRONG PRO/II2Khi khi ng PROII, u tin s xut hin mt ca s giao din qui c ban u nh hnh bn.

Cc nt hoc cc biu tng trong mt vi trng hp c vin quanh bi 1 trong 6 mu: , xanh lc, xanh dng, vng, nu v en. ngha ca mi mu nh sau :

: d liu yu cu cn phi nhp Xanh lc : d liu mc nh hoc la chn Xanh dng : d liu va cung cp tho mn yu cu Vng : d liu ta va nhp ngoi khong cho php Nu: d liu khng c gi tr en: d liu khng yu cu nhp vo I. Giao din ca PRO/II- Qui c ban u 3Ca s PRO/IIDng trn cng gi l Application Title Bar (Thanh tiu ng dng), c tn ca ng dng l PRO/II with PROVISION, km theo l Document Title Bar (Thanh tiu ti liu) c tn ca chng trnh m phng ang thc hin (chng hn l View 1 - l tn nguyn ca ti liu khi mi khi ng PRO/II)Dng th hai gi l Menu Bar (Thanh trnh n) gm 10 mc t File n Help ;Dng th ba gi l Standard Tool Bar (Thanh cng c chun) cha biu tng ca cc lnh thng dngBn phi v pha di mn hnh l thanh trt dc v thanh trt ngang

Bn phi mn hnh, bn ngoi thanh trt dc l thanh cng c floating PFD (Pipe Flow Diagram). Nu thanh cng c PFD khng hin th th ta c th gi n nh sau :-click vo biu tng Show or Hide PFD Palette trn Standard Tool Bar-hoc t View Palettes nhp chn (hoc khng) PFDNgoi ra cn c thanh cng c Run. lm xut hin hoc bin mt thanh cng cny cng t View Palettes nhp chn (hoc khng) RunT File menu Chn New : mt ca s View1 s xut hin cho chng ta mt flowsheet mi nh sau:II. Ca s PRO/II

Standard Tool Bar (Thanh cng c chun) cha biu tng ca cc lnh thng dngIII. Cc thao tc thng dng trong m phng bng PRO/II 1. M mt chng trnh m phng mi (Opening a New Simulation) T File Menu New; Nu ta mun PRO/II lun lun c m vi mt chng trnh m phng mi Options Menu New File on Startup;

2. M mt chng trnh m phng c (Opening an Existing Simulation) Ta c th m bt k mt chng trnh m phng no c ghi trc chnh sa, xem hoc in. Qui trnh: T File Menu Open hin th ca s Open Simulation; Nhp tn chng trnh vo hoc chn tn file m phng; OK hoc Enter hin th file Simulation cn thit.3. Ghi mt file m phng ang hin hnh (Saving the Current Simulation) a. Ghi mt file m phng ang hin hnh T File Menu Save nu ta cha ghi chng trnh m phng ny ln no th s hin th ca s Save as nhp tn Chn OK hoc nhp Enter. Cn sau ln ghi u tin, mun ghi li file ang hin hnh nhp vo biu tng Save. Chng trnh PRO/II s t ng nn 3 file d liu (*.pr1, .pr2, .pr3) v 1 file flowsheet biu cc dng (*.sfd) thnh mt file n *.prz. V vy, bn cnh vic gim kch thc ca cc file lu tr cn m bo rng vic ci t file hon thnh mi khi chng ta ghi cc chng trnh m phng. Chc nng Autosave ca PRO/II s t ng to mt file sao chp d phng (backup file). Nu ta ng hoc thot ra chng trnh m phng m khng ghi th file ny s b xa. Hy chn Options / Simulation Defaults / Autosave t menu bar hin th ca s Autosave Options nhp chn Automatic Save File every nhp chu k save (pht) OK.b. Ghi mt file m phng vi mt tn khc T File Menu chn Save as hin th ca s Save as Nhp tn mi cho chng trnh m phng Chn OK hoc nhp Enter.III. Cc thao tc thng dng trong m phng bng PRO/II 4. Xa mt chng trnh m phng (Deleting a Simulation) T File Menu chn Delete PRO/II s hin th mt danh sch cc file m phng c; Nhp hoc chn tn ca flie mun xa (Ta khng th xa mt chng trnh m phng ang hin hnh); Chn OK hoc nhp Enter PRO/II s xa tt c cc file lin kt vi chng trnh m phng ny;

5. Sao chp mt chng trnh m phng (Copy a Simulation) PRO/II c th copy tt c cc file lin kt vi chng trnh m phng (3 file d liu v 1 flowsheet) vo mt file m phng mi hoc ang hin hnh. Nu ta mun copy vo mt file m phng ang hin hnh PRO/II s hi ta c mun vit ln file hin hnh ny khng? T File Menu chn Copy PRO/II s hin th ca s Select File to Copy Hy chn tn file cn copy (Ta khng th copy mt chng trnh m phng ang hin hnh) Nhp tn file ch (target) OK;III. Cc thao tc thng dng trong m phng bng PRO/II 6. Thay i dng ng vin cc dng (Modifying the Flowsheet Stream Border Style) Thng thng ng vin cc dng thng c dng hnh ch nht Chng ta c th thay i thnh ng vin dng trn. Qui trnh nh sau : - Right-click vo dng c chn hin th ca s la chn;- Chn Display xut hin ca s Stream Style;- Chn Circle t drop-down list box ca Stream Label Border;- click OK ng vin dng c chn t dng hnh ch nht chuyn thnh ng vin dng trn. Vi cch nh trn, bn c th thay i dng ng vin cho tng dng ring l. Cn nu mun, bn c th click chut tri v qut chn mt hnh ch nht bao xung quanh cc dng mun thay i dng ng vin ri tin hnh qui trnh nh trn. Hoc bn c th mc nh dng ng vin cho tt c cc dng ngay t u theo qui trnh sau: - T Options Menu Drawing Defauts Stream Display hin th ca s Stream Style;- Chn Circle t drop-down list box ca Stream Label Border. V la chn ny ch c gi tr khi chng ta chn Name mc Stream Label Type OK. III. Cc thao tc thng dng trong m phng bng PRO/II Qui trnh nh sau: (a) Right-click vo dng c chn hin th ca s la chn; (b) Chn Display xut hin ca s Stream Style; (c) Chn Properties t drop-down list box mc Stream Label Type; (d) Mc nh mc Property List l Property Label List s hin th tn, nhit , p sut v lu lng dng OK.

7. Hin th tnh cht ca dng trn s m phng PRO/II c mt cng c hu ch cho php hin th nhanh chng cc tnh ton flash ca bt k dng no c chn l cng c Flash Hot-key, cung cp mt phng tin nhanh chng, d dng xc nh hm lng v thnh phn ca pha lng v pha hi ca bt k dng no.

8. S dng Flash Hot-key Tool 9. Xut mt s m phng ra ca s lu tr tm (Exporting the PFD to the Windows Clipboard) T Clipboard, ta c th dn mt cch n gin hnh v ln bt k mt chng trnh son tho no nh trong Microsoft Word. Qui trnh nh sau : T Menu File Export Chn Flowsheet Drawing Click OK PRO/II s hin th mt hp hi thoi khng nh rng flowsheet c xut ra ca s lu tr tm

10. Nhp mt file PRO/II c sn (Importing a PRO/II Keyword Input File) Ta c th nhp mt file keyword Input ca PRO/II dng *.inp c sn vo giao din PRO/II ang hin hnh. PRO/II s t ng chuyn i file ny thnh mt s tnh ton v ta c th tin hnh m phng nh m phng trn mt s PFD, t ta c th chnh sa theo mnh T Menu File Import Nhp hoc chn tn ca flie mun nhp Chn OK hoc nhp Enter III. Cc thao tc thng dng trong m phng bng PRO/II 11. Xc nh cc tnh cht v cn bng lng - hi ca cc h 2 cu t (Display BVLE) xc nh cc tnh cht v cn bng lng - hi ca cc h 2 cu t ny p sut bt k no , ta s dng cng c Display BVLE. Qui trnh nh sau : Chn cu t v m hnh nhit ng thch hp Nhp chn biu tng Display BVLE Chn cc cu t, chn p sut v nhp chn Calculate Ta s c 5 loi biu :

- Biu X - Y - Biu T - X - Y - Biu h s Fugacity - Hng s cn bng K theo phn mol - Hng s cn bng K theo nhit III. Cc thao tc thng dng trong m phng bng PRO/II

IV. CC LOI PHN NG TRONG PRO/IIConversion Reactor

Equilibrium Reactor

Gibbs Reactor

CSTR (Continuous-Stirred Tank Reactor)

PFR (Plug Flow Reactor)

Phng trnh phn ng ha hc phi c nh ngha trc ti ca s Reaction Data.

y l ca s chnh cung cp cc d liu c bn cho thit b phn ng:

Unit Reaction Definitions Button: m ca s nhp cc thng s cho phn ng.Reactor Data Button: m ca s nhp cc thng s ca thit b phn ng.Pressure Button: m ca s xc nh cc gi tr v p sut.

Reactor Type: Loi thit b phn ngReaction Set Name: la chn phn ng xy ra trong thit b, phn ng ny c xc nh ti ca s Reaction Data.Thermal Specification:Temperature Rise: s tng nhit trong thit b.Fixed Temperature: nhp nhit vn hnh mong mun cho thit b.Fixed Duty: nhit lng tiu tn khi vn hnh thit b.Unit reaction definitions button

Ca s ny dng xem h s t lng ca phn ng cng nh nhp cc thng s ng hc phn ng cho thit b.Reactor Operation Phase: i vi thit b phn ng khuy lin tc, pha ca phn ng trong thit b c th la chn l pha lng (Liquid) hoc pha hi (Vapor).Reaction Activity Basis: chn Mole Fraction tnh ton bng phn mol cht phn ng.Ta c th xem li phng trnh phn ng ha hc xy ra trong thit b:Name: tn ca phng trnh ha hc.Definition: cc cht tham gia, cht sn phm cng nh h s t lng.Kinetic Data Button: m ca s nhp cc thng s ng hc ca phn ng.Nhp cc thng s phng trnh cn bng vo phn Equilibrium Data:

Reactor data buttonCa s Reactor Data c dng xc nh d liu ca thit b phn ng:Reactor Volume: th tch ca thit b phn ng, y l thng s bt buc phi xc nh thit b c th tnh ton c thi gian lu.Product Estimates Button: cung cp cc gi tr c tnh cho cc thnh phn trong sn phm phn ng.

Pressure button

Mc nh ca thit b l gim p sut ca dng sau khi qua thit b l 0. C th cung cp cc gi tr gim p hay p sut u ra ca dng sn phm bng nhp vo cc la chn tng ng v nhp s.IV.1. Conversion Reactor Sn xut ethanol t tinh bt c thc hin qua cc bc nh sau:Bc 1: Tinh bt + H2O Glucose , hiu sut 89% (C6H10O5)n + nH2O nC6H12O6 n= 200-1000, chn n=800

Bc 2: Glucose Ethanol + CO2 , hiu sut 68.7% C6H12O6 2C2H5OH + 2CO2

M phng bng Pro/II qu trnh phn ng trn!(Nhit phn ng 180 oC)Conversion Reactor: THC HNH-1

Thm cu t mi24

Amylose structureCategoryGroupAlcohols02001600Alcohols0277800Ethers06021600Paraffins 09022400

Structure of glucoseCategoryGroupNumberAlcohols02004Alcohols02141Aldehyde03001Paraffins 09023

31

ComponentMolecular Weight (g/mol)Standard Liquid Density (kg/m3)Normal Boiling Point ( oC )Starch129600 1500250Glucose1801540150Click Fixed trong mc Thermophysical properties. Nhp thuc tnh ca STARCH v GLUCOSE theo bang sau.1 gc C6H10O5 la 16232

nh ngha cc phn ngBc 1: Click icon Bc 2: di Reaction Set Name. G SET1 vo hng 1, SET2 hng 2. Sau nhp d liu cho tng phn ng bng cch nhn Enter Data.

Bc 3: Click Enter Data cho SET1.Bc 4: Click di Name. Nhp THUYPHAN ri click dng Reactants = Products.Bc 5: Cn bng phn ng Starch + 800 H20 800 Glucoseg 800 cho H2O. G 1 cho STARCH, v 800 cho GLUCOSE. Bc 6: Click OK 2 lnBc 7: g LENMEN cho SET2 ri click dng Reactants = ProductsBc 8: cn bng cho phn ng Glucose 2 C2H6O + 2 CO2g 1 cho GLUCOSE, 2 cho C2H6O, v 2 cho CO2.

3.To conversion reactor R1(cho phn ng thy phn tinh bt)

To conversion reactor R1(cho phn ng thy phn tinh bt)To dng cc dng u vo cho TBP

Reactor Data.

Reaction Definitions.

Convertion = A+B*T+C*T2

RUN The Simulation.Thc hin phn ng thun nghchL thit b dng thng cha trong thc hin cc phn ng cn bng. Thnh phn cht phn ng v qu trnh ha trn c coi l l tngTnh ton hot tnh ha hc ca mi cu t hn hp trn c s hot ca hn hp v cu t tinh khit

IV.2. EQUILIBRIUM REACTOREQUILIBRIUM REACTOR: THC HNH 2Phn ng tng hp Etylen glycol t Etylen oxide. CH2 (O)CH2 + H2O OHCH2-CH2OH

Hai dng nhp liu c sut lng mi dng l 100 kmol/h c a vo thit b trn Mixer, sau c a vo bnh phn ng. Dng sn phm ra c tch li mt dng hon lu, mt dng thu sn phm. M phng v ti u ha qu trnh sn xut etylen glycolCc thng s:Dng 1: 100 kmol/h EODng 2: 99% H2O, 1% H2SOT= 550CP=1 kg/cm2Hon lu 10 kmol/hChi ph EO70 $/kmolH2O30 $/kmolHon lu20 $/kmolBnh30 $/kmolGi bnEG150 $/kmolM phng bng Pro/II?Tnh ton ti u ho?3. CC BC TIN HNH M PHNGBc 1: To dng bn s qui trnh sn xut. B tr thit b ln mn hnh. V s cc dng sao cho ph hp.

Bc 3: Vo ca s Component Selection khai bo thnh phn cc cu t H2O, EO, EG, H2SO4 (chn Select from Lists)

48Bc 4: Vo ca s Thermodynamic Data xc nh phng php nhit ng, vo Most Common Used Chn NRTL

Bc 5: Thit lp cc thng s cho dng.Dng S1 (nhp liu lng) Composition Defined Flowrate and Composition Total FluidFlowrate Individual Component Flowrates (nhit 55oC v p sut 1 kg/cm2)

Thao tc tng t vi dng S2. Ta c:

Nhp Reaction Set Name Chn Enter Data Chn Name Nhp h s trong Reactant stoichiometry nh sau:Bc 6:Vo ca s khai bo thng s ng hc cho phn ng

Chn E trong Reaction defination, nhp A, B ta c:

C:[kg-mol/m3],R: 1.987[kcal/kg-mol K],r:[kg-mol/m3 h]Bc 7: Khai bo cc thng s cho TBPUVo Reactor Data, nhp 5 vo ct Reactor Volume, nhit 55oCta c:

Bc 8: Khai bo cc thng s cho thit b splitterChn hnh thit b splitter, nhp parameter stream S6Chn flowrate All components nhp 10.Ta c:

Bc 9: Khai bo xong, nhn nt chy th m phng

4. TNH TON V TI U HA (hc sau)-Chn calculator t hp PFD-Trong hp thoi calculator, chn Edit/wiew declarations chn parameter Nhp 1 Set up definition.. Stream S5 flowrate All componentsTa c:

-Thao tc tng t vi parameter number 2,3,4 ta ng vi S6, S1, S2.-Vi parameter number 5 ta chn TBPU volume nh hnh bn.

Ta c bng sau:

Trong hp Calculator chn constants v nhp cc gi tr hng s nh sau:

Trong hp Calculator chn Results v nhp nh sau:

Chn Hide Declarations Nhp vo Procedure

-Chn optimizer t PFD-Chn maximize Parameter Calculator R(2) nh hnh sau

Tip tc thao tc trong hp thoi variables nh sau:

i vi bin s cho dng hay thit b, chn Minimum Value v Maximum Value, nhp gi tr cc tiu 5 v cc i 50.

Tin hnh chy v xut kt qu

PFR (Plug Flow Reactor)

THC HNH 3: PFRng hc phn ngtng hpcaethylacetatetmethanolvaxitaxeticCH3COOH + C2H5OHCH3COOC2H5 + H2O HOAC EtOH EOACTham kho: Song,W.,G. Venimadhavan,J.M.Manning,M.F.Malone, and M.F.Doherty Measurement of Residue Curve Map and Heterogeneous Kinetics in Acetate Synthesis, Ind.Eng.Chem.Research,37,1917-1928(1998)r = kf(CHOACCEtOH - CEOACCH2O/Keq)Vi: Keq l hng s cn bng ca phn ng. (K Equilibrium)kf = 9.732.108exp(-12493.6/RT) (m3/kg-mol.h)Keq = 2.32exp(1555.78/RT)Phng trnh trn bt ngun t cc phng trnh di y:rf = kf CHOACCEtOH rb = kbCEOACCH2Okb= kf/Keq = 4.195.108exp(-14049.4/RT)ln(Keq) = 0.84156 + 782.98/TC:[kg-mol/m3],R: 1.987[kcal/kg-mol K],r:[kg-mol/m3 h]Thc hnh

Thc hnhBc 1: S thit b phn ng.Ti thanh PFD Chn Reactor 2 x Plug flow Reactor v 1 Gibbs Reactor m phng.

Thc hnhBc 2: Xc nh danh mc cc cht thnh phn.Vo Th Input Component Selection hoc click chut vo biu tng trn thanh cng c chn cc cht thnh phn. Nhp cc cht thnh phn ti Component nhn Add nhp cht hoc vo Select from List chn cht thch hp Thit lp Component Phases (thnh phn pha) l Vapor-Liquid( hi lng) cho tt c cc cht.

Thc hnhBc 3: Xc nh phng php/m hnh nhit ng v phn ng.Chn NRTL, v ta x l hn hp Hydrocacbon:Chn h nhit ng NRTL t hp danh mc Primary Method Add Single Liquid Phase Only xc nh phng php nhit ng i vi h ang xt: Vi h l tng v khng l tng chn phng php Hayden OConnel: chn Modify Property: Vapor Fugatcity Chn Hayden OConnel Vi cu t phn cc nh Etanol nn chn RKMPR: trong mc: Liquid Entropy v Vapor Entropy th ta chn SRK Modified Panag ReidKt thc click thanh Transport Properties tick vo Compute Transport. OKThc hnhBc 4: Nhp h s t lng cc cht tham gia phn ngVo Input hoc click biu tng chn Reaction Data Vng Reation Set Name t l SET1, SET 2 Enter Data t tn R1( phn ng thun) ,R2 ( phn ng nghch) chn h s t lng ca tc nhn v sn phm (1:1/1:1) trong ca s

Thc hnh

Thc hnh

Thc hnh

RRATES(1)=PREEXP(1)*EXP(-ACTIVE(1)*1000/(RGAS*RTABS))&*XLCONC(1)*XLCONC(2)RRATES(2)=PREEXP(2)*EXP(-ACTIVE(2)*1000/(RGAS*RTABS))&*XLCONC(3)*XLCONC(4)ISOLVE=1RETURNThc hnh

Thc hnhBc 9: Nhp Thng tin cho cc thit b lm vic.Vi thit b PFR1 ( thit b phn ng lm vic theo cn bng nng lng):Dng vo: Nhit phn ng t =77oC p sut phn ng: P = 1.0332 kg/cm2 (101.3 kPa) Nng nhp liu : Acid Acetic 280 kg-mol/hrEthanol 280 kg-mol/hr

Thc hnh

Thc hnh

Thc hnhVi thit b PFR2 ( thit b phn ng tnh ton theo nhit ng hc)Dng nhp liu ging vi PFR1Kch thc v ch thn thit b: (2) chn Unit Reaction Definitions chn Kinetic Procedure PSET1

Thc hnhThit b phn ng Gibbs

runIV.4. THIT B PHN NG KHUY LIN TC

I. L THUYT

Bi ton :sn xut propylene glycol trong thit b phn ng khuy trn hot ng n nh on nhitPropylene glycol c sn xut t phn ng thy gii propylene oxide nhit thng 20oC vi xc tc l sulfuric acid.Nhp liu c sut lng 1250 kg/h (21.52 kmol/h) propylene oxide c a vo bnh phn ng thnh 2 dng : (1) 1 dng c lu lng bng nhau 1260l/h propylene oxide v 1260l/h methanol v (2) 6294 l/h nc cha 0.1% H2SO4 theo khi lng. Lu lng mol tng ng ca methanolv nc l 35.94 v 401.4 kmol/h. Nhit c 2 dng nhp liu l 24oC. Phn ng l bc 1 theo propylene oxide v c hng s vn tc phn ng l : k=16.96x1012(e-41830/RT) ,h-1.V propylene oxide si nhit thp nn nhit phn ng khng vt qu 51.7oC.Vi th tch bnh l 1083 lt.THC HNH 4M phng bi ton trn pro II

M phng thc hin phn ng trong 1 bnh phn ng :Bc 1: To dng s qu trnh (thit b, dng)

Bc 2: Xc nh cc cht tham gia phn ng

Bc 3: Xc nh phng php nhit ng:

Click chut vo biu tng trn thanh cng c chn phng php nhit ng t mt danh mc cc phng php nhit ng ph bin .Trong ca s Thermodynamic Data : Chn Most Commoly Used trong danh mc CategoryChn Peng-Robinson t hp danh mc Primary Method Click chut vo nt bm Add xc nh phng php tnh ton nhit ng i vi h ang xt.

II. BAI TOANII. BAI TOAN

Bc 4: Xc nh cc d liu v phn ng

Nhp 1 vo Reaction Set Name trong ca s Reaction Data Click vo Enter Data , nhp 1 vo hp danh mc Name , click vo dng Reactants = productsNhp cc h s t lng cho cc cht tham gia phn ng, tc cht ct bn tri v sn phm ct bn phi.II. BAI TOAN

II. BAI TOANII. BAI TOANChn ch K khai bo cc d liu v ng hc phn ng theo phng trnh.

II. BAI TOANClick vo R khai bo bc phn ng

Bc 5: Khai bo d liu i vi cc dng

Nhp d liu dng S1 :Click i chut vo dng S1, xut hin ca s Stream Data : Chn nt Flowrate and Composition khai bo lu lng dng nhp liu v t l cc tc cht tham gia phn ngSau , khai bo nhit v p sut ca h thng: Click chut vo mi tn hng xung trong vng d liu First Specification v chn Temperature, nhp gi tr nhit 72.5, Chn Pressure t hp danh mc ri Second Specification, nhp gi tr 14,696

II. BAI TOANII. BAI TOAN

II. BAI TOAN

II. BAI TOANNhp d liu dng S2 :

II. BAI TOAN

II. BAI TOANBc 6: Khai bo d liu i vi thit b

Click i vo thit b R1, xut hin ca s Continuous Stirred Tank Reactor.Chn 1 dng Reaction Set Name .

II. BAI TOANNhn vo nt Reactor Data, nhp 1.083 vo Reactor Volume trong ca s Reactor Data, click OK 2 ln tr li mn hnh PFD .

II. BAI TOAN M phng thc hin phn ng trong 2 bnh phn ng ni tip nhau:Ta thc hin nh thc hin phn ng trong 1 bnh, nhng ta s cho dng vo 2 bnh phn ng c th tch bng nhau

II. BAI TOAN

ConversionReaction

EquilibriumReactionKineticReactionHeterogeneousCatalytic ReactionYes

YesLU : khi la chn phn ng

Thng tin vPhn ng

Bit chuyn ho

No

Bit hng scn bng

No

Bit tc phn ngSimple RateReactionCc c im chung khi m phng TBP

Tt c cc loi phi c h s t lng ca phn ng.

Mi phn ng i hi cc thng s ph hp:

Conversion: bit chuyn ho

Equilibrium: bit hng s cn bng CSTR v PFR: phi c k (cng thc tnh k)

3. Cc phn ng c th c trong: Tank Separator Three Phase Separator Column