RobustNonlinearContro_省略_usStirredTankRe
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( T r - T rf 0 ) < CA f 0 - CA , x 2 = , CA f 0 T rf 0 © 1994-2010 China Academic Journal Electronic Publishing House. All rights reserved.
Fr , T rf 0 V j Fj ( T rf - T rf 0 ) < CA f 0 - CA f , d 2 = , CA f 0 T rf 0 ( T j f - T jf 0 ) < E , <= , T rf 0 R T rf 0 - ∃H CA f 0 < UA , Βr = , Θ F rΘ 0 rC p r T rf 0 0 rC p r ( T jf 0 - T rf 0 ) < UA V r , x 3f = , F rΘ C V T rf 0 0j p j j 3 Vr t , t= . k 0 Σ exp ( - <) , Σ= Fr Σ
ca rried ou t in a CSTR.
2 M a thema tica l M odel for CSTR
A CSTR is u sed to convert reactan t s in to p roduct s, the reacto r and it s con t ro l schem e a re show n in F ig. 1. Con sider an irreversib le exo therm ic react ion A →B ca rried ou t in a CSTR , the chem ica l react ion ra te is a ssum ed to fo llow first 2 o rder k inet ics, and the p rocess is m odelled by the fo llow ing [ 1- 5 ] : equa t ion s
136Байду номын сангаас
J ou rna l of S hang ha i U n iv ersity
0
g (x ) =
0
x 3f - x 3
, ∃ f (x ) =
d1 d 2 , ∃ g (x ) =
0 0
d3
0
3 D es ign of Robust Track ing Con tro ller
In th is sect ion the robu st con t ro l ob ject ive is to design a p a ram eterised feedback con t ro l law such tha t the desired ou tp u t t ra jecto ry of the clo sed 2loop system is ach ieved and the effect s of system uncerta in ty is w h ile m a in ta in ing the boundedness of a ll signa ls in side the con t ro l loop s. Con sider the fo llow ing non linea r uncerta in system
x = f (x ) + g (x ) u + ∃ f (x ) + ∃ g (x ) u , y = h ( x ).
n
F ig. 1 Schem a tic diagram of CSTR
・
( T j - T rf 0 ) < V x 3 = , u =
d 1= d 3= B=
Βc =
D=
(N anj ing U n iv ersity of S cience and T echnology )
Abstract T h is p ap er dea ls w ith the tem p era tu re track ing con tro l p rob lem of con tinuou s stirred tank reacto rs (CSTR s) w idely u sed in chem ica l engineering. D esign of robu st track ing con tro ller fo r a cla ss of CSTR s p lan t . T he con tro l schem e ha s w ith uncerta in ties is p resen ted u sing inp u t 2 ou tp u t feedback linea riza tion techn iques been app lied to a first 2 o rder irreversib le exo therm ic reaction p rocess ca rried ou t in a CSTR , and si m u la tion resu lts show tha t it is effective. Key words chem ica l reacto rs, tem p era tu re track ing, linea riza tion, uncerta in ties non linea r con tro l, robu st con tro l, feedback
UA
r
(T r - T j ) ,
dT j F j UA ( T jf - T j ) + (T r - T j ) = Θ d t3 V j 0 j C p jV j
3
w here C A is react ion concen t ra t ion, t is react ion t im e, T is tem p era tu re, V is vo lum e, and F is flow ra te. R eacto r and coo ling jacket va lues a re deno ted w ith sub scrip t s r and j resp ect ively, the in let feed va lues and reference va lues a re deno ted w ith sub scrip t s f and 0 resp ect ively, T he rem a in ing sym bo ls a re defined in the A pp end ix.
R eceived N ov. 26, 1997 X iang Zhengrong, Ph. D. , D ep a rtm en t of A u tom a tic Con tro l, N an jing U n iversity of Science and T echno logy, N an jing, 210094
dC A F r - E (C A f - C A ) - C A k 0 exp = RTr , d t3 V r dT r F r ∃H CA ( T rf - T r ) + = k 0 exp Θ d t3 V r 0 rC p r - E RTr ( 1b ) ( 1c) ( 1a )
Θ 0 rC p rV
1 In troduction
Robu st con t ro l of uncerta in system s is a cen t ra l issue in con t ro l theo ry. In the p a st few yea rs m uch in terest ha s been devo ted to the design of robu st con t ro ls fo r dynam ic system s w ith uncerta in t ies. D esp ite the advances in the theo ry of non linea r [6 ] con t ro l system s , up to da te the issue of design ing robu st feedback con t ro ls of non linea r system s w ith uncerta in t ies ha s no t been fu lly invest iga ted. Robu st t rack ing of a cla ss of uncerta in non linea r system s sa t isfying the so 2ca lled m a tch ing cond it ion ha s been [ 7, 8 ] ana lyzed in a num ber of p ap ers . How ever, the p rob lem of robu st t rack ing and robu st p erfo rm ance of non linea r system s w ith uncerta in t ies rem a in s to be im po rtan t and cha lleng ing. Con t inuou s st irred tank reacto rs ( CSTR s ) a re included an im po rtan t cla ss of indu st ria l p rocesses w here con t ro l ha s to dea l w ith uncerta in t ies. In th is p ap er w e study the tem p era tu re t rack ing p rob lem of a cla ss of uncerta in CSTR s via regu la t ing the coo ling st ream flow ra te, and the con t ro l st ra tegy of robu st t rack ing fo r a cla ss of CSTR s w ith uncerta in t ies is p resen ted u sing inp u t 2 ou tp u t feedback linea riza t ion techn iques. T he effect iveness of the m ethod is illu st ra ted by a sim u la t ion exam p le on the tem p era tu re con t ro l of an exo therm ic react ion p rocess