• 沒有找到結果。

3.2

~ ™  €  Œ  Ž   ‘

- —  ‘ a  L E 1 i G H 0 E 3 Y 5  ‡ ˆ < '  p 1 P M l

m E ‡ ˆ  <  f _ U 7 ½ v w  Z ’ E i N 7

1. 1 i V ! Q K  E @ ? 7 Ç “ Q “ , E P

2. : R a E ¯ I t 7 V 9  I E P

3. b Q R 1 i V ! Q a < v w 9 L M E ? ? ³ / 7 “ , E P

'  I R U 7 S ? T U š Z 7

„ 4 u = : 7

(a) !  “ E 2 ^  ! ? G  P

3.2 … ž † ‰ Ÿ § ¨ © ª « ¬ 43

(b) b R 1 i V ! Q G > h E K  ) * G  { n P

(c) b R 1 i V ! Q " : € E  @ l ! 2 d E ³ / ? P

(d) b R 1 i V ! Q K a  , ³ / ! ? E  { P

(e) I R i ™ E ; < 0 P

? U 7 O  > 7

(a) ¬ Q 5 ¡ a v E # E 3 e P

(b) ¬   a v E ! ) ? _ P

(c) ¬ V ! Q K   L G > h G  X Y P

U 7 E Z [ 7  ‘ !  < y < U | } Q R K L M E ! 

^ _ E „ 4 < ?  o 7

(a) K C   ! E > ? P

(b) K = M  E  = P

44 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

3.3

~ ‹  €  • – ¢ £

1 F _ : 3 4 E l m p  1 i V ! Q ?  7 Q p % < 4 f _ 6

!  ` ^ _ % S ?  p  R F G < 1 i V ! Q (Ä 3.2 )K 

(Ä 3.3 )<  Q 6 ½ ~ \ Q R s t  (Mixer)< ? F ( k  ´ ¬ R V W

 “ E ! ) — f  Q  < 6   Q  E  ‘ Q a =   <  Q 6

  \ Q R  V  (Splitter)< Z E 7 k  ’ ) ! © A Q E !  Q R  V E V < P Ä 3.4 p Q R " # w E ` ^ _ <   ^ _ a  l !  “ ? 

I $ ! < ! ! > . ( @  ?  I Q R ( & < B V   V < I a ©

A F G 7 6  !   Q E : \ # E S ] w P a <  U E a b <

I R ` ^ _ !  Ç \ $ e E Ô _ < 4 Z E F _ k  G  E a b b

R d l ? : U 6 E d l 4 m  5 P { n 7 P

) 3.2 ` ^ _ (Superstructure)

Water Using S Unit M

From Other Water Using

Unit

To Other Water Using

Unit From

FreshWater Supplied From

Storage Tank

Storage To Tank Environment To

Micnload out

qi in qii n

in

3.3 … œ † ‰ Ÿ ˜ ™ ¦ § 45

) 3.3 ` ^ _ (Superstructure)

Storage S Tank

M From Water Using Unit

To Water Using Unit From Other

Storage Tank ’

out

in To Other

Storage Tank ’

) 3.4 " # w E ` ^ _

46 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

3.4

~ ‹  š › œ  ž œ ¨ © Ÿ   Œ ¨ © ¡  

( Indices, Sets, Parameters, and Variables)

1  7 ² V ` ^ _  , D < 4 ` ^ _  , D % % 9 i N ` ^ _

a < : \ a v . p   < x ? { n 7 ? { n a v E    ­ < : ? v

w 9  V  ? E P  < f g : ¡ E n @  k @ < '  f g U 7 E '

e ª x 7 „ , : R a E < j (indices)9 3 t (sets)9 : R k @ (parameters)

?  : R n @ (¼ „ # O n @  0-1n @ )(variables)9 1 2 k  ’ — 3.4.1

_ - 3.4.4_ P

3.4.1

” • – ! — B ˜ ™

(Indies and Sets)

 " E [ < j 7 ? U 6 d  E < j < + š : i7 1 i V ! Q

9 c 7 ! 2 d 2 ^ ... Z < © A [ < j . / Ò 3.1 = 4  U 7 a : 

V E # É k @  n @ « ” > R [ < j P

* 3.1 [ < j  3 t . /

c ∈ C : \ ! 2 d 2 ^ 6 3 t

e ∈ E K  ! 2 d > . — c £ E 2 ^ 6 3 t

i ∈ Ic : \ # O 7 1 i V ! Q 6 3 t i ∈ Ib : \  7 1 i V ! Q 6 3 t

i ∈ Ip  p " : \ V ! Q 6 3 t

n ∈ N : \ 0  6 3 t

n ∈ N j M 8 Q R 0  < : \ 0  6 3 t

p ∈ P : \ 6 3 t

s ∈ S : \  6 3 t

s ∈ Sp : \  p" E  6 3 t

w ∈ W : \   !  “ 6 3 t

47

3.4.2

  œ $

(Parameters)

 1 _ k a b U 7 a : ¡ E P 1 ’ ¢ < j ¡ „ 4 u : s ‘ E k @

< + š 7 Cic,maxin 6  ! G ‘ 1 i V ! Q i 0 < ! 2 d 2 ^ c E K  S

) * 6 G  G  7 Q R 9 „ , E “ , _ = 4 © f k @ 6 , m   ^ £

< š 6 2.2 :  P

* 3.2 : R k @

Cic,maxin ! G ‘ 1 i V ! Q i0 < ! 2 d 2 ^ cK  S ) * 6 G ( G 

Cic,maxout ! V c 1 i V ! Q i< ! 2 d 2 ^ cK  S ) * 6 > h G 

Cwc !  “ w: € ! 2 d 2 ^ cE G 

Micnload  0  n 1 i V ! Q ia < ! 2 d 2 ^ cE ? ? ³ /

Qmini 1 i V ! Q i S @ * K = ! @ ?

Qmaxi 1 i V ! Q i S @ * K  ! @ ?

Qmaxs  s K  E @ ?

Yinst. ∈ {0, 1},= 16  1 i V ! Q i  0  n c  ; <

Yinend ∈ {0, 1},= 16  1 i V ! Q i  0  n ^ ; <

Zcyc. ∈ {0, 1}, = 06  p Q 5 ; < ,= 16  p 2 c ; <

Δi 1 i V ! Q c  ; < ^ ; < E 0  ›

3.4.3

   $

(Variables)

1 _ k a b „ 4 n @ < j U 7 s > E n @ < ¼ „ Q 3 E # O n @ 

E 0 − 1n @ <  2 V W E : R n @ P

0 − 1n @ (binary variable)< 7 6  Q R %    N V   E n @

< Q @ _ ? ]   — 0 1 u 6 Q < \ j 0 − 1n @ E ^ } V 7 0x 7

1P + š 7  ywi = 10 < 6  m !  “ W ) 1 i V ! Q iE a v 7

  E =  ywi = 10 < 6  m !  “ W ) 1 i V ! Q i E a v 7

48 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

V   E P 4 # O n @ (continuous variable)< 7  Q , h — " : \ S ] - @ A r  } E ^ } < p # É  — N Z — 0 E @ _ < © f 0 − 1n @

 # O n @ š 6 :  =

* 3.3 # O n @

cinicn  0  n 1 i V ! Q i a < ! 2 d 2 ^ cE G ‘ G 

couticn  0  n 1 i V ! Q i a < ! 2 d 2 ^ cE > h G 

cinscn  0  n  s a < ! 2 d 2 ^ cE G ‘ G 

coutscn  0  n  s a < ! 2 d 2 ^ cE > h G 

qinin  0  n G ‘ 1 i V ! Q i E Š ) ?

qinout  0  n V c 1 i V ! Q i E Š ) ?

qiin 1 i V ! Q i  Q R 1 i V ! Q i E Š ) ?

qisn 1 i V ! Q i  s E Š ) ?

qien 1 i V ! Q i c £ e E Š ) ?

qsn  0  n  s E  Š ?

qsnin  0  n G ‘  s E Š ) ?

qsnout  0  n V c  s E Š ) ?

qsin  0  n  s 1 i V ! Q iE

qssn  0  n  s  Q R  s E Š ) ?

qwin  0  n !  “ w 1 i V ! Q iE Š ) ?

y∗n  0  n E 0 − 1n @

*∈{ si, is, ss, ii}

∀i ∈ I, s ∈ S

49

3.6

& ' ‹

(Constraints)

3.6.1

¤ ¥ ¦ § ¨ © 5 0 1 3 4

(Flow Rate Balance for Water-using Unit)

) 3.5 1 i V ! Q E ` ^ _

50 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

- Ä 3.5 S M 1 i V ! Q E ` ^ _ <  G h   E  “ S ] \ 

´ © A 1 i V ! Q i9  s< ?    !  “ wP x  Q   < V

c 1 i V ! Q E ! S ] ” ) # © f E 1 i V ! Q i9  s< ?

 > . # c £ a eP Ì (3.1)Í (3.2) T U 1 i V ! Q E ) ?  =  G

h   (Mixer) K > h   (Split) — 0  nP

qinin = 

w∈W

qwin+

s∈S

qsin+

i∈I

qiin ∀i ∈ I, n ∈ N (3.1) qinout = 

i∈I

qiin+

s∈S

qisn+

e∈E

qien ∀i ∈ I, n ∈ N (3.2)

4 1 i V ! Q G > h ) ? E  Z { Ì (3.3) Í (3.4)  6 U 6 < 4

Yinst.K Yinend p 0 − 1k @ V  > 1 i V ! Q E c   ^ E 0  =

 Yinst. = 16  1 i V ! Q i  0  n c  ; < P W l < Yinend = 1B

p ; < C ± — 0  n< -  R F i 7 S  / I " n  1 i V ! Q

i ; <  C ± 0 ! G > E Š ?  = P : ? < V ” \ # É E ! G ‘ N V

c 1 i V ! Q < — V  ; < N ^ E 0  0 P

Qmini Yinst. ≤ qinin ≤ Qmaxi Yinst. ∀i ∈ I, n ∈ N (3.3) Qmini Yinend ≤ qoutin ≤ Qmaxi Yinend ∀i ∈ I, n ∈ N (3.4)

Ì (3.5) B p 1 i V ! Q E Š ) ?  = < i N ¥ \ # É   ! E ®

¦  ˜ # P © a Δi p 1 i V ! Q ic  ^ 0  E › @

qinin = qi,n+Δout i ∀i ∈ I, n ∈ N (3.5)

51

3.6.2

¤ ¥ ¦ § ¨ © 5 ª P 3 4

(Contaminant Balance for Water-using Unit)

M 1 ) ?  = < 1 i V ! Q E > ?  =  7 v w  I E P Ì (3.6)T

(Flow Rate Balance for Storage Tank)

) 3.6  E ` ^ _

52 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

 V    <  0  n 0 P

qsnin =

i∈I

qisn+

s∈S

qssn ∀s ∈ S, n ∈ N (3.10) qsnout =

i∈I

qsin+

s∈S

qssn ∀s ∈ S, n ∈ N (3.11)

4 Ì (3.12)B p I R  s E ) ?  = <  0  n  E ! Š ?

Z — ½ Q R 0  t − 1  E ?  — 0  n 0 ! G ‘  E ?

? ( — 0  n 0 ! V c  E ? P  a Zcyc. p 0 − 1k @ 6  : R

E ; < U 7 =  Zcyc. = 00 6  p Q 5 ; < <   3 e Z  K $ 7

¥ \  ! ? E = 4  Zcyc. = 00 6  p 2 c ; < < K $   " E

! Š ? ” Z —  R 2 c ; < ^ E 0  N E  ? P

qsn = Zcyc.qsN |n=1+qs,n−1|n>1+qsnin − qsnout ∀s ∈ S, n ∈ N (3.12)

4 !  —  " E Š ? ?  G (  E ) ? E  { < - Ì

(3.13)Í (3.14) 6 U 6 P

qsn≤ Qmaxs ∀s ∈ S, n ∈ N (3.13) Zcyc.qsN |n=1+qs,n−1 |n>1+qinsn≤ Qmaxs ∀s ∈ S, n ∈ N (3.14)

3.6.4

   5 ª P 3 4

(Contaminant Balance for Storage Tank)

  a M 1  I ) ?  =  <  v w  I > ?  = P Ì (3.15)B

T U  s — 0  n  s t    E > ?  = P Ì (3.16) B p 

53

n— 0  n E Š > ?  = P š }  — W Q R 0  n W 0 \ G ‘

 V c E ) ? < B i N G ( E ) ? p ¯ 9 ž # (9 G  > )P

qsnincinscn =

i∈I

qisncouticn+

s∈S

qssncoutscn ∀s ∈ S, n ∈ N , c ∈ C (3.15) qsncoutscn = Zcyc.qsNcoutscN |n=1+qs,n−1coutsc,n−1 |n>1+qsnincinscn− qsnoutcoutscn

∀s ∈ S, n ∈ N , c ∈ C (3.16)

3.6.5

+ , - . /

(Logical Constraints)

yQL†n ≤ f ≤ yQU†n † ∈

ii, is, ss, si

(3.17)

Ì (3.17) a b ¬ d ) a < ) ? E S ) *  = h — = © a QL 6  5  a

v a ! ) ) ? E K « S ) * ) ? < QU B 7 5  a v a ! ) ) ? E  {

k @ =   <   @ A U 7 a  ‘ 1 0 − 1n @ (Binary variables)< y< I

 6  @ ! ) a v 7 ­   <    < B y = 1< Ï 6 < y = 0= : ?

I R { n 7 U 6 E 4 m <  @ Q R ! ) a v   0 < a v a E ! ) )

? v w  ) ?  Z { E h —  a P   ) ?  E { n 7 ( { n 

I t  E ; < { n P

Ì (3.18)Í (3.19)B 6  # O 7 1 i V ! Q 7 V ] ° © f E 1 i V

! Q D E # E E P

yiin = 0 ∀i ∈ Ic, i ∈ I, n ∈ N (3.18) yiin = 0 ∀i ∈ Ic, i ∈ I, n ∈ N (3.19)

54 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

3.7

7 0 1  

(Objective Function)

8 Q R Z [ \ @ p K = M   ! E > ? < š Ì (3.24) :  :

3.7 = J K ² (Objective Function) 55

56 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

3.8

¨ ©  4 5 ~ 6 Œ 

-

 5 6  7   4 ‹ 7   

3.8.1

: ! " 

3 4  F _ E l m < ˜ §  V Generalized Algebraic Modeling System(GAMS, Brooke et al., 1988)<  z { < 4  z { K L M l m E { m  (solver) F

< ² V E MINLP solverp BARONP

3.8.2

¨ m $ % § & ' ¯ ( F

-

n G

3.1

* 3.4 1 i V ! Q ; < I 6

Unit [Qmini , Qmaxi ] Cic,maxin Cic,maxout tstin tendin Micload (ton) (kg salt/ton water) (h) (h) (kg)

A [0, 1000] 0 0.1 0 3 100

B [0, 280] 0.25 0.51 0 4 72.8

C [300, 400] 0.1 0.1 4 5.5 0

D [0, 280] 0.25 0.51 2 6 72.8

E [300, 400] 0.1 0.1 6 7.5 0

F [0, 500] 0 0.1 0 7.5 187.5

[0, 350] 0.1 0.25 0 7.5 187.5

[0, 200] 0.25 0.51 0 7.5 187.5

8 Q R + p 7 - L R  7 1 i V ! Q (A-E)k  Majozi(2005)?  Q

R # O 7 1 i V ! Q (F) E ; < Á  - Ò 3.4 S } < ¼ „ Q G > E

Š ) ?  Z {  = 9 G > h S ) * E K  G  < c   ^ E ; < 0

 < ¡ L M E ³ / ? ? P   + p  k 5  o 2 # O 7 1 i V !

Q < © ¬ ´  \ V W G > h S ) * E K  G  < G 4 ® 5 !  E

57

58 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

59

60 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

61

200 100 166.7 25083.3 200

62 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

63

64 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

65

66 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

) 3.22 Q 5 ; < Z " ! ? n M  > h G  -(Cfc,maxin = 0.25), (Cfc,maxout = 0.51)

0 2 4 6 Time (h)

3 5.5 7.5

100 300 500 700 900

0.1 0.3 0 (kgsalt/kgwater) 1100

Storage

(kg) Level

Conc.

575

Q A9 B9 D .  V $ ! < Q C9 E  V  ´ Q A  .

 E ! ! < Q F B — F G 0   V   ! 9 F G  V 

E  ! P 4 Ä 3.22 p  " ! ? n M E 3 e < -  S } “

  = p 575kgP

3. Q R  Q 2 c ; <

‘  6  Q 2 c ; < E ^ } š Ä 3.23 <   !  V ? - p

1000kg< Q ? & Q A V   ! < © f E Q .  V Q A 

—  E 2 c ! < - — Q A G ‘  E ! ? - « < J p

E  = '  Z - p 813kg Ä 3.24 P

K  < Ò 3.5 p 3 4 + p 3.1 E Š ^ <  S ? M   ! E >

? '  E ‘ ? C V C <  2 c ; < E Á  Z  ] - « P 4  

1 i V ! Q F — (Cmaxin = 0.1)< (Cmaxout = 0.25) 0 < j p  R p º

 Q R p 0 S x 5 - «   ! E > ? < š }  1 i V ! Q F

— (Cmaxin = 0)< (Cmaxout = 0.1)0 < - — F ? ]  V   ! < J  j p

67 121.95 61 61 91.46 30.5

91.46

68 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

* 3.5 + p 3.1 E Š ^

(Cmaxin )F Operation mode Single operation Cyclic operation

(Cmaxout)F Storage tank 0 1 2

0 Freshwater (kg) 3760.5 3017.8 2875

-0.1 Ratio (%) 100 80 76.5

-Tank size (kg) (base) 300 300 -0.1 Freshwater (kg) 2635.5 1513.6 1330 1150

0.25 Ratio (%) 100 61.3 48.9 43.6

Tank size (kg) (base) 1000 998 720,280 0.25 Freshwater (kg) 2253 1432.5 1000

-0.51 Ratio (%) 100 63.6 44.4

-Tank size (kg) (base) 575 813

-3.8.3

¨ m $ % § & ' ¯ ( F

-

n G

3.2

8 > R + p B 7 k  Wang 1995E o R  7 1 i V ! Q (Q 1-3)

 Q R # O 7 1 i V ! Q (Q 4)< © ; < Á  ’ — Ò 3.6 6 a S }

“ Q G > E Š ) ?  Z {  = 9 G > h S ) * E K  G  < c  

^ E ; < 0  < ¡ L M E ³ / ? ? P   + p  5  E ! 

r % p o 2 < C  9 Q R  Q Q 5 ; < 9 Q R  Q 2 c

; < = ? Z p ^ }  ,  5  7

69

* 3.6 1 i V ! Q ; < I 6

Unit [Qmini , Qmaxi ] Cic,maxin Cic,maxout tstin tendin Micload (ton) (kg salt/ton water) (h) (h) (kg)

1 [0, 100] 0.1 0.4 0.5 1.5 30

70 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

71

72 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

3.8.4

# $ % § & ' ¯ ( F

-

n G

3.3

 + p 3.3 a <  5  E 7 Q R  E !  : R < k 9 ½ : =

E  R + p  Q R I t y -  R  E ¡ 5 = : < ?   = E 

 ! > ? < n - — I E 2 c 0 7 7.5hr 4 II B 7 1.5hr< J

  Q R 2 c " II ; < 5 @ p L 5 < 4  R " E 1 i V ! Q

; < Á  š Ò 3.7 P

* 3.7 1 i V ! Q ; < I 6

Plant Unit [Qmini , Qmaxi ] Cic,maxin Cic,maxout tstin tendin Micload (ton) (kg salt/ton water) (h) (h) (kg)

I A [0, 1000] 0 0.1 0 3 100

B [0, 280] 0.25 0.51 0 4 72.8

C [300, 400] 0.1 0.1 4 5.5 0

D [0, 280] 0.25 0.51 2 6 72.8

E [300, 400] 0.1 0.1 6 7.5 0

F [0, 350] 0.1 0.25 0 7.5 187.5

II 1 [0, 100] 0.1 0.4 0.5 1.5 30

2 [0, 40] 0 0.2 0 0.5 8

3 [0, 25] 0.1 0.2 0.5 1 25

4 [0, 85] 0 0.1 0 1.5 25.5

- Ä 3.30 } “ Iy -  E I t  <   ! > ? - p 1000(ton)<

 9 ½ E + p a B p 1330(ton) Z 1 o 25%  ! ? < m I  S ? M

? \ Q A  V   ! < 4 © f E Q  V E . p p " E  !

< - — Q C9 E V  E ! - — ¹ p  { < J  0  x   V

6 < 4 p 1E  = B - Ä 3.31 } “ p 956(ton) P

73

74 y z { | } ~    … œ † † -‡ |  ˆ ‰ ° œ Œ  < =

4

N  O & ' ( )

4.1

*

 Ÿ d   < - — ! “ o 1 R  R  ?  c £ $ + B h , -  ! <

 ‘ V ! i ™ a 4 — ! \ Î  V E  m d . 9 6 * < 4  * E 2

² 4 — !  K L M E N O Ç \ * E   ® 5 P

1 2 3 4 " E 1 i V ! Q ? # O 7 K ?  7 Q p %  2 3

Y < = > ? @ A B C D E F 7 G H I J K L M E N O P ' 9   !

 : R " ¬ Q : \ S ] E a v # E < G 4 = > ` ^ _ <   ` ^ _

d e f g B h F i 7 P ¼ „ ) ?  =  > ?  = <  ? Ô _ 6 { n 7

< x  3 4 K =   ! E > ?  K =  E  =  R V W E Z

[ < k  !  K L M E N O l m < # n o p Q R q r E s t I @ u

v w B C (MINLP)@ A l m < x y /  z { < K ~ S | } !  E K L

M N O P  Q K L M N O < ¼ „ !  : R E Ô _ ?  ¬ Q a v

75

76 S ¥ · 0 1 ¸ 2

# E E 3 e Z P

 < ( 2 ² < º ¹ < < (  !  E   F  ~ 3 4 V ! Q ¸

p  7 N # O 7 Q = 4 1  2 B ® 5  " \  7  # O 7 Q

E !  N O < I - U 7 ` ^ _ E  , < = > Q  5 4  I E @ A U

7 P 3 4 : = f _ E @ A U 7  N O 4  <   2 a = >  R ? \ U

6 w E + p <  8 > F 5  ? # O 7 1 i V ! Q p % E !  : R

< ' 9 k : \ E  7 Q * p # O 7 ; < (  !  ^ _ E K L M O

 K =   ! > ? < 4  ( O   7 1 i O V  E  ) ? 

 = =  8 o F B 5  ?  7 1 i V ! Q p % E !  : R < k #

O 7 V ! Q  p R  7 V ! Q < 4 0  E  7    7

V ! Q E ; < 0 4 , < a <  E I t ( O  K =   ! >

? ?  K =   = P - ?  E 3 £ U | ^ }  , S ? } “ < a <

1  : f _ E @ A U 7  N O 4  < ~ ] o ± E { „ V W E Z [ ¡

z  !  N O l m <  Q = : K = E !  N O Ô _ P

4.2

3 4 ¹ 5

4 — 1  : f g E @ A U 7 4 š < Z ½ I  ] O { „ : = > E 

R l m < § 4 < p 1 ]   E  ? : \ E l m <  @ A U 7 f _ 0 <

 V u v w (Non-Linear) E { n 7  6  © d l 4 m <  Q  ) ?  Z {  a v E º · { n 7 a <  V 0 − 1n @  6  \ N C E K # <  D

t  u v w E Z [ \ @ <  } I R @ A U 7 e o Q R s t I @ u v w

B C (MINLP)l m P 4  z { MINLPl m E < i a < ! ! ” } * V

4.2 0 1 ¸ 2 77

W E  { (Local solution)< 4 V @ u } ¸  { (Global solution)= '  <

š É \ Î E z } ¹  r Q ‡ ˆ E   w ‘ !  N O 6 ¸  { < 7

_ } N O ® 5 E l m P

  < 1  % 7 = ? # O 7 N  7 Q p % 0 E l m < 4 —

  R Q E @ Z p 5 Ÿ 0 <  ¥ \ 5  ©  V E F D < ' p v

w * l m  E V W ( 7 Q  # O 7 Q E s < ; < 0  E D

t )4 \ : V W { „ F D < Q  8 o F : = E ?  7 Q p % E l m

<  ¥ \  I ! ! @ l Q ?  c £ > .  E { n <  ^ _ a P

" (Inner) ?  (Central) E ! ! @ l Q < G 4 ® 5   Š o 1

E K = M (Total annualized cost)?  K L M E !  ^ _ <  F G E U 7 J ! < \ p C  ¸ t E ‘ < P

78 S ¥ · 0 1 ¸ 2

% & ' (

[1] Bagajewicz M. A review of recent design procedures for water networks in refineries and process plants. Computers and Chemical Engineering, 24:2093–2113, 2000.

[2] Bandyopadhyay, S.; Ghanekar, M. D.; Pillai, H. K. Process water management. Ind.

Eng. Chem. Res., 45(15):5287–5297, 2006.

[3] Chen C.-L.,Hung S.-W. and Lee J.-Y. Design of inter-plant water network with cen-tral and decencen-tralized water mains. Computers and Chemical Engineering, 34:1522–

1531, 2010.

[4] Cheng, K.-F.; Chang, C.-T. Integrated water network designs for batch processes.

Ind. Eng. Chem. Res., 46:1241–1253, 2007.

[5] Chew, I. M. L.; Foo, D. C. Y. Automated targeting for inter-plant water integration.

Chem. Eng. J., 153(1-3):23–36, 2009.

[6] Chew, I. M. L.; Tan, R., Ng, D. K. S.; Foo, D. C. Y.; Majozi, T.; Gouwws, J.

Synthesis of direct and indirect interplant water network. Ind. Eng. Chem. Res., 47(23):9485–9496, 2008.

[7] Feng, X.; Seider, W. D. New structure and design methodology for water networks.

Ind. Eng. Chem. Res, 40(26):6140–6146, 2001.

[8] Foo, D. C. Y.; Manan, Z. A.; Tan, Y. L. Synthesis of maximum water recovery network for batch process systems. J. Clean. Prod., 13:1381–1394, 2005.

[9] Gouws, J. F.; Majozi, T.; Foo, D. C. Y.; Chen, C.-L.; Lee, J.-Y. Water minimization techniques for batch processes. Ind. Eng. Chem. Res., 49:8877–8893, 2010.

[10] Gunarantam, M., Alva-Argaez, A., Kokossis, A., Kim, J-K, and Smith, R. Auto-mated design of total water systems. Ind. Eng. Chem. Res., 44:588, 2005.

[11] Gunaratnam, M.; Alva-Argaez, A., Kokossis, A., Kim, J. K.; Smith, R. Automated design of total water systems. Ind. Eng. Chem. Res., 44(3):588–599, 2005.

[12] Halim.l and Srinivasan R. Sequential methodology for simultaneous batch pro-cess scheduling and waste reuse optimization. Chemical Engineering Transactions, 21:727–732, 2010.

79

80 ¹ 6 { |

[13] Kim, J. K.; Smith, R. Automated design of discontinuous water systems. Trans.

IChemE., 82(3):238–248, 2004.

[14] Kuo, W. C. J.; Smith R. Design of water-using systems involving regeneration.

Trans. IChemE., 76(2):94–114, 1998.

[15] Li, B.-H.; Chang, C.-T. A mathematical programming model for discontinuous water-reuse ststem design. Ind. Eng. Chem. Res, 45:5027–5036, 2006.

[16] Liao, Z. W.; Wu, J. T.; Jiang, B. B.; Wang, J. D.; Yang, Y. R. Design methodology for flexible multiple plant water networks. Ind. Eng. Chem. Res., 46(14):4954–4963, 2008.

[17] Lovelady, E. M.; El-Halwagi, M. M. Design and integration of eco-industrial parks for managing water resources. Env. Progress Sustainable Energy, 28(21):265–272, 2009.

[18] Lovelady, E. M.; El-Halwagi, M. M. and Krishnagopalan,G.A. An integrated ap-proach to the optimization of water usage and discharge in pulp and paper plants.

International Journal of Environment and Pollution, 29:274–307, 2007.

[19] C.J.; Buckley C. A. Majozi, T.; Brouckaert. A graphical technique for wastewater minimisation in batch processes. J. Environ Manage, 78:317–329, 2006.

[20] Majozi, T. Wastewater minimisation using central reusable water storage in batch plants. Computers and Chemical Engineering, 29:1631, 2005.

[21] Majozi, T. and Zhu, X. X. A novel continuous time milp gprmilation for multipur-pose batch plants. 1. short-term scheduling. Industrian and Engineering Chemistry Research, 40(25):5935, 2001.

[22] Manan, Z. A.; Tan, Y. L.; Foo, D. C. Y. Targeting the minimum water flowrate using water cascade analysis technique. AIChE J., 50(12):3169–3183, 2004.

[23] Ng, D. K. S.; Foo, D. C. Y.; Tan, Y. L.; Tan, R. R. Ultimate flow rate targeting with regeneration placement. Trans. IChemE., 85(9):1253–1267, 2007.

[24] Olesen, S. G.; Polley, G. T. Dealing with plant geography and piping constraints in water network design. Trans. IChemE., 74(4):273–276, 1996.

[25] Takama, N., Kuriyama,T., Shiroko, K. and Umeda, T. Optimal water allocation in a petroleum refinery. Comp. Chem. Eng., 4:251, 1980.

[26] Wang, Y. and Smith, R. Design of distributed effluent treatment system. Chem. Eng.

Sci., 49:3127, 1994.

[27] Wang, Y. and Smith, R. Wastewater minimization. Chem. Eng. Sci., 49:981, 1994.

¹ 6 { | 81

[28] Wang, Y. P.; R. Smith. Wastewater minimization with flowrate constraints. Chem.

Eng. Res. Des. ( Trans. IChemE.), 73:889–904, 1995.

[29] Zheng, X.; Feng, X.; Shen, R.; Seider, W. D. Design of optimal water-using net-works with internal water mains. Ind. Eng. Chem. REs., 45(25):8413–8420, 2006.

[30] Zhu, X. X. and Majozi, T. A novel continuous time milp gprmilation for multipur-pose batch plants. 2. integrated. Industrian and Engineering Chemistry Research, 40(23):5621, 2001.

相關文件