209808994-Energie-si-Mediu-Proiect-Dinca.pdf

N := 11

Ngr := 11

Compozitia elementara a carbunelui si gazului natural: Lignit c := 0.4 + 0.002 ⋅ N = 0.422 h := 0.06 − 0.001 2⋅ N = 0.0468 n2 := 0.02 − 0.000 3⋅ N = 0.0167 o2 := 0.015 − 0.000 2⋅ N = 0.0128 s := 0.015 + 0.001 5⋅ N = 0.0315 w := 0.15 + 0.002 ⋅ N = 0.172 A := 1 − c − h − n2 − o2 − s − w = 0.2982

Gaz natural: ch4 := 0.8 + 0.000 4⋅ N = 0.8044 c2h6 := 0.023 + 0.000 2⋅ N = 0.0252 c3h8 := 0.033 + 0.000 3⋅ N = 0.0363 c4h10 := 0.032 + 0.000 2⋅ N = 0.0342 c5h12 := 0.03 + 0.000 5⋅ N = 0.0355

−3

h2s := 0.007 − 0.00003⋅ N = 6.67 × 10

co2 := 1 − ch4 − c2h6 − c3h8 − c4h10 − c5h12 − h2s = 0.05773

Numarul consumatorilor: 4

Npers := 2000 + 450 ⋅ N + 650⋅ Ngr = 1.41 × 10

Energia Energia electrica electric a consumata de o persoana: Epers := 4.5

MWh an⋅ om

Energia anuala: 4

Ean Ean := Nper Nperss⋅ Eper Eperss = 6.345 × 10

Durata anuala de functionare 3

a! := 8500 − 150⋅ N − 125⋅ Ngr = 5.475 × 10

Durata de viata " := 1

an

Distanta de transport pentru carbune #c := 250 + 10⋅ N = 360 1

3

#gn := 1700 + 25⋅ N = 1.975 × 10

Puterea calorifica inferioara inferioara $ar%&ne 4

'$(c := ) 81.3⋅ c + 243 ⋅ h + 15n2 + 45.6⋅ s − 25.3⋅ o2 − 6 ⋅ w* ⋅ 418.68 = 1.92 1.9264 6433 33 × 10

Gaz natural ch4⋅ 16 + c2h6⋅ 30 + c3h8⋅ 44 + c4h10⋅ 58 + c5h12⋅ 72 + h2s⋅ 34 + co2⋅ 44 = 1.00518 ρgn := 22.414 '$(c '$(ch4 h4 := 3576 35764 4 '$(c '$(c2h 2h6 6 := 6367 63670 0

+,

'$(c '$(c3h 3h8 8 := 9113 91138 8

(m3) N

'$(c '$(c4h 4h10 10 := 1185 118500 00 '$(c '$(c5h 5h12 12 := 1459 145900 00 '$(h2s (h2s := 2335 23354 4

4

'$(g '$(gn1 n1 := ch4 ch4⋅ '$(c '$(ch4 h4 + c2h6⋅ '$(c2h6 + c3h8⋅ '$(c3h8 = 3.36 3.3681 8136 36 × 10

3

'$(g '$(gn2 n2 := c4h1 c4h10 0⋅ '$(c '$(c4h 4h10 10 + c5h12⋅ '$(c5h12 + h2s⋅ '$(h2s = 9.38 9.3879 7921 21 × 10

4

'$(gn (gn := '$(gn (gn1 + '$(gn2 (gn2 = 4.30 4.3069 6928 28 × 10

'$(gn 4 '$(gnn := 4.2847 4734 34 × 10 = 4.28 ρgn

+,

(m3) N

+, +g

Eficienteleproceselor pe durata ciclului de viata Procesul de extractie

ηe-c := 0.9 − 0.004 ⋅ N = 0.856 ηe-gn := 0.91 + 0.002 ⋅ N = 0.932 Procesul de tratare

ηtrc := 0.85 + 0.003 ⋅ N = 0.883 ηtrgn := 0.88 + 0.002 ⋅ N = 0.902 Procesul de t ransport ransport

ηtpc := 0.9 − 0.006 ⋅ N = 0.834 ηtpgn := 0.85 + 0.003 ⋅ N = 0.883 Procesul de combustie 2

ηc1c := 0.42 − 0.002 ⋅ N = 0.398 ηc2c := 0.45 − 0.003 ⋅ N = 0.417 ηcgn := 0.5 + 0.005 ⋅ N = 0.555 Determinarea Determinarea cantitatii de c ombustibil neces ara in cadrul fiecarei etape si filiere energetice energetice Filiera de carbune ardere pulverizata! 6

Ean⋅ 3.6⋅ 10

Mac :=

ηc1c⋅ '$(c

Matp :=

Mac

ηtpc

7

2.9791 9183 83 × 10 = 2.97

7

3.5721 2162 62 × 10 = 3.57

Matp 7 Matr := 4.0454 5483 83 × 10 = 4.04 ηtrc Matr 7 Mae- := 4.7260 6032 32 × 10 = 4.72 ηe-c

Filiera de gaz natural

M%c :=

M%tp :=

Ean⋅ 3.6⋅ 10

6

ηcgn⋅'$(gnn M%c

ηtpgn

6

9.6054 5441 41 × 10 = 9.60

7

1.0878 7819 19 × 10 = 1.08

M%tp 7 = 1.20 M%tr := 1.2060 6008 08 × 10 ηtrgn M%tr 7 M%e- := = 1.294 × 10 ηe-gn

Filiera de carbune ardere in pat fluidizat!

6

Mcc :=

Mctp :=

Ean⋅ 3.6⋅ 10

ηc2c⋅'$(c Mcc

ηtpc

7

2.8434 3441 41 × 10 = 2.84

7

3.4094 9401 01 × 10 = 3.40

Mctp 7 Mctr := 3.8611 1157 57 × 10 = 3.86 ηtrc Mctr 7 Mce- := 4.5106 0697 97 × 10 = 4.51 ηe-c

"

Emisii le specifice pentru fiecare filiera energetica energetica si etapa etapa

Filiera de carbune Etapa de extractie N3e-$ := 0.0494 + 0.0003 ⋅ N = 0.0527 $/2e-$ := 3.643 + 0.08 ⋅ N = 4.523 $/e-$ := ) 0.00381 + 0.0002⋅ N* = 6.01 × 10

−3 −9

$Le $Le-$ -$ := 0.00 0.0000 0000 0000 0013 131 1 + 0.00 0.0000 0000 0000 0000 005 5⋅ N = 1.86 × 10

−9

ee-$ $ := 0.00 0.0000 0000 0000 0024 243 3 + 0.00 0.0000 0000 0000 0000 003 3⋅ N = 2.76 × 10

2e 2e-$ -$ := 0.00 0.0000 0000 0000 0010 103 3 + 0.00 0.0000 0000 0000 0000 003 3⋅ N = 1.36 × 10

−9

$4e-$ 4e-$ := 0.63 0.6391 91 + 0.00 0.006 6 ⋅ N = 0.7051 N/-e-$ := 0.0191 + 0.0007 ⋅ N = 0.0268

−4

N2/e-$ := 0.000316 + 0.0000138⋅ N = 4.678 × 10 're-$ e-$ := 0.007 .00789 89 + 0.00 0.0004 045 5 ⋅ N = 0.01284 /2e-$ 2e-$ := 0.04 0.0412 12 + 0.00 0.002 2 ⋅ N = 0.0632

Etapa de tratare

N3tr$ := ) 0.0245 + 0.0003⋅ N* = 0.0278 $/2tr$ := 3.74 + 0.08 ⋅ N = 4.62

−3

$/tr$ tr$ := 0.00 0.0032 322 2 + 0.00 0.0002 02⋅ N = 5.42 × 10

−9

$Lt $Ltr$ r$ := 0.00 0.0000 0000 0000 0030 305 5 + 0.00 0.0000 0000 0000 0000 005 5⋅ N = 3.6 × 10

−9

tr tr$ $ := 0.00 0.0000 0000 0000 0052 526 6 + 0.00 0.0000 0000 0000 0000 003 3⋅ N = 5.59 × 10

2t 2tr$ r$ := 0.00 0.0000 0000 0000 0011 112 2 + 0.00 0.0000 0000 0000 0000 003 3⋅ N = 1.45 × 10

−9

−3

$4tr 4tr$ := 0.00 0.0073 738 8 + 0.00 0.0000 006 6 ⋅ N = 8.04 × 10 N/-tr$ := 0.0173 + 0.0007 ⋅ N = 0.025

−4

N2/tr$ := 0.000466 + 0.000045⋅ N = 9.61 × 10

−3

'rtr 'rtr$ $ := 0.00 0.0015 153 3 + 0.00 0.0000 0045 45⋅ N = 2.025 × 10 /2tr$ 2tr$ := 0.01 0.0112 12 + 0.000 .0005 5⋅ N = 0.0167

Etapa de t ransport: ransport: #c = 360 N3tp$ := )0.000000221 + 0.0003⋅ N* ⋅ #c = 1.18808 #

$/2tp$ := ) 0.039 + 0.0004⋅ N* ⋅ #c = 15.624 $/tp$ := ) 0.00322 + 0.0002⋅ N* ⋅ #c = 1.9512

−7

$Lt $Ltp$ p$ := )0.00 0.0000 0000 0000 0003 0305 05 + 0.00 0.0000 0000 0000 0000 005 5⋅ N* ⋅ #c = 3.078 × 10

tp tp$ $ := ) 0.00 0.0000 0000 0000 0000 0016 164 4 + 0.00 0.0000 0000 0000 0000 0000 003 3⋅ N* ⋅ #c = 7.092 × 10

−9 −9

2t 2tp$ p$ := ) 0.00 0.0000 0000 0000 0000 0000 0015 154 4 + 0.00 0.0000 0000 0000 0000 0000 003 3⋅ N* ⋅ #c = 1.24 1.2434 344 4 × 10

−4

$4t $4tp$ p$ := ) 0.00 0.0000 0002 0204 04 + 0.00 0.0000 0000 0006 06⋅ N* ⋅ #c = 9.72 × 10 N/-tp$ := )0.000413 + 0.000007⋅ N* ⋅ #c = 0.1764

−4

N2/tp$ := )0.00000055 + 0.0000000138⋅ N* ⋅ #c = 2.52 2.5264 648 8 × 10 'rtp 'rtp$ $ := )0.00 0.0000 0041 412 2 + 0.00 0.0000 0000 0045 45⋅ N* ⋅ #c = 0.016614 /2tp$ 2tp$ := ) 0.000 .00021 213 3 + 0.00 0.0000 0005 05⋅ N* ⋅ #c = 0.09648

Etapa de Combustie:

−4

N3c$ := 0.000121 + 0.000008⋅ N = 2.09 × 10 $/c$ := ) 0.1737 + 0.002⋅ N* = 0.1957

c$ := ) 0.00 0.0000 0040 407 7 + 0.00 0.0000 000 003⋅ N* = 4.4 × 10

−5

$Lc $Lc$ $ := )0.00 0.0000 0001 0196 96 + 0.00 0.0000 0000 0005 05⋅ N* = 2.51 × 10

−6

c$ c$ := )0.00 0.0000 0000 0016 1699 99 + 0.00 0.0000 0000 0000 003 3⋅ N* = 2.029 × 10

−7

2c 2c$ $ := ) 0.00 0.0000 0000 0000 0098 989 9 + 0.00 0.0000 0000 0000 0000 003 3⋅ N* = 1.022 × 10

−8

$4c$ := ) 0.00943 + 0.00006⋅ N* = 0.01009 N2/c$ := )0.00353 + 0.000138⋅ N* = 5.048 × 10

−3

F$%$E&' DE G'( N')*&'% E-tractie $66e 66e- -N N := 0.0 0.044 + 0.000 .0005 5⋅ N = 0.0495 $/2e /2e-N -N := 76. 76.52 + 0.08 0.08 ⋅ N = 77.4 $/e- /e-N N := 0.06 0.0624 24 + 0.00 0.002 2 ⋅ N = 0.0844 $4e 4e-N -N := 3.80 3.801 1 + 0.02 0.02 ⋅ N = 4.021 N/e-N := 0.372 + 0.007 ⋅ N = 0.449

−4

N2/e-N := 0.000625 + 0.000018⋅ N = 8.23 × 10 'rere-N := 0.04 0.0451 51 + 0.00 0.0007 075 5 ⋅ N = 0.05335 /2e- 2e-N N := 0.14 0.144 4 + 0.00 0.002 2 ⋅ N = 0.166

ratare

$66t 66trrN := 0.22 0.224 4 + 0.00 0.005 5 ⋅ N = 0.279 +

$/2trN := 22 + 0.4⋅ N = 26.4 $/trN trN := 0.07 0.0718 18 + 0.00 0.003 3 ⋅ N = 0.1048 $4trN := 2.82 + 0.08 ⋅ N = 3.7 N/trN := 0.171 + 0.007 ⋅ N = 0.248 N2/trN := 0.00036 + 0.000018⋅ N = 5.58 × 10

−4

'rtrN trN := 0.02 0.02 + 0.00 0.0007 075 5 ⋅ N = 0.02825 /2tr 2trN N := 1.02 1.02 + 0.00 0.002 2 ⋅ N = 1.042 ransport

−3

$66 $66tp tpN N := ) 0.00 0.0000 0002 0219 19 + 0.00 0.0000 0000 0005 05⋅ N* ⋅ #gn = 5.41 5.4115 15 × 10 $/2tpN := ) 0.306 + 0.004⋅ N* ⋅ #gn = 691.25 $/tp /tpN N := ) 0.00 0.0026 269 9 + 0.00 0.0000 003 3 ⋅ N* ⋅ #gn = 5.9645 $4t 4tpN pN := ) 0.00 0.0072 724 4 + 0.00 0.0000 008 8⋅ N* ⋅ #gn = 16.037 N/-tpN := ) 0.00245 + 0.00007 ⋅ N* ⋅ #gn = 6.3595 N2/tpN := ) 0.00003879 + 0.00000018⋅ N* ⋅ #gn = 0.080521 'rtp 'rtpN N := ) 0.00 0.0000 0038 3879 79 + 0.00 0.0000 0000 0018 18⋅ N* ⋅ #gn = 0.080521 /2tp 2tpN N := ) 0.00 0.0002 0268 68 + 0.00 0.0000 002 2 ⋅ N* ⋅ #gn = 0.9638

$om%&stie N3cN := 0.137 + 0.004 ⋅ N = 0.181 $66 66cN cN := 0.04 0.0496 96 + 0.00 0.0005 05 ⋅ N = 0.0551 $/cN := 0.174 + 0.003 ⋅ N = 0.207 $2/ 2/cN cN := 0.05 0.056 6 + 0.00 0.0004 04 ⋅ N = 0.0604 $4cN := 2.212 + 0.09 ⋅ N = 3.202

Filiera de carbune 'rdere in pat fluidizat circulant!

$om%&stie

−3

$/c% /c% := 0.00 0.0039 395 5 + 0.00 0.0000 002 2⋅ N = 4.17 × 10

$Lc% $Lc% := 0.00 0.0039 395 5 + 0.00 0.0000 002 2 ⋅ N = 4.17 × 10

−3

c% c% := 0.00 0.0000 0000 0011 117 7 + 0.00 0.0000 0000 0000 003 3⋅ N = 1.5 × 10

−7 −9

2c 2c% % := 0.00 0.0000 0000 0000 0064 646 6 + 0.00 0.0000 0000 0000 0000 003 3⋅ N = 6.79 × 10

−4

$4c $4c% % := 0.00 0.0002 0269 69 + 0.00 0.0000 0006 06⋅ N = 3.35 × 10

−4

N2/c% := 0.000139 + 0.000008⋅ N = 2.27 × 10

,

Recalcularea Recalcularea emisii lor specifice

Filiera de carbune Etapa de extractie 7

Mae- = 4.726 × 10

6

N3e-$rec := N3e-$⋅ Mae- = 2.49 2.4906 062 2 × 10

g g

8

$/2e-$ $/2e-$rec rec := $/2e$/2e-$ $⋅ MaeMae- = 2.13 2.1375 758 8 × 10 5

$/e$/e-$r $rec ec := $/e$/e-$ $⋅ MaeMae- = 2.84 2.8403 035 5 × 10

g

$Le-$ $Le-$rec rec := $Le-$ $Le-$⋅ MaeMae - = 0.0879

g

ee-$r $rec ec := ee-$ $⋅ MaeMae = 0.13044

g

2e 2e-$ -$re recc := 2e 2e-$ -$⋅ MaeMae = 0.06427

g 7

$4e-$ $4e-$rec rec := $4e$4e-$ $⋅ MaeMae- = 3.33 3.3323 233 3 × 10

6

N/-e-$rec := N/-e-$⋅ Mae- = 1.26 1.2665 658 8 × 10

g g

4

N2/e-$rec := N2/e-$⋅ Mae- = 2.21 2.2108 084 4 × 10 5

're're-$r $rec ec := 're're-$ $⋅ MaeMae- = 6.06 6.0682 822 2 × 10

g g

6

/2e /2e-$ -$re recc := /2e /2e-$ -$⋅ MaeMae- = 2.98 2.9868 685 5 × 10

g

Etapa de tratare 7

Matr Matr = 4.04 4.0454 5483 83 × 10

g

6

N3tr$rec := ) N3tr$⋅Matr * = 1.12464 × 10

g

8

$/2tr$ $/2tr$rec rec := $/2tr $/2tr$ $⋅Matr Matr = 1.869 × 10

$/tr $/tr$r $rec ec := $/tr $/tr$ $ ⋅Matr Matr = 2.19 2.1926 265 5 × 10

g

$Ltr$ $Ltr$rec rec := $Ltr$ $Ltr$⋅Matr Mat r = 0.14564

g

tr tr$r $rec ec := tr tr$ $⋅Matr Matr = 0.22614

g

2t 2tr$ r$re recc := 2t 2tr$ r$⋅Matr Matr = 0.05866

g

5

5

$4tr$ $4tr$rec rec := $4tr $4tr$ $⋅Matr Matr = 3.25 3.2525 257 7 × 10 10

6

N/-tr$rec := N/-tr$⋅ Matr = 1.01 1.0113 137 7 × 10 10

4

N2/tr$rec := N2/tr$⋅ Matr = 3.88 3.8877 771 1 × 10 10

g g g g

4

'rtr 'rtr$r $rec ec := 'rtr 'rtr$ $⋅Matr Matr = 8.19 8.1921 21 × 10

5

/2t /2tr$ r$re recc := /2t /2tr$ r$⋅Matr Matr = 6.75 6.7559 596 6 × 10 10

g

Etapa de t ransport: ransport:

-

#c = 360 7

Matp = 3.572162 × 10

10

N3tp$rec := N3tp$⋅Matp ⋅ #c = 1.52 1.5278 784 4 × 10

g g

11

$/2t $/2tp$ p$re recc := $/2t $/2tp$ p$⋅ #c ⋅ Matp = 2.00 2.0092 921 1 × 10 10 10

$/tp $/tp$r $rec ec := $/tp $/tp$ $⋅#c ⋅ Matp = 2.50 2.509 92 × 10

g 3

$Lt $Ltp$ p$re recc := $Lt $Ltp$ p$⋅#c ⋅ Matp = 3.95 3.9582 824 4 × 10 10

g

tp tp$r $rec ec := tp tp$ $⋅ #c ⋅ Matp = 91.20158

g

2t 2tp$ p$re recc := 2t 2tp$ p$⋅ #c ⋅ Matp = 15.99037

g 7

$4t $4tp$ p$re recc := $4t $4tp$ p$⋅ #c ⋅ Matp = 1.24 1.2499 997 7 × 10 10

g

9

N/-tp$rec := N/-tp$⋅#c ⋅ Matp = 2.26 2.2684 847 7 × 10 10 N2/tp$rec := N2/tp$⋅Matp ⋅ #c = 3.249 × 10

g

6

g g

8

'rtp$ tp$rec rec := ) 'rtp$ tp$ * ⋅ # c⋅Matp = 2.13 2.1365 652 2 × 10 10

g

9

/2t /2tp$ p$re recc := /2t /2tp$ p$⋅ #c ⋅ Matp = 1.24 1.2407 071 1 × 10 10

F$%$E&' DE G'( N')*&'% E-tractie 7

M%e- = 1.294 × 10

g

5

$66e$66e-N Nrec rec := $66e$66e-N N⋅ M%eM%e- = 6.405 .4053 3 × 10

g

9

$/2e$/2e-N Nrec rec := $/2e- $/2e-N N⋅ M%eM%e- = 1.00 1.0015 156 6 × 10 6

$/e-N $/e-Nrec rec := $/e- $/e-N N⋅ M%eM%e- = 1.09 1.0921 214 4 × 10

g

7

$4e$4e-N Nrec rec := $4e- $4e-N N⋅ M%eM%e- = 5.20 5.2031 317 7 × 10 6

N/e-Nrec := N/e-N⋅M%e- = 5.81 5.810 006 × 10

g g

4

N2/e-Nrec := N2/e-N⋅M%e- = 1.06 1.0649 496 6 × 10

g g

5

're- 're-Nre Nrecc := 're-N 're-N⋅ M%eM%e- = 6.90 6.9034 349 9 × 10

6

/2e/2e-N Nrec rec := /2e/2e-N N⋅ M%eM%e- = 2.14 2.1480 804 4 × 10

g

ratare

.

7

M%t M%tr = 1.20 1.2060 6008 08 × 10

g

6

$66tr $66trN Nrec rec := $66tr $66trN N⋅ M%tr M%tr = 3.36 3.3647 476 6 × 10 10

g

8

$/2tr $/2trNre Nrecc := $/2tr $/2trN N⋅ M%tr M%tr = 3.18 3.1838 386 6 × 10 10 6

$/trN $/trNrec rec := $/trN $/trN⋅M%tr M%tr = 1.26 1.2639 39 × 10

g 7

$4tr $4trNre Nrecc := $4tr $4trN N⋅ M%tr M%tr = 4.46 4.4622 223 3 × 10 10

g

6

N/trNrec := N/trN⋅M%tr = 2.99 2.9909 09 × 10

g 3

N2/trNrec := N2/trN⋅M%tr = 6.72 6.7295 952 2 × 10 10

g

5

'rtrN 'rtrNrec rec := 'rtr 'rtrN N⋅M%tr M%tr = 3.40 3.4069 697 7 × 10 10

g 7

/2tr /2trNr Nrec ec := /2tr /2trN N ⋅M%tr M%tr = 1.25 1.2566 666 6 × 10 10

g

ransport 3

#gn = 1.975 × 10

7

M%tp M%tp = 1.08 1.0878 7819 19 × 10

g

8

$66 $66tp tpN Nre recc := ) 0.00 0.0000 0002 0219 19 + 0.00 0.0000 0000 0005 05⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.16 1.1626 263 3 × 10

g

13

$/2t $/2tp pNre Nrecc := ) 0.30 0.306 6 + 0.0 0.004⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.48 1.4851 511 1 × 10

11

$/tp $/tp Nrec rec := ) 0.00 0.0026 269 9 + 0.00 0.0000 003 3⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.28 1.2814 144 4 × 10

g

11

$4t $4tp pNr Nrec ec := ) 0.00 0.0072 724 4 + 0.00 0.0000 008 8 ⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 3.44 3.4454 546 6 × 10

g

11

N/-tpNrec := ) 0.00245 + 0.00007⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.36 1.3663 63 × 10 10

9

g

N2/tpNrec := ) 0.00003879 + 0.00000018⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.72 1.7299 994 4 × 10 9

g

'rtp 'rtpN Nre recc := )0.00 0.0000 0038 3879 79 + 0.00 0.0000 0000 0018 18⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 1.72 1.7299 994 4 × 10 10

g

/2t /2tp pNr Nrec ec := ) 0.00 0.0002 0268 68 + 0.00 0.0000 002 2⋅ N* ⋅ #g n⋅ M%tp⋅ #gn = 2.07 2.0706 067 7 × 10

Filiera de carbune 'rdere in pat fluidizat circulant! Etapa de extractie 7

Mcece- = 4.51 4.5106 0697 97 × 10

6

N3e-$rec3 := N3e-$⋅Mce- = 2.37 2.377 714 × 10

g g

8

$/2e-$ $/2e-$rec rec3 3 := $/2e$/2e-$ $⋅ MceMce- = 2.04 2.0401 019 9 × 10 5

$/e$/e-$r $rec ec3 3 := $/e$/e-$ $⋅ MceMce- = 2.7 2.71093 1093 × 10

g

$Le-$ $Le-$rec rec3 3 := $Le-$ $Le-$⋅ MceMce - = 0.0839

g

ee-$r $rec ec3 3 := ee-$ $⋅ MceMce = 0.1245

g

2e-$ 2e-$rec rec3 3 := 2e-$ 2e-$⋅ MceMce - = 0.06135

g 7

$4e-$ $4e-$rec rec3 3 := $4e$4e-$ $⋅ MceMce- = 3.18 3.1804 049 9 × 10

6

N/-e-$rec3 := N/-e-$⋅Mce- = 1.20 1.208 887 × 10

g g

/

4

N2/e-$rec3 := N2/e-$⋅Mce- = 2.11 2.110 01 × 10

g

5

're're-$r $rec ec3 3 := 're're-$ $⋅ MceMce- = 5.79 5.7917 174 4 × 10

g 6

/2e/2e-$re $rec3 c3 := /2e/2e-$ $⋅ MceMce- = 2.850 .85076 76 × 10

g

Etapa de tratare 7

Mct Mctr = 3.861 .86115 157 7 × 10

g

6

N3tr$rec3 := )N3tr$⋅ Mctr * = 1.0734 × 10

g

8

$/2tr$ $/2tr$rec rec3 3 := $/2tr $/2tr$ $⋅Mctr Mctr = 1.78 1.7838 385 5 × 10 10 $/tr $/tr$r $rec ec3 3 := $/tr $/tr$ $ ⋅ Mctr Mctr = 2.09 2.0927 275 5 × 10 10

g

$Ltr$ $Ltr$rec rec3 3 := $Ltr$ $Ltr$⋅Mctr Mct r = 0.139

g

tr tr$r $rec ec3 3 := tr tr$ $⋅Mctr Mctr = 0.21584

g

2tr$ 2tr$rec rec3 3 := 2tr$ 2tr$⋅ Mctr Mct r = 0.05599

g

5

g

5

$4tr$ $4tr$rec rec3 3 := $4tr $4tr$ $⋅Mctr Mctr = 3.10 3.1043 437 7 × 10 10

g

5

N/-tr$rec3 := N/-tr$⋅ Mctr = 9.65 9.6528 289 9 × 10

4

N2/tr$rec3 := N2/tr$⋅ Mctr = 3.71 3.7105 057 7 × 10

g g

4

'rtr 'rtr$r $rec ec3 3 := 'rtr 'rtr$ $⋅Mctr Mctr = 7.81 7.8188 884 4 × 10 10

g

5

/2tr /2tr$re $rec3 c3 := /2tr /2tr$ $ ⋅ Mctr Mctr = 6.44 6.4481 813 3 × 10

Etapa de t ransport: ransport: 7

Mctp = 3.409401 × 10 #c = 360

10

N3tp$rec3 := N3tp$⋅ Mctp ⋅ #c = 1.45 1.4582 823 3 × 10

g

11

$/2t $/2tp$ p$re rec3 c3 := $/2t $/2tp$ p$⋅ #c ⋅ Mctp = 1.91 1.9176 767 7 × 10

g

10

$/tp $/tp$r $rec ec3 3 := $/tp $/tp$ $⋅ #c ⋅ Mctp = 2.39 2.3948 487 7 × 10 10

g 3

$Lt $Ltp$ p$re rec3 c3 := $Lt $Ltp$ p$⋅ #c ⋅ Mctp = 3.77 3.7778 789 9 × 10 10 tp tp$r $rec ec3 3 := tp tp$ $⋅ #c ⋅ Mctp = 87.04611

g g

2t 2tp$ p$re rec3 c3 := 2t 2tp$ p$⋅ #c ⋅Mctp = 15.26179

g 7

$4t $4tp$ p$re rec3 c3 := $4t $4tp$ p$⋅ #c ⋅ Mctp = 1.19 1.1930 302 2 × 10

g 9

N/-tp$rec3 := N/-tp$⋅ #c ⋅ Mctp = 2.16 2.1651 511 1 × 10 10

g

6

N2/tp$rec3 := N2/tp$⋅ Mctp ⋅ #c = 3.10 3.1009 096 6 × 10

g 8

'rtp 'rtp$r $rec ec3 3 := ) 'rtp 'rtp$ $ * ⋅ # c⋅Mctp = 2.03 2.0391 918 8 × 10 10

g 9

/2t /2tp$ p$re rec3 c3 := /2t /2tp$ p$⋅ #c ⋅Mctp = 1.18 1.1841 418 8 × 10 10

g

10

Etapa 3

Emisia de C2

Filiera de carbune ardere pulverizata! ca :=

+g

Mac

= 1.511508 a! ⋅ 3600 3600

s

7

Mac = 2.979183 × 10 3

a! = 5.475 × 10

co2a := 3.67⋅ c⋅ ca = 2.340933

Filiera de gaz natural Mch4 := 16

Mc2h6 := 3 0

Mc := 12

Mco2 := 44

Mc3h8 := 4 4 Mh2s := 34

Mc4h10 := 58

Mc5h12 := 7 2

Mh := 1

Mo := 16

Ms := 32 32

= 16.7284 Mam1 am1 := ch4⋅ Mch4 Mch4 + c2h6⋅ Mc2h6 + c3h8⋅ Mc3h8 + c4h10⋅ Mc3h8 Mam2 Mam2 := c5h1 c5h12 2⋅ Mc5h Mc5h12 12 + co2⋅ Mco2 + h2s⋅ Mh2s = 5.3229

Mam := Mam1 + Mam 2 = 22.0513

ch4 :=

Mch4⋅ ch4 Mam

Mc2h6⋅ c2h6

c2h6 :=

Mam Mc3h8⋅ c3h8

c3h8 :=

Mam

c4h10 :=

c5h12 :=

co2 :=

h2s :=

= 0.583657 = 0.034284 = 0.072431

Mc4h10⋅ c4h10 Mam Mc5h12⋅ c5h12 Mam

Mco2⋅ co2 Mam Mh2s⋅ h2s Mam

= 0.089954 = 0.115912

= 0.115191

= 0.010284

11

$i :=

i :=

/i :=

i :=

Mc

⋅ ch4 +

Mch4 Mh⋅ 4 Mch4

Mo⋅ 2 Mco2

Mc2h6 Mh⋅ 6 Mc2h6

⋅ c2h6 +

⋅ c2h6 +

Mc⋅ 3 Mc3h8 Mh⋅ 8 Mc3h8

⋅ c3h8 +

⋅ c3h8 +

Mc⋅ 4 Mc4h10 Mh⋅ 10 Mc4h10

⋅ c4h10 +

⋅ c4h10 +

Mc⋅ 5 Mc5h12 Mh⋅ 12 Mc5h12

⋅ c5h12 +

⋅ c5h12 +

Mc Mco2 Mh⋅ 2 Mh2s

⋅ co2 = 0.726885

⋅ h2s = 0.201373

= 0.083776 ⋅ co2

−3

Ms

9.6792 9248 48 × 10 ⋅ h2s = 9.67

Mh2s

c% :=

⋅ ch4 +

Mc⋅ 2

6

M%c = 9.605441 × 10

M%c

= 0.487338 a! ⋅ 3600 3600

3

a! = 5.475 × 10

co2% co2% := 3.67 .67⋅ $i⋅ c% = 1.300057

Filiera de carbunearderea in pat fluidizat! Mcc

cc :=

= 1.442639 a! ⋅ 3600 3600

co2c := 3.67⋅ c⋅ cc = 2.234272

c = 0.422

Calculul emisiilor de Nx oxid de azot! Combustibili Combustibili gazosi gazosi Filiera de gaz natural

β1 := 0.85 β2 := 0.03 β3 := 0.85 # := 70 − 2 ⋅ N = 48 t

#n := 70

+ := 3.5⋅

t h

h #

#n

= 2.4

4 := ) 0.04 − 0.001⋅ N* ⋅ 100 = 2.9 r := 0.25 − 0.005 ⋅ N = 0.195 gn :=

M%c a!

3

1.7544 4419 19 × 10 = 1.75

3

m

h

12

gnn :=

gn 3600

3

= 0.487338

m

4

s

'$(gn (gn = 4.30 4.3069 692 28 × 10

g '$(gnn −6 ) 1 − 0.01⋅ 4* ) 1 − β2⋅ r * ⋅ β3 = 1.18 1.1883 8375 75 × 10 ⋅ β1⋅ + ⋅ gnn⋅ s 1000

−6

no-% no-% := 0.03 0.034 4⋅ 10

Combustibili solizi si licizi Filiera de carbune ardere pulverizata! 3

gt := 1900 − 2.5⋅ N = 1.87 1.8725 25 × 10

3

go := 1300 − 2.5⋅ N = 1.27 1.2725 25 × 10 ! := 0.92 0.925 5⋅ ) gt⋅ go*

0.5

  3

1.4278 7847 47 × 10 = 1.42



λ ! := 1.4

− 64500

λ ! := 1.4 16

!

0.45⋅ 10 ⋅ e no-termic :=

λ ! − 1  ⋅   λ ! ! 

0.5

−6

1.5328 2807 07 × 10 = 1.53

! 4

n2

n :=

'$(c⋅10

−6

= 0.866887

'$(c = 1.92 1.9264 6433 33 × 10

2

ελ := ) 0.35⋅ λ ! ! + 0.4* = 0.7921 p := 0.2

ε p := 1.73⋅ p + 0.48 = 0.826 εr := 1 − 0.016 ⋅ r = 0.992935

r = 0.195

1

0.11⋅ ) ! − 1100 11 00* εθ := 0.11

3

= 0.758489

+w := 2.4

(

2

)

+w + 0.32 = 0.2432 εw := 0.04⋅ +w nono-co com% m%&s &sti tiee := 0.7 0.7⋅ n⋅ ελ ⋅ ε p ⋅ εr ⋅ εθ⋅ εw = 0.07272 nono- := nono-te term rmic ic + nono-co com% m%&s &sti tiee = 0.072722

ca ca = 1.51 1.5115 1508 08

+g ,

+g s

nonono-aa := ca ca⋅ '$(c '$(c⋅ = 2.117523 1000

4

'$(c = 1.92 1.9264 6433 33 × 10

1"

Filiera de carbune ardere in pat pulverizat! +g

cc cc = 1.44 1.4426 2639 39

s

nonono-cc := cc cc⋅ '$(c '$(c⋅ = 2.021041 1000

4

'$( '$(c = 1.92 1.9264 6433 33 × 10

Calculul emisiilor de praf

aantr := 0.3 99.5 η := 100 4 = 2.9

Filiera de carbune ardere pulverizata! '$(c  pra!a := 10) 1 − η *  A + 4⋅ ⋅ aantr ⋅ ca = 0.045496 32700  

+g

ca ca = 1.51 1.5115 1508 08

s

Filiera de carbune ardere in strat fluidizat!

'$(c   pra!c := 10) 1 − η * A + 4⋅ ⋅ aantr ⋅ cc = 0.043423 32700  

+g s

cc cc = 1.44 1.4426 2639 39

Calculul emisiilor de oxizi de sulf

ηce" := 0.2 ηgne" := 0 η := 0 Filiera de carbune ardere pulverizata!

so2a := 20⋅ ca⋅ s⋅ ) 1 − η* ) 1 − ηce"* = 0.7618

Filiera de carbune ardere in pat fluidizat!

so2c := 20⋅ cc⋅ s⋅ ) 1 − η* ) 1 − ηce"* = 0.72709

cc cc = 1.44 1.4426 2639 39


so2 so2% := 20⋅ c% c%⋅ i⋅ ) 1 − η* ) 1 − ηce"* = 0.075473

1#

4. Analiza de impact

Consumul de resurse naturale

Contributia la epuizarea resurselor de gaz natural si carbune sunt prezentate mai 3os:

A#' gn := 0.0187

+gs% 3

m A#'gn :=

A#' gn

ρgn

A#' % := 0

A#'c := 0.00671

= 0.0186

+gs% +g

+gs% +g +gs% +g

Pentru a determina contributia la epuizarea unei resurse se tine cont de cantitatea de energie maxima primara extrasa4 Prin urmare5 obtinem: 5

A#'cgn := A#'gn⋅ M%e- = 2.40 2. 4073 731 1 × 10

+gs%

5

A#'cc := A#'c⋅ Mae- = 3.17 3.1711 1167 67 × 10

+gs% 5

A#'cc3 := A#'c⋅ Mce- = 3.02 3.0266 6678 78 × 10

+gs%

6cimbari climatice Contributia Contributia relativa a gazelor cu efect de sera este prezentat prezentat mai 3os :

W'co2 := 1

+gco2 +gco2

W'n2o := 280 +gco2 +gn2o

W'ch4 := 21

+gco2 +gch4

1+


E-tractie

−3

W'cco2e-gn := $/2e-Nrec⋅ W'co2⋅ 10

6

1.0015 1556 56 × 10 = 1.00

−3

−3

+gco2

3

W'cn2oe-gn := N2/e-Nrec⋅ W'n2o⋅ 10 W'cch4e-gn := $4e-Nrec⋅ W'ch4⋅ 10

+gco2

2.9818 1893 93 × 10 = 2.98

+gco2

6

1.0926 2666 66 × 10 = 1.09

6

W'tote-gn := W'cco2e-gn + W'cn2oe-gn + W'cch4e-gn = 2.09 2.0972 7204 04 × 10

+gco2

ratare

−3

W'cco2trgn := $/2trNrec⋅ W'co2⋅ 10

+gco2

5

3.1838 386 6 × 10 = 3.18

−3

3

W'cn2otrgn := N2/trNrec⋅ W'n2o⋅ 10

1.8842 4266 66 × 10 = 1.88

+gco2

−3

W'cch4trgn := $4trNrec⋅ W'ch4⋅ 10

5

9.3706 068 8 × 10 = 9.37

+gco2 6

W'tottrgn := W'cco2trgn + W'cn2otrgn + W'cch4trgn = 1.25 1.2573 7338 38 × 10

+gco2

ransport

W'cco2tpgn := $/2tpNrec⋅ W'co2⋅ 10

−3

−3

W'cn2otpgn := N2/tpNrec⋅ W'n2o ⋅ 10

−3

W'cch4tpgn := $4tpNrec⋅ W'ch4⋅ 10

10

1.4851 5111 11 × 10 = 1.48 8

4.8438 3837 37 × 10 = 4.84 9

= 7.23 7.2354 546 6 × 10

+gco2 +gco2

+gco2

10

W'tottpgn := W'cco2tpgn + W'cn2otpgn + W'cch4tpgn = 2.25 2.2570 7095 95 × 10

+gco2

$om%&stie 10

$/2co 2coNr Nrec ec := ) 244 2444.44 4.44 + 14⋅ N* ⋅ M%c = 2.49 2.4959 5916 16 × 10

6

$/co coNrec Nrec := ) 0.1 0.174 + 0.003 .003⋅ N* ⋅ M%c = 1.98 1.9883 8326 26 × 10

7

$4co 4coNr Nrec ec := ) 2.21 2.212 2 + 0.09 0.09⋅ N* ⋅ M%c = 3.07 3.0756 5662 62 × 10

1,

W'cco2cogn := $/2coNrec⋅ W'co2⋅ 10

−3

7

2.4959 5916 16 × 10 = 2.49

−3

W'c$/cogn := $/coNrec⋅ W'n2o⋅ 10

5

5.5673 7314 14 × 10 = 5.56

−3

W'cch4cogn := $4coNrec⋅ W'ch4⋅ 10

+gco2 +gco2 5

6.4588 8891 91 × 10 = 6.45

+gco2

7

W'totcogn := W'cco2cogn + W'c$/cogn + W'cch4cogn = 2.61 2.6161 6178 78 × 10

+gco2

&ezultate globale filiera de gaz natural 10

W'totgn := W'tote-gn + W'tottrgn + W'tottpgn + W'totcogn = 2.26 2.2600 0047 47 × 10

+gco2

Filiera de carbune E-tractie

−3

W'cco2e-c := $/2e-$rec⋅ W'co2⋅ 10

5

2.1375 7584 84 × 10 = 2.13

−3

3

W'cn2oe-c := N2/e-$rec⋅ W'n2o ⋅ 10

−3

W'cch4e-c := $4e-$rec⋅ W'ch4⋅ 10

+gco2

6.1903 0346 46 × 10 = 6.19

5

6.9978 7883 83 × 10 = 6.99

+gco2

+gco2

5

W'tote-c := W'cco2e-c + W'cn2oe-c + W'cch4e-c = 9.19 9.1973 737 7 × 10

+gco2

ratare

−3

W'cco2trc := $/2tr$rec⋅ W'co2⋅ 10

+g

5

= 1.86 1.8690 9013 13 × co2 10

−3

+g

−3

W'cch4trc := $4tr$rec⋅ W'ch4⋅ 10

4

1.0885 8559 59 ×co2 10 = 1.08

W'cn2otrc := N2/tr$rec⋅ W'n2o ⋅ 10

+gco2 3 = 6.83 6.8303 0394 94 × 10

5

W'tottrc := W'cco2trc + W'cn2otrc + W'cch4trc = 2.04 2.0461 6173 73 × 10

+gco2

ransport

−3

W'cco2tpc := $/2tp$rec⋅ W'co2⋅ 10

−3

W'cn2otpc := N2/tp$rec⋅ W'n2o⋅ 10

−3

W'cch4tpc := $4tp$rec⋅ W'ch4⋅ 10

8

2.0092 9212 12 × 10 = 2.00

+gco2 5

9.0971 7195 95 × 10 = 9.09

5

2.6249 4939 39 × 10 = 2.62

+gco2

+gco2 1-

8

W'tottpc := W'cco2tpc + W'cn2otpc + W'cch4tpc = 2.02 2.0209 0935 35 × 10

+gco2

$om%&stie 10

$/2co$ 2co$re recc := ) 1103 1103.1 .187 87 + 1.5 1.5⋅ N* ⋅ Mac = 3.33 3.3357 5752 52 × 10 10

5

N2/co$rec := ) 0.00353 + 0.000138⋅ N* ⋅ Mac = 1.50 1.5038 3892 92 × 10 10 5

$4c $4co$ o$re recc := ) 0.00 0.0094 943 3 + 0.00 0.0000 006 6⋅ N* ⋅ Mac = 3.00 3.0059 5996 96 × 10 10

−3

W'cco2coc := $/2co$rec⋅ W'co2⋅ 10

−3

W'cn2ococ := N2/co$rec⋅ W'n2o⋅ 10

−3

W'cch4coc := $4co$rec⋅ W'ch4⋅ 10

+g

7

3.3357 5752 52 ×co2 10 = 3.33 +g

4

4.2108 0896 96 co2 = 4.21 × 10 +g

3

6.3125 2591 91 × co2 10 = 6.31

7

W'totcoc := W'cco2coc + W'cn2ococ + W'cch4coc = 3.34 3.3405 0594 94 × 10

+gco2

&ezultate globale filiera de carbune ardere pulverizata! 8

W'totc := W'tote-c + W'tottrc + W'tottpc + W'totcoc = 2.36 2.3662 6237 37 × 10

Filiera de carbune ardere in pat fluidizat E-tractie

−3

W'cco2e-c3 := $/2e-$rec3⋅ W'co2⋅ 10

−3

W'cn2oe-c3 := N2/e-$rec3⋅ W'n2o⋅ 10 W'cch4e-c3 := $4e-$rec3⋅ W'ch4⋅ 10

+gco2

5

2.0401 0188 88 × 10 = 2.04

−3

3

5.9082 8291 91 × 10 = 5.90

5

= 6.67 6.6790 9034 34 × 10

+gco2

+gco2

5

W'tote-c3 := W'cco2e-c + W'cn2oe-c + W'cch4e-c = 9.19 9.1973 737 7 × 10

+gco2

ratare

−3

W'cco2trc3 := $/2tr$rec3⋅ W'co2⋅ 10

−3

W'cn2otrc3 := N2/tr$rec3⋅ W'n2o ⋅ 10

5

1.7838 3854 54 × 10 = 1.78

4

.03896 96 × 10 = 1.038

+gco2 +gco2

1.

W'cch4trc3 := $4tr$rec3⋅ W'ch4⋅ 10

−3

+gco2

3

6.5191 9177 77 × 10 = 6.51

5

W'tottrc3 := W'cco2trc + W'cn2otrc + W'cch4trc = 2.04 2.0461 6173 73 × 10

+gco2

ransport

−3

W'cco2tpc3 := $/2tp$rec3⋅ W'co2⋅ 10

1.9176 7666 66 × 10 = 1.91

−3

W'cn2otpc3 := N2/tp$rec3⋅ W'n2o⋅ 10 W'cch4tpc3 := $4tp$rec3⋅ W'ch4⋅ 10

+gco2

8

−3

5

8.6826 2695 95 × 10 = 8.68

5

= 2.50 2.5053 5337 37 × 10

+gco2

+gco2

8

W'tottpc3 := W'cco2tpc + W'cn2otpc + W'cch4tpc = 2.02 2.0209 0935 35 × 10

+gco2

$om%&stie

10

$/2co$ 2co$re rec3 c3 := ) 110 1103.18 3.187 7 + 1.5 1.5⋅ N* ⋅ Mcc = 3.18 3.1837 3764 64 × 10 10

5

N2/co$rec3 := ) 0.00353 + 0.000138⋅ N* ⋅ Mcc = 1.43 1.4353 5369 69 × 10 10 5

$4c $4co$ o$re rec3 c3 := ) 0.00 0.0094 943 3 + 0.00 0.0000 006 6 ⋅ N* ⋅ Mcc = 2.86 2.8690 9032 32 × 10 10

W'cco2coc3 := $/2co$rec3⋅ W'co2⋅ 10

−3

−3

W'cn2ococ3 := N2/co$rec3⋅ W'n2o ⋅ 10

−3

W'cch4coc3 := $4co$rec3⋅ W'ch4⋅ 10

7

3.1837 3764 64 × 10 = 3.18

+gco2 4

4.0190 9033 33 × 10 = 4.01

3

6.0249 4967 67 × 10 = 6.02

+gco2

+gco2

7

W'totcoc3 := W'cco2coc + W'cn2ococ + W'cch4coc = 3.34 3.3405 0594 94 × 10

+gco2

&ezultate globale filiera de carbune ardere in pat fluidizat! 8

W'totc3 := W'tote-c3 + W'tottrc3 + W'tottpc3 + W'totcoc3 = 2.36 2.3662 6237 37 × 10

Toxicitatea umana

7ai 3os se prezinta contributia relativa a poluantilor la aceasta clasa de impact:

1/

'hc := 0.5

+gc%

+gc%

'h! := 94

+gh!

+ghc

'no- := 1.2

+gc% +gno-

'ch2o := 0.83

+gc% +gch2o

'h2s := 0.22

'so- := 0.096 +g so-

+g pr

+gc%

'hg := 260

+gh2s +gc%

+gc%

' pr := 0.82

+gc%

'c6h6 := 1900

+ghg

+gc% +gc6h6

Determinarea contributiei totale la clasa de toxicitate umana tine cont de masa de poluant generata in cadrul etapei ciclului de viata: extractie5 tratare5 transport si combustie

Filiera Filiera de gaz ga z natural E-tractie

−3

'cc6h6e-gn := $66e-Nrec⋅ 'c6h6⋅ 10

−3

'cno-e-gn := N/e-Nrec⋅ 'no-⋅ 10

6

1.2170 7007 07 × 10 = 1.21 3

6.9720 207 7 × 10 = 6.97

−3

'cpre-gn := 're-Nrec⋅ ' pr ⋅ 10 = 566.08604

−3

'cso-e-gn := /2e-Nrec⋅ 'so-⋅ 10 = 206.211789 6

'tote-gn := 'cc6h6e-gn + ' cno-e-gn + 'cpre-gn + 'cso-e-gn = 1.22 1.2247 4751 51 × 10

ratare

−3

'cc6h6trgn := $66trNrec⋅ ' c6h6⋅ 10

−3

'cno-trgn := N/trNrec⋅ ' no-⋅ 10

6

6.3930 3047 47 × 10 = 6.39 3

= 3.58 3.5890 9079 79 × 10

−3

'cprtrgn := 'rtrNrec⋅ ' pr ⋅ 10 = 279.371684

−3

'cso-trgn := /2trNrec⋅ ' so-⋅ 10

3

1.2063 6394 94 × 10 = 1.20

6

'tottrgn := 'cc6h6trgn + ' cno-trgn + 'cprtrgn + 'cso-trgn = 6.39 6.3981 8122 22 × 10

ransport

−3

'cc6h6tpgn := $66tpNrec⋅ 'c6h6⋅ 10

−3

'cno-tpgn := N/-tpNrec⋅ 'no- ⋅ 10

8

2.2089 8996 96 × 10 = 2.20 8

1.6395 9562 62 × 10 = 1.63

20

−3

'cprtpgn := 'rtpNrec⋅ ' pr ⋅ 10

6

1.4185 8552 52 × 10 = 1.41

−3

'cso-tpgn := /2tpNrec⋅ ' so-⋅ 10

6

1.9878 7842 42 × 10 = 1.98

8

'tottpgn := 'cc6h6tpgn + 'cno-tpgn + 'cprtpgn + 'cso-tpgn = 3.88 3.8826 2623 23 × 10

$om%&stie 5

$66 $66co coN Nre recc := ) 0.04 0.0496 96 + 0.00 0.0005 05⋅ N* ⋅ M%c = 5.29 5.2925 2598 98 × 10 6

N/-coNrec := ) 0.633 + 0.007⋅ N* ⋅ M%c = 6.81 6.8198 9863 63 × 10

5

$2/ $2/co coN Nre recc := ) 0.05 0.056 6 + 0.00 0.0004 04⋅ N* ⋅ M%c = 5.80 5.8016 1687 87 × 10 6

'rco coNrec Nrec := ) 0.39 0.39 + 0.00 0.0075 75⋅ N* ⋅ M%c = 4.53 4.5385 8571 71 × 10

5

/2co 2coN Nrec rec := ) 0.01 0.0108 08 + 0.00 0.002 2⋅ N* ⋅ M%c = 3.15 3.1505 0585 85 × 10

−3

'cc6h6cogn := $66coNrec⋅ 'c6h6⋅ 10

−3

'cno-cogn := N/-coNrec⋅ 'no- ⋅ 10

6

1.0055 5594 94 × 10 = 1.00 3

8.1838 3836 36 × 10 = 8.18

−3

'cch2ocogn := $2/coNrec⋅ 'ch2o⋅ 10 = 481.539984

−3

'cprcogn := 'rcoNrec⋅ ' so-⋅ 10 = 435.702818

−3

'cso-cogn := /2coNrec⋅ 'so-⋅ 10 = 30.245614

6

'totcogn1 := 'cc6h6cogn + 'cno-cogn + 'cprcogn = 1.01 1.0142 4213 13 × 10 'totcogn2 := 'cso-cogn + ' cch2ocogn = 511.785597 6

'totcogn := 'totcogn1 + 'totcogn2 = 1.01 1.0147 4725 25 × 10


'totgn := ' tote-gn + 'tottrgn + 'tottpgn + 'totcogn = 3.96 3.9689 8999 99 × 10

Filiera de carbune - ardere pulverizata E-tractie

−3

'chce-c := $Le-$rec⋅ ' hc⋅ 10

−5

4.3952 521 1 × 10 = 4.39

21

−3

'ch!e-c := e-$rec⋅ ' h! ⋅ 10 = 0.012261 'ch2se-c := 2e-$rec⋅ 'h2s⋅ 10

−3

−3

'cno-e-c := N/-e-$rec⋅ ' no-⋅ 10

−5

1.4140 4029 29 × 10 = 1.41

3

1.5198 9892 92 × 10 = 1.51

−3

'cpre-c := 're-$rec⋅ ' pr ⋅ 10 = 497.59444

−3

'cso-e-c := /2e-$rec⋅ ' so-⋅ 10 = 286.737804

= 0.012319 'tote-c1 := 'chce-c + 'ch!e-c + 'ch2se-c 3

'tote-c2 := 'cno-e-c + 'cpre-c + 'cso-e-c = 2.30 2.3042 4224 24 × 10 3

'tote-c := ' tote-c1 + 'tote-c2 = 2.30 2.3042 4236 36 × 10

ratare

−3

'chctrc := $Ltr$rec⋅ ' hc⋅ 10

−5

7.2818 187 7 × 10 = 7.28

−3

'ch!trc := tr$rec⋅ ' h! ⋅ 10 = 0.021257

−3

'ch2strc := 2tr$rec⋅ ' h2s⋅ 10

'cno-trc := N/-tr$rec⋅ ' no- ⋅ 10

−5

1.2905 0509 09 × 10 = 1.29

−3

3

1.2136 3645 45 × 10 = 1.21

−3

'cprtrc := 'rtr$rec⋅' pr ⋅ 10 = 67.175249

−3

'cso-trc := /2tr$rec⋅ ' so-⋅ 10 = 64.857188

3

'tottrc1 := 'chctrc + 'ch!trc + 'ch2strc + 'cno-trc = 1.21 1.2136 3666 66 × 10 'tottrc2 := 'cprtrc + 'cso-trc = 132.032437 3

'tottrc := ' tottrc1 + ' tottrc2 = 1.34 1.3456 5699 99 × 10

ransport

−3

'chctpc := $Ltp$rec⋅ ' hc⋅ 10 = 1.97912

−3

'ch!tpc := tp$rec⋅' h! ⋅ 10 = 8.572948 22

'ch2stpc := 2tp$rec⋅ ' h2s⋅ 10

−3

−3

= 3.51 3.5178 7881 81 × 10

−3

6

'cno-tpc := N/-tp$rec⋅ ' no- ⋅ 10

−3

'cprtpc := 'rtp$rec⋅ ' pr ⋅ 10

2.7221 2159 59 × 10 = 2.72 5

.75195 95 × 10 = 1.751

'cso-tpc := /2tp$rec⋅ ' so-⋅ 10

−3

5

1.1910 1083 83 × 10 = 1.19

6

'tottpc1 := 'chctpc + 'ch!tpc + ' ch2stpc + 'cno-tpc = 2.72 2.7221 2169 69 × 10 5

'tottpc2 := 'cprtpc + 'cso-tpc = 2.94 2.9430 3033 33 × 10 6

'tottpc := 'tottpc1 + 'tottpc2 = 3.01 3.0164 6473 73 × 10

$om%&stie $Lc $Lco$ o$re recc := ) 0.00 0.0000 0001 0196 96 + 0.00 0.0000 0000 0005 05⋅ N* ⋅ Mac = 74.77749 co co$r $rec ec := ) 0.00 0.0000 0000 0016 1699 99 + 0.00 0.0000 0000 0000 003 3⋅ N* ⋅ Mac = 6.044762 2c 2co$ o$re recc := ) 0.00 0.0000 0000 0000 0098 989 9 + 0.00 0.0000 0000 0000 0000 003 3⋅ N* ⋅ Mac = 0.304472 3

co co$r $rec ec := ) 0.00 0.0000 0040 407 7 + 0.00 0.0000 0000 003 3⋅ N* ⋅ Mac = 1.3 1.31084 1084 × 10 10 8

N/-co$rec := ) 3.4639 + 0.05⋅ N* ⋅ Mac = 1.19 1.1958 5814 14 × 10 10 8

'rco$rec := ) 10.198 + 0.45⋅ N* ⋅ Mac = 4.51 4.5128 2866 66 × 10 10

8

/2co$rec := ) 7.2598 + 0.3⋅ N* ⋅ Mac = 3.14 3.1459 5958 58 × 10 10

−3

'chccoc := $Lco$rec⋅ ' hc⋅ 10 = 0.037389

−3

'ch!coc := co$rec⋅ ' h! ⋅ 10 = 0.568208 'ch2scoc := 2co$rec⋅ 'h2s⋅ 10

−3

−5

6.6983 8395 95 × 10 = 6.69

−3

'chgcoc := co$rec⋅ 'hg⋅ 10 = 340.81852

−3

'cno-coc := N/-co$rec⋅ ' no-⋅ 10

−3

'cprcoc := 'rco$rec⋅ ' pr ⋅ 10

5

= 1.43 1.4349 4977 77 × 10 5

3.700 055 × 10 = 3.70

'cso-coc := /2co$rec⋅ 'so-⋅ 10

−3

4

3.0201 0119 19 × 10 = 3.02

2"

5

'totcoc1 := 'chccoc + ' ch!coc + 'ch2scoc + 'cno-coc = 1.43 1.4349 4983 83 × 10 5

'totcoc2 := 'chgcoc + 'cprcoc + 'cso-coc = 4.00 4.0059 597 7 × 10 5

'totcoc := 'totcoc1 + 'totcoc2 = 5.44 5.4409 0954 54 × 10


'totc := 'tote-c + 'tottrc + 'tottpc + 'totcoc = 3.56 3.5642 4218 18 × 10

Filiera de carbune - ardere in pat flu idizat E-tractie

−3

'chce-c3 := $Le-$rec3⋅ 'hc⋅ 10

−5

4.1949 4948 48 × 10 = 4.19

−3

'ch!e-c3 := e-$rec3⋅ 'h! ⋅ 10 = 0.011703

−3

'ch2se-c3 := 2e-$rec3⋅ 'h2s⋅ 10

−5

1.3496 9601 01 × 10 = 1.34

−3

'cno-e-c3 := N/-e-$rec3⋅ 'no- ⋅ 10

3

1.4506 064 4 × 10 = 1.45

−3

'cpre-c3 := 're-$rec3⋅ ' pr ⋅ 10 = 474.922272

−3

'cso-e-c3 := /2e-$rec3⋅ 'so-⋅ 10 = 273.673012 3

'tote-c31 := 'chce-c3 + 'ch!e-c3 + 'ch2se-c3 + 'cno-e-c3 = 1.45 1.4506 0652 52 × 10 'tote-c32 := 'cpre-c3 + 'cso-e-c3 = 748.595284 3

'tote-c3 := 'tote-c31 + 'tote-c32 = 2.19 2.1992 9247 47 × 10

ratare

−3

'chctrc3 := $Ltr$rec3⋅ ' hc⋅ 10

−5

6.9500 0082 82 × 10 = 6.95

−3

'ch!trc3 := tr$rec3⋅ ' h! ⋅ 10 = 0.020289 'ch2strc3 := 2tr$rec3⋅ ' h2s⋅ 10

−3

−3

'cno-trc3 := N/-tr$rec3⋅ ' no- ⋅ 10

−5

1.2317 1709 09 × 10 = 1.23

3

1.1583 8347 47 × 10 = 1.15

−3

'cprtrc3 := 'rtr$rec3⋅ ' pr ⋅ 10 = 64.114507

−3

'cso-trc3 := /2tr$rec3⋅ ' so-⋅ 10 = 61.902064 3

'tottrc31 := 'chctrc3 + 'ch!trc3 + 'ch2strc3 + 'cno-trc3 = 1.15 1.1583 8367 67 × 10

2#

'tottrc32 := 'cprtrc3 + 'cso-trc3 = 126.016571 3

'tottrc3 := 'tottrc31 + 'tottrc32 = 1.28 1.2843 4384 84 × 10

ransport

−3

'chctpc3 := $Ltp$rec3⋅ ' hc⋅ 10 = 1.888945

−3

'ch!tpc3 := tp$rec3⋅ ' h! ⋅ 10 = 8.182334

−3

'ch2stpc3 := 2tp$rec3⋅ 'h2s⋅ 10

−3

3.3575 7594 94 × 10 = 3.35

−3

'cno-tpc3 := N/-tp$rec3⋅ 'no- ⋅ 10

−3

'cprtpc3 := 'rtp$rec3⋅ ' pr ⋅ 10

6

2.5981 8127 27 × 10 = 2.59 5

1.6721 2125 25 × 10 = 1.67

−3

'cso-tpc3 := /2tp$rec3⋅ 'so-⋅ 10

5

1.1368 6813 13 × 10 = 1.13

6

'tottpc31 := 'chctpc3 + ' ch!tpc3 + 'ch2stpc3 + 'cno-tpc3 = 2.59 2.5981 8138 38 × 10 5

'tottpc32 := 'cprtpc3 + 'cso-tpc3 = 2.80 2.8089 8938 38 × 10 6

'tottpc3 := 'tottpc31 + 'tottpc32 = 2.87 2.8790 9031 31 × 10

$om%&stie

$Lc $Lco$ o$re rec3 c3 := ) 0.00 0.0000 0001 0196 96 + 0.00 0.0000 0000 0005 05⋅ N* ⋅ Mcc = 71.370362 co co$r $rec ec3 3 := ) 0.00 0.0000 0000 0016 1699 99 + 0.00 0.0000 0000 0000 003 3⋅ N* ⋅ Mcc = 5.769341 2c 2co$ o$re rec3 c3 := ) 0.00 0.0000 0000 0000 0098 989 9 + 0.00 0.0000 0000 0000 0000 003 3⋅ N* ⋅ Mcc = 0.2906 3

co co$r $rec ec3 3 := ) 0.00 0.0000 0040 407 7 + 0.00 0.0000 0000 003 3⋅ N* ⋅ Mcc = 1.25 1.2511 1114 14 × 10 10 8

N/-co$rec3 := ) 3.4639 + 0.05⋅ N* ⋅ Mcc = 1.14 1.1413 1329 29 × 10 10 8

'rco$ co$rec rec3 := ) 10. 10.198 198 + 0.45 0.45⋅ N* ⋅ Mcc = 4.30 4.3072 7244 44 × 10 10

8

/2co$ 2co$rrec3 ec3 := ) 7.25 7.2598 98 + 0.3 0.3⋅ N* ⋅ Mcc = 3.00 3.0026 2617 17 × 10 10

−3

'chccoc3 := $Lco$rec3⋅ 'hc⋅ 10 = 0.035685

−3

'ch!coc3 := co$rec3⋅ 'h! ⋅ 10 = 0.542318 2+

−3

'ch2scoc3 := 2co$rec3⋅ 'h2s⋅ 10

−5

6.3931 3192 92 × 10 = 6.39

−3

'chgcoc3 := co$rec3⋅ ' hg⋅ 10 = 325.289619

−3

'cno-coc3 := N/-co$rec3⋅ 'no-⋅ 10

−3

'cprcoc3 := 'rco$rec3⋅ ' pr ⋅ 10

5

1.3695 9594 94 × 10 = 1.36 5

3.5319 194 4 × 10 = 3.53

−3

'cso-coc3 := /2co$rec3⋅ 'so-⋅ 10

4

2.8825 2512 12 × 10 = 2.88

5

'totcoc31 := 'chccoc3 + ' ch!coc3 + 'ch2scoc3 + 'cno-coc3 = 1.36 1.3696 96 × 10 5

'totcoc32 := 'cprcoc3 + 'chgcoc3 + 'cso-coc3 = 3.82 3.8234 3444 44 × 10 5

'totcoc3 := 'totcoc31 + 'totcoc32 = 5.19 5.1930 3044 44 × 10

&ezultate globale filiera de carbune ardere in pat fluidizat!

6

'totc3 := ' tote-c3 + 'tottrc3 + 'tottpc3 + 'totcoc3 = 3.40 3.4018 1819 19 × 10

Ecotoxicitate $n aceast a categorie intra urmatorii urmatorii indicatori:

a! poluarea asupra panzei de apa freatica 8 F'E)P b! poluarea poluarea apei din mari si oceane 8 7'E)P c! poluarea solului 8 )E)P

7ai 3os se prezinta contributia relatica a poluantilor la aceasta clasa de impact:

AE' c6h6 := 0.000084

AE' ch2o := 8.3

AE' h! := 4.6

AE' hg := 320

+gc% +gc6h6 +gc%

+gch2o +gc%

MAE'c6h6 := 0.0028

MAE'ch2o := 1.6

+gc% +gc6h6 +gc% +gch2o +gc%

MAE'h! := 41000000

+gh!

+gh! +gc% +ghg

MAE'hg := 12000000

+gc% +ghg

E'c6h6 := 0.000016

+gc% +gc6h6

E'ch2o := 0.94

E'h! := 0.0029

+gc% +gch2o +gc% +gh!

E'hg := 28000

+gc% +ghg

2,

Filiera Filiera de gaz g az natural

E-tractie

−3

AE' cc6h6e-gn := $66e-Nrec⋅ AE'c6h6⋅ 10 = 0.053805 AE' tote-gn := AE' cc6h6e-gn = 0.053805

−3

MAE'cc6h6e-gn := $66e-Nrec⋅ MAE'c6h6⋅ 10 = 1.793484 MAE'tote-gn := MAE'cc6h6e-gn = 1.793484

−3

E'cc6h6e-gn := $66e-Nrec⋅ E'c6h6⋅ 10 = 0.010248 E'tote-gn := E'cc6h6e-gn = 0.010248

ratare

−3

AE' cc6h6trgn := $66trNrec⋅ AE'c6h6⋅ 10 = 0.28264 AE' tottrgn := AE' cc6h6trgn = 0.28264

−3

MAE'cc6h6trgn := $66trNrec⋅ MAE'c6h6⋅ 10 = 9.421332 MAE'tottrgn := MAE'cc6h6trgn = 9.421332

−3

E'cc6h6trgn := $66trNrec⋅ E'c6h6⋅ 10 = 0.053836 E'tottrgn := E'cc6h6trgn = 0.053836

ransport

−3

AE' cc6h6tpgn := $66tpNrec⋅ AE'c6h6⋅ 10 = 9.766089 AE' tottpgn := AE' cc6h6tpgn = 9.766089

−3

MAE'cc6h6tpgn := $66tpNrec⋅ MAE'c6h6⋅ 10 = 325.536293 MAE'tottpgn := MAE'cc6h6tpgn = 325.536293

−3

E'cc6h6tpgn := $66tpNrec⋅ E'c6h6⋅ 10 = 1.860207 E'tottpgn := E'cc6h6e-gn = 0.010248

$om%&stie 2-

−3

AE' cc6h6cogn := $66coNrec⋅ AE'c6h6⋅ 10 = 0.044458

−3

AE' cch2ocogn := $2/coNrec⋅ AE'ch2o⋅ 10

3

4.815 54 × 10 = 4.81

3

AE' totcogn := AE' cc6h6cogn + AE' cch2ocogn = 4.81 4.8154 5444 44 × 10

−3

MAE'cc6h6cogn := $66coNrec⋅ MAE'c6h6⋅ 10 = 1.481927

−3

MAE'cch2ocogn := $2/coNrec⋅ MAE'ch2o⋅ 10 = 928.269848 MAE'totcogn := MAE'cc6h6cogn + MAE'cch2ocogn = 929.751776

−3

−3

E'cc6h6cogn := $66coNrec⋅ E'c6h6⋅ 10

= 8.46 8.4681 8157 57 × 10

−3

E'cch2ocogn := $2/coNrec⋅ E'ch2o⋅ 10 = 545.358536 E'totcogn := E'cc6h6cogn + E'cch2ocogn = 545.367004

3

AE' totgn := AE' tote-gn + AE' tottrgn 4.8255 5547 47 × 10 + AE'tottpgn + AE'totcogn = 4.82

3

+ MAE'tottpgn + MAE'totcogn = 1.26 MAE'totgn := MAE'tote-gn + MAE'tottrgn 1.2665 6503 03 × 10

&ezultate globale filiera de gaz natural E'totgn := E'tote-gn + E'tottrgn + E'tottpgn + E'totcogn = 545.441337

Filiera Filiera de carbune - ardere pulverizata

E-tractie

−3

AE' ch!e-c := e-$rec⋅ AE'h! ⋅ 10

−4

6.0001 017 7 × 10 = 6.00

−4

AE' tote-c := AE' ch!e-c = 6.00 6.0001 017 7 × 10

−3

MAE'ch!e-c := e-$rec⋅ MAE'h! ⋅ 10

3

5.3479 7978 78 × 10 = 5.34 3

MAE'tote-c := MAE'ch!e-c = 5.34 5.3479 7978 78 × 10 E'ch!e-c := e-$rec⋅ E'h! ⋅ 10

−3

−7

3.7827 2716 16 × 10 = 3.78

−7

E'tote-c := E'ch!e-c = 3.78 3.7827 2716 16 × 10

ratare

2.

−3

AE' ch!trc := tr$rec⋅ AE'h! ⋅ 10

−3

1.0402 0256 56 × 10 = 1.04

−3

AE' tottrc := AE' ch!trc = 1.04 1.0402 0256 56 × 10

−3

MAE'ch!trc := tr$rec⋅MAE'h! ⋅ 10

3

9.2718 1843 43 × 10 = 9.27

−3

MAE'tottrc := MAE'ch!trc⋅ 10 = 9.271843

−3

E'ch!trc := tr$rec⋅ E'h! ⋅ 10

−7

6.5581 8133 33 × 10 = 6.55

−7

E'tottrc := E'ch!trc = 6.55 6.5581 8133 33 × 10

ransport

−3

AE' ch!tpc := tp$rec⋅AE'h! ⋅ 10 = 0.419527 AE' tottpc := AE' ch!tpc = 0.419527

−3

MAE'ch!tpc := tp$rec⋅ MAE'h! ⋅ 10

6

3.7392 9265 65 × 10 = 3.73 6

MAE'tottpc := MAE'ch!tpc = 3.73 3.7392 9265 65 × 10 E'ch!tpc := tp$rec⋅ E'h! ⋅ 10

−3

−4

= 2.64 2.6448 4846 46 × 10 −4

E'tottpc := E'ch!tpc = 2.64 2.6448 4846 46 × 10

$om%&stie

−3

AE' ch!coc := co$rec⋅ AE'h! ⋅ 10 = 0.027806

−3

AE' chgcoc := co$rec⋅ AE'hg⋅ 10 = 419.468948 AE' totcoc := AE' ch!coc + AE' chgcoc = 419.496754

−3

MAE'ch!coc := co$rec⋅ MAE'h! ⋅ 10

−3

MAE'chgcoc := co$rec⋅ MAE'hg⋅ 10

5

2.4783 8352 52 × 10 = 2.47

7

1.5730 3009 09 × 10 = 1.57

7

MAE'totcoc := MAE'ch!coc + MAE'chgcoc = 1.59 1.5977 7792 92 × 10

−3

E'ch!coc := co$rec⋅ E'h! ⋅ 10

E'chgcoc := co$rec⋅ E'hg⋅ 10

−3

−5

1.7529 2981 81 × 10 = 1.75

4

3.6703 0353 53 × 10 = 3.67

4

E'totcoc := E'ch!coc + E'chgcoc = 3.67 3.6703 0353 53 × 10

&ezultate globale filiera de carbune ardere pulverizata! AE' totc := AE' tote-c + AE' tottrc + AE' tottpc + AE' totcoc = 419.917922 2/

7

MAE'totc := MAE'tote-c + MAE'tottrc 1.9722 2254 54 × 10 + MAE'tottpc + MAE'totcoc = 1.97 4

E'totc := E'tote-c + E'tottrc 3.6703 0353 53 × 10 + E'tottpc + E'totcoc = 3.67

Filiera de carbune - ardere in strat fluidizat

E-tractie AE' ch!e-c3 := e-$rec3⋅ AE'h! ⋅ 10

−3

−4

5.7267 6781 81 × 10 = 5.72

−4

AE' tote-c3 := AE' ch!e-c3 = 5.72 5.7267 6781 81 × 10

−3

MAE'ch!e-c3 := e-$rec3⋅ MAE'h! ⋅ 10

3

5.1043 4305 05 × 10 = 5.10 3

MAE'tote-c3 := MAE'ch!e-c3 = 5.10 5.1043 4305 05 × 10

−3

E'ch!e-c3 := e-$rec3⋅ E'h! ⋅ 10

−7

3.6103 0362 62 × 10 = 3.61

−7

E'tote-c3 := E'ch!e-c3 = 3.61 3.6103 0362 62 × 10

ratare

−3

AE' ch!trc3 := tr$rec3⋅ AE'h! ⋅ 10

−4

= 9.92 9.9285 8578 78 × 10 −4

AE' tottrc3 := AE' ch!trc3 = 9.92 9.9285 8578 78 × 10 MAE'ch!trc3 := tr$rec3⋅ MAE'h! ⋅ 10

−3

3

8.8493 9385 85 × 10 = 8.84 3

MAE'tottrc3 := MAE'ch!trc3 = 8.84 8.8493 9385 85 × 10

−3

E'ch!trc3 := tr$rec3⋅E'h! ⋅ 10

−7

6.2593 9321 21 × 10 = 6.25

−7

E'tottrc3 := E'ch!trc3 = 6.25 6.2593 9321 21 × 10

ransport

−3

AE' ch!tpc3 := tp$rec3⋅ AE'h! ⋅ 10 = 0.400412 AE' tottpc3 := AE' ch!tpc3 = 0.400412 MAE'ch!tpc3 := tp$rec3⋅ MAE'h! ⋅ 10

−3

6

3.56889 6889 × 10 = 3.5 6

MAE'tottpc3 := MAE'ch!tpc3 = 3.56 3.5688 889 9 × 10

−3

E'ch!tpc3 := tp$rec3⋅ E'h! ⋅ 10

−4

2.5243 4337 37 × 10 = 2.52

"0

−4

E'tottpc3 := E'ch!tpc3 = 2.52 2.5243 4337 37 × 10

$om%&stie

−3

AE' ch!coc3 := co$rec3⋅ AE'h! ⋅ 10 = 0.026539

−3

AE' chgcoc3 := co$rec3⋅ AE'hg⋅ 10 = 400.356454 AE' totcoc3 := AE' ch!coc3 + AE' chgcoc3 = 400.382993 MAE'ch!coc3 := co$rec3⋅ MAE'h! ⋅ 10

−3

MAE'chgcoc3 := co$rec3⋅ MAE'hg⋅ 10

−3

5

2.3654 543 3 × 10 = 2.36

7

= 1.50 1.5013 1337 37 × 10

7

MAE'totcoc3 := MAE'ch!coc3 + MAE'chgcoc3 = 1.52 1.5249 4991 91 × 10

−3

E'ch!coc3 := co$rec3⋅ E'h! ⋅ 10

−3

E'chgcoc3 := co$rec3⋅ E'hg⋅ 10

−5

= 1.67 1.6731 3109 09 × 10

4

3.5031 3119 19 × 10 = 3.50

4

E'totcoc3 := E'ch!coc3 + E'chgcoc3 = 3.50 3.5031 3119 19 × 10

&ezultate globale filiera de carbune ardere in pat fluidizat! AE' totc3 := AE' tote-c3 + AE' tottrc3 + AE' tottpc3 + AE' totcoc3 = 400.784971 7

+ MAE'tottpc3 + MAE'totcoc3 = 1.88 MAE'totc3 := MAE'tote-c3 + MAE'tottrc3 1.8832 3275 75 × 10 4

E'totc3 := E'tote-c3 + E'tottrc3 3.5031 3119 19 × 10 + E'tottpc3 + E'totcoc3 = 3.50

Poluarea fotocimica fotocimica $ndicatorul care st a la baza acestei c lase de impact poarta poarta denumirea de potentialul potentialul de poluare fotocimica5 PCP4 PCP4 7ai 7 ai 3os se prezinta contributia relativa relativa a poluantilor la aceasta c lasa de impact :

'/$' co := 0.027

'/$' ch4 := 0.006

+gc2h4 +gco +gc2h4 +gch4

'/$' ch2o := 0.519

+gc2h4 +gch2o

'/$' no- := 0.028

+gc2h4 +gno2

"1

'/$' so- := 0.048

+gc2h4 +gso2

Filiera Filiera de gaz ga z natural

E-tractie

−3

'/$' ccoe-gn := $/e-Nrec⋅ '/$'co⋅ 10 = 29.487665

−3

'/$' cch4e-gn := $4e-Nrec⋅ '/$'ch4⋅ 10 = 312.190363

−3

'/$' cno-e-gn := N/e-Nrec⋅ '/$' no-⋅ 10 = 162.68164

−3

'/$' cso-e-gn := /2e-Nrec⋅ '/$'so-⋅ 10 = 103.105895 '/$' tote-gn := '/$' ccoe-gn + '/$' cch4e-gn + '/$' cno-e-gn + '/$' cso-e-gn = 607.465562

ratare

−3

'/$' ccotrgn := $/trNrec⋅'/$' co⋅ 10 = 34.125194

−3

'/$' cch4trgn := $4trNrec⋅ '/$'ch4⋅ 10 = 267.73371

−3

'/$' cno-trgn := N/trNrec⋅ '/$' no- ⋅ 10 = 83.745175

−3

'/$' cso-trgn := /2trNrec⋅ '/$' so-⋅ 10 = 603.196813

+ '/$' cno-trgn + '/$' cso-trgn = 988.800891 '/$' tottrgn := '/$' ccotrgn + '/$' cch4trgn ransport

−3

6

'/$' ccotpgn := $/tpNrec⋅ '/$' co⋅ 10

= 3.45 3.4598 9884 84 × 10

'/$' cch4tpgn := $4tpNrec⋅ '/$' ch4⋅ 10

−3

6

2.0672 7274 74 × 10 = 2.06

−3

'/$' cno-tpgn := N/-tpNrec⋅ '/$' no-⋅ 10

−3

'/$' cso-tpgn := /2tpNrec⋅ '/$' so-⋅ 10

6

3.8256 5645 45 × 10 = 3.82 5

= 9.93 9.9392 921 1 × 10

7

'/$' tottpgn := '/$' ccotpgn + '/$' cch4tpgn 1.0346 4672 72 × 10 + '/$' cno-tpgn + '/$' cso-tpgn = 1.03 $om%&stie

−3

'/$' ccocogn := $/coNrec⋅ '/$' co⋅ 10 = 53.684811

−3

'/$' cch2ocogn := $2/coNrec⋅ '/$'ch2o⋅ 10 = 301.107532

$/co $/coNre Nrecc = 1.9883 1.988326 26 "2

−3

'/$' cch4cogn := $4coNrec⋅ '/$'ch4⋅ 10 = 184.539738

N/-co N/-coNre Nrecc = 6.8198 6.8198

−3

'/$' cno-cogn := N/-coNrec⋅ '/$'no-⋅ 10 = 190.956173

−3

'/$' cso-cogn := /2coNrec⋅ '/$'so-⋅ 10 = 15.122807 '/$' totcogn1 := '/$' ccocogn + '/$' cch4cogn + '/$' cno-cogn = 429.180723 '/$' totcogn2 := '/$' cso-cogn + '/$' cch2ocogn = 316.230339 '/$' totcogn := '/$' totcogn1 + '/$' totcogn2 = 745.411062


'/$' totgn := '/$' tote-gn + '/$' tottrgn 1.0349 4907 07 × 10 + '/$' tottpgn + '/$' totcogn = 1.03

Filiera de carbune - ardere pulverizata

E-tractie

−3

'/$' ccoe-c := $/e-$rec⋅ '/$'co⋅ 10 = 7.668932

−3

'/$' cch4e-c := $4e-$rec⋅ '/$'ch4⋅ 10 = 199.939503

−3

'/$' cno-e-c := N/-e-$rec⋅ '/$'no- ⋅ 10 = 35.464143

−3

'/$' cso-e-c := /2e-$rec⋅ '/$' so-⋅ 10 = 143.368902 '/$' tote-c := '/$' ccoe-c + '/$' cch4e-c + '/$' cno-e-c + '/$' cso-e-c = 386.44148

ratare

−3

'/$' ccotrc := $/tr$rec⋅ '/$' co⋅ 10 = 5.92016

−3

'/$' cch4tr := $4tr$rec⋅ '/$' ch4⋅ 10 = 1.951541

−3

'/$' cno-trc := N/-tr$rec⋅ '/$'no- ⋅ 10 = 28.318383

−3

'/$' cso-trc := /2tr$rec⋅ '/$' so-⋅ 10 = 32.428594 '/$' tottrc := '/$' ccotrc + '/$' cch4tr + '/$' cno-trc + '/$' cso-trc = 68.618678

ransport

""

−3

5

'/$' ccotpc := $/tp$rec⋅ '/$'co⋅ 10

6.7748 4842 42 × 10 = 6.77

−3

'/$' cch4tp := $4tp$rec⋅ '/$'ch4⋅ 10 = 74.99825

−3

'/$' cno-tpc := N/-tp$rec⋅ '/$' no- ⋅ 10

−3

'/$' cso-tpc := /2tp$rec⋅ '/$'so-⋅ 10

4

6.3517 1704 04 × 10 = 6.35 4

5.9554 5417 17 × 10 = 5.95

5

'/$' tottpc := '/$' ccotpc + '/$' cch4tp 8.0063 6304 04 × 10 + '/$' cno-tpc + '/$' cso-tpc = 8.00

$om%&stie 6

$/co$ co$rec rec := ) 0.17 0.1737 37 + 0.00 0.002 2⋅ N* ⋅ Mac = 5.83 5.8302 0261 61 × 10 10

−3

'/$' ccococ := $/co$rec⋅ '/$'co⋅ 10 = 157.417044

5

$4c $4co$ o$re recc = 3.00 3.0059 5996 96 × 10

−3

'/$' cch4co := $4co$rec⋅ '/$'ch4⋅ 10 = 1.803597

−3

'/$' cno-coc := N/-co$rec⋅ '/$'no- ⋅ 10 '/$' cso-coc := /2co$rec⋅ '/$'so-⋅ 10

−3

8

N/-co$rec = 1.195814 × 10 3

3.3482 828 8 × 10 = 3.34

8

/2c /2co$ o$re recc = 3.14 3.1459 5958 58 × 10

4

1.5100 006 6 × 10 = 1.51

4

'/$' totcoc := '/$' ccococ + '/$' cch4co 1.8608 081 1 × 10 + '/$' cno-coc + '/$' cso-coc = 1.86


+ '/$' tottpc + '/$' totcoc = 8.19 '/$' totc := '/$' tote-c + '/$' tottrc 8.1969 6935 35 × 10

Filiera Filiera de carbune carbun e - ardere in pat fluidizat

E-tractie

−3

'/$' ccoe-c3 := $/e-$rec3⋅ '/$'co⋅ 10 = 7.319508

−3

'/$' cch4e-c3 := $4e-$rec3⋅ '/$'ch4⋅ 10 = 190.82955

−3

'/$' cno-e-c3 := N/-e-$rec3⋅ '/$'no-⋅ 10 = 33.848271

−3

'/$' cso-e-c3 := /2e-$rec3⋅ '/$'so-⋅ 10 = 136.836506 '/$' tote-c3 := '/$' ccoe-c3 + '/$' cch4e-c3 + '/$' cno-e-c3 + '/$' cso-e-c3 = 368.833834

ratare "#

−3

'/$' ccotrc3 := $/tr$rec3⋅ '/$'co⋅ 10 = 5.650417

−3

'/$' cch4trc3 := $4tr$rec3⋅ '/$' ch4⋅ 10 = 1.862622

−3

'/$' cno-trc3 := N/-tr$rec3⋅ '/$' no- ⋅ 10 = 27.028097

−3

'/$' cso-trc3 := /2tr$rec3⋅ '/$'so-⋅ 10 = 30.951032 '/$' tottrc3 := '/$' ccotrc3 + '/$' cch4trc3 + '/$' cno-trc3 + '/$' cso-trc3 = 65.492167

ransport

−3

'/$' ccotpc3 := $/tp$rec3⋅ '/$'co⋅ 10

5

6.4661 6156 56 × 10 = 6.46

−3

'/$' cch4tpc3 := $4tp$rec3⋅ '/$' ch4⋅ 10 = 71.581063

−3

4

'/$' cno-tpc3 := N/-tp$rec3⋅ '/$'no-⋅ 10 '/$' cso-tpc3 := /2tp$rec3⋅ '/$'so-⋅ 10

−3

6.0622 2297 97 × 10 = 6.06 4

5.6840 4067 67 × 10 = 5.68

5

'/$' tottpc3 := '/$' ccotpc3 + '/$' cch4tpc3 7.6415 1508 08 × 10 + '/$' cno-tpc3 + '/$' cso-tpc3 = 7.64

$om%&stie 6

$/co$ co$rec rec3 := ) 0.17 0.1737 37 + 0.00 0.002 2⋅ N* ⋅ Mcc = 5.56 5.5646 4613 13 × 10 10

−3

'/$' ccococ3 := $/co$rec3⋅ '/$'co⋅ 10 = 150.244564

−3

'/$' cch4coc3 := $4co$rec3⋅ '/$'ch4⋅ 10 = 1.721419

−3

'/$' cno-coc3 := N/-co$rec3⋅ '/$'no- ⋅ 10 '/$' cso-coc3 := /2co$rec3⋅ '/$'so-⋅ 10

−3

3

3.1957 572 2 × 10 = 3.19

4

1.4412 1256 56 × 10 = 1.44

4

+ '/$' cno-coc3 + '/$' cso-coc3 = 1.77 '/$' totcoc3 := '/$' ccococ3 + '/$' cch4coc3 1.7760 6025 25 × 10 &ezultate globale filiera de carbune ardere in pat fluidizat! 5

'/$' totc3 := '/$' tote-c3 + '/$' tottrc3 7.8234 3454 54 × 10 + '/$' tottpc3 + '/$' totcoc3 = 7.82

"+

Acidificare

$ndicatorul care sta la baza acestei clase de impact poarta denumirea de potential de acidificare5 'P4 7ai 3os se prezinta contributia relativa a poluantilor la aceasta clasa de impact:

A'nh3 := 1.6

+gso2

+gso2

A' no- := 0.5

+gno2

+gnh3

A'so- := 1.2

+gso2 +gso2

Filiera de gaz natural E-tractie

−3

3

A'cno-e-gn := N/e-Nrec⋅ A' no-⋅ 10

= 2.90 2.9050 5029 29 × 10

−3

A'cso-e-gn := /2e-Nrec⋅ A'so-⋅ 10

3

2.5776 7647 47 × 10 = 2.57

3

A'tote-gn := A'cno-e-gn + A'cso-e-gn = 5.48 5.4826 2677 77 × 10

ratare

−3

A'cno-trgn := N/trNrec⋅ A' no- ⋅ 10

−3

A'cso-trgn := /2trNrec⋅ A' so-⋅ 10

3

1.4954 545 5 × 10 = 1.49

4

1.5079 7992 92 × 10 = 1.50

4

A'tottrgn := A'cno-trgn + A'cso-trgn = 1.65 1.6575 7537 37 × 10

ransport

−3

A'cno-tpgn := N/-tpNrec⋅ A'no- ⋅ 10

−3

A'cso-tpgn := /2tpNrec⋅ A' so-⋅ 10

7

6.8315 151 1 × 10 = 6.83

7

= 2.48 2.4848 4803 03 × 10

7

A'tottpgn := A'cno-tpgn + A'cso-tpgn = 9.31 9.3163 6312 12 × 10

$om%&stie 6

N3coNrec := ) 0.137 + 0.004⋅ N* ⋅ M%c = 1.73 1.7385 8585 85 × 10

−3

A'cnh3cogn := N3coNrec⋅ A'nh3⋅ 10

3

2.7817 1736 36 × 10 = 2.78

",

−3

A'cno-cogn := N/-coNrec⋅ A'no-⋅ 10

3

3.4099 9932 32 × 10 = 3.40

6

N/-coNrec = 6.819863 × 10

5

/2c /2co oNr Nrec ec = 3.15 3.1505 0585 85 × 10

−3

A'cso-cogn := /2coNrec⋅ A'so-⋅ 10 = 378.07017 3

A'totcogn := A'cno-cogn + A'cso-cogn + A' cnh3cogn = 6.56 6.5697 9738 38 × 10

7

A'totgn := A'tote-gn + A'tottrgn + A'tottpgn + A'totcogn = 9.31 9.3191 9175 75 × 10

Filiera de carbune - Ardere pulverizata E-tractie

−3

A'cnh3e-c := N3e-$rec⋅ A'nh3 ⋅ 10

3

3.9849 499 9 × 10 = 3.98

−3

A'cno-e-c := N/-e-$rec⋅ A'no- ⋅ 10 = 633.288267

−3

3

A'cso-e-c := /2e-$rec⋅ A' so-⋅ 10

3.5842 4223 23 × 10 = 3.58

3

A'tote-c := A'cnh3e-c + A'cno-e-c + A'cso-e-c = 8.20 8.2025 2501 01 × 10

ratare

−3

3

A'cnh3trc := N3tr$rec⋅ A' nh3⋅ 10

= 1.79 1.7994 9431 31 × 10

−3

A'cno-trc := N/-tr$rec⋅ A'no- ⋅ 10 = 505.685407

−3

A'cso-trc := /2tr$rec⋅ A' so-⋅ 10 = 810.714844 3

A'tottrc := A'cnh3trc + A'cno-trc + A'cso-trc = 3.11 3.1158 5831 31 × 10

ransport

−3

A'cnh3tpc := N3tp$rec⋅ A' nh3⋅ 10

−3

A'cno-tpc := N/-tp$rec⋅ A' no-⋅ 10

−3

A'cso-tpc := /2tp$rec⋅ A'so-⋅ 10

7

2.4445 4551 51 × 10 = 2.44

6

1.1342 4233 33 × 10 = 1.13 6

= 1.48 1.4888 8854 54 × 10

7

A'tottpc := A'cnh3tpc + A' cno-tpc + A'cso-tpc = 2.70 2.7068 686 6 × 10

$om%&stie 3

N3co$rec := ) 0.000121 + 0.000008⋅ N* ⋅ Mac = 6.22 6.2264 6492 92 × 10 10

"-

3

N3co$rec = 6.226492 × 10

−3

A'cnh3coc := N3co$rec⋅ A' nh3⋅ 10 = 9.962388

−3

A'cno-coc := N/-co$rec⋅ A' no-⋅ 10 A'cso-coc := /2co$rec⋅ A'so-⋅ 10

8

N/-co$rec = 1.195814 × 10

4

5.9790 9071 71 × 10 = 5.97

8

−3

/2c /2co$ o$re recc = 3.14 3.1459 5958 58 × 10

5

3.7751 5149 49 × 10 = 3.77

5

A'totcoc := A'cnh3coc + A'cno-coc + A' cso-coc = 4.37 4.3731 3156 56 × 10


A'totc := A'tote-c + A'tottrc + A'tottpc + A'totcoc = 2.75 2.7517 1723 23 × 10

Filiera de carbune - Ardere in pat fluidizat

E-tractie

−3

A'cnh3e-c3 := N3e-$rec3⋅ A'nh3 ⋅ 10

3

3.8034 342 2 × 10 = 3.80

−3

A'cno-e-c3 := N/-e-$rec3⋅ A'no- ⋅ 10 = 604.433406 A'cso-e-c3 := /2e-$rec3⋅ A' so-⋅ 10

−3

3

3.4209 0913 13 × 10 = 3.42

3

A'tote-c3 := A'cnh3e-c3 + A'cno-e-c3 + A'cso-e-c3 = 7.82 7.8287 8766 66 × 10

ratare

−3

A'cnh3trc3 := N3tr$rec3⋅ A' nh3 ⋅ 10

3

1.7174 7442 42 × 10 = 1.71

−3

A'cno-trc3 := N/-tr$rec3⋅ A' no- ⋅ 10 = 482.644585

−3

A'cso-trc3 := /2tr$rec3⋅ A'so-⋅ 10 = 773.775799 3

A'tottrc3 := A'cnh3trc3 + A' cno-trc3 + A'cso-trc3 = 2.97 2.9738 3863 63 × 10

ransport

".

−3

A'cnh3tpc3 := N3tp$rec3⋅ A' nh3⋅ 10

−3

A'cno-tpc3 := N/-tp$rec3⋅ A' no-⋅ 10

−3

7

2.3331 3169 69 × 10 = 2.33

6

1.0825 2553 53 × 10 = 1.08 6

A'cso-tpc3 := /2tp$rec3⋅ A'so-⋅ 10

1.4210 1017 17 × 10 = 1.42

7

A'tottpc3 := A'cnh3tpc3 + A'cno-tpc3 + A'cso-tpc3 = 2.58 2.5835 3526 26 × 10

$om%&stie

3

N3co$rec3 := ) 0.000121 + 0.000008⋅ N* ⋅ Mcc = 5.94 5.9427 2791 91 × 10 10

−3

A'cnh3coc3 := N3co$rec3⋅ A'nh3 ⋅ 10 = 9.508466

−3

A'cno-coc3 := N/-co$rec3⋅ A'no- ⋅ 10

−3

A'cso-coc3 := /2co$rec3⋅ A'so-⋅ 10

4

5.7066 6643 43 × 10 = 5.70 5

3.6031 314 4 × 10 = 3.60

8

N/-c N/-co$ o$re rec3 c3 = 1.14 1.1413 1329 29 × 10

8

/2c /2co$ o$re rec3 c3 = 3.00 3.0026 2617 17 × 10 5

A'totcoc3 := A'cnh3coc3 + A'cno-coc3 + A'cso-coc3 = 4.17 4.1738 3899 99 × 10

7

A'totc3 := A'tote-c3 + A'tottrc3 + A'tottpc3 + A' totcoc3 = 2.62 2.6263 6345 45 × 10

Eutrofizare

E'nh3 := 0.35

+g po43 +gnh3

E'no- := 0.13

+g po43 +gno2

Filiera Filiera de gaz g az natural

"/

E-tractie

−3

E'cno-e-gn := N/-e-$rec3⋅ E'no- ⋅ 10 = 157.152685 E'tote-gn := E'cno-e-gn = 157.152685

ratare

−3

E'cno-trgn := N/-tr$rec3⋅ E'no-⋅ 10 = 125.487592 E'tottrgn := E'cno-trgn = 125.487592 ransport

−3

E'cno-tpgn := N/-tp$rec3⋅ E'no- ⋅ 10

5

2.8146 4638 38 × 10 = 2.81 5

E'tottpgn := E'cno-tpgn = 2.81 2.8146 4638 38 × 10

$om%&stie

−3

E'cnh3cogn := N3co$rec⋅ E'nh3⋅ 10 = 2.179272 E'cno-cogn := N/-co$rec⋅ E'no-⋅ 10

−3

4

1.5545 4558 58 × 10 = 1.55

4

E'totcogn := E'cno-cogn + E'cnh3cogn = 1.55 1.5547 4776 76 × 10

5

E'totgn := E'tote-gn + E'tottrgn + E'tottpgn + E'totcogn = 2.97 2.9729 2942 42 × 10

Filiera de carbune - Ardere pulverizata

E-tractie

−3

E'cnh3e-c := N3e-$rec⋅ E'no-⋅ 10 = 323.780441

−3

E'cno-e-c := N/-e-$rec⋅ E'no-⋅ 10 = 164.654949 E'tote-c := E'cnh3e-c + E'cno-e-c = 488.435391

#0

ratare

−3

E'cnh3trc := N3tr$rec⋅ E'no- ⋅ 10 = 146.203765

−3

E'cno-trc := N/-tr$rec⋅ E'no-⋅ 10 = 131.478206 E'tottrc := E'cnh3trc + E'cno-trc = 277.681971

ransport

−3

E'cnh3tpc := N3tp$rec⋅ E'no-⋅ 10

−3

E'cno-tpc := N/-tp$rec⋅ E'no-⋅ 10

6

1.9861 6198 98 × 10 = 1.98

5

2.9490 9005 05 × 10 = 2.94

6

E'tottpc := E'cnh3tpc + E'cno-tpc = 2.28 2.2810 1098 98 × 10

$om%&stie

−3

E'cnh3coc := N3co$rec⋅ E'no-⋅ 10 = 0.809444

−3

E'cno-coc := N/-co$rec⋅ E'no-⋅ 10

4

1.5545 4558 58 × 10 = 1.55

4

E'totcoc := E'cnh3coc + E'cno-coc = 1.55 1.5546 4639 39 × 10

6

E'totc := E'tote-c + E'tottrc + E'tottpc + E'totcoc = 2.29 2.2974 7411 11 × 10

Filiera de carbune - Ardere in pat fluidizat

E-tractie

−3

E'cnh3e-c3 := N3e-$rec3⋅ E'no-⋅ 10 = 309.027855

−3

E'cno-e-c3 := N/-e-$rec3⋅ E'no- ⋅ 10 = 157.152685

= 466.180541 E'tote-c3 := E'cnh3e-c3 + E'cno-e-c3

#1

ratare

−3

E'cnh3trc3 := N3tr$rec3⋅ E'no-⋅ 10 = 139.542202

−3

E'cno-trc3 := N/-tr$rec3⋅ E'no-⋅ 10 = 125.487592 E'tottrc3 := E'cnh3trc3 + E'cno-trc3 = 265.029795

ransport

−3

E'cnh3tpc3 := N3tp$rec3⋅ E'no- ⋅ 10

−3

E'cno-tpc3 := N/-tp$rec3⋅ E'no- ⋅ 10

6

1.8957 57 × 10 = 1.89

5

2.8146 4638 38 × 10 = 2.81

6

E'tottpc3 := E'cnh3tpc3 + E'cno-tpc3 = 2.17 2.1771 7163 63 × 10

$om%&stie

−3

E'cnh3coc3 := N3co$rec3⋅ E'no-⋅ 10 = 0.772563

−3

E'cno-coc3 := N/-co$rec3⋅ E'no-⋅ 10

4

1.4837 3727 27 × 10 = 1.48

4

E'totcoc3 := E'cnh3coc3 + E'cno-coc3 = 1.48 1.4838 3805 05 × 10

6

E'totc3 := E'tote-c3 + E'tottrc3 + E'tottpc3 + E'totcoc3 = 2.19 2.1927 2733 33 × 10

ETAPA !

7atricea ce contine indicatorii calculati anterior

#2

AW :=

 W'totc

A#'cc

 W'totgn  W' totc3 

A#'cgn '/$' totgn A'totgn E'totgn 'totgn 

'/$' totc

A'totc

E'totc

'totc 



A#'cc3 '/$' totc3 A'totc3 E'totc3 'totc3 

8  2.36 2.3662 6237 37 × 10 10 AW =  2.26 2.2600 0047 47 × 10  8 2.3662 6237 37 × 10  2.36

3.17 3.1711 1167 67 × 10

5

8.19 8.1969 6935 35 × 10

5

1.03 1.0349 4907 07 × 10

5

7.82 7.8234 3454 54 × 10

2.40 2.4073 731 1 × 10

3.02 3.0266 6678 78 × 10

5

2.75 2.7517 1723 23 × 10

7

9.31 9.3191 9175 75 × 10

5

2.62 2.6263 6345 45 × 10

7

2.19 2.1927 2733 33 × 10

A#' := A#'cc 0

A#' := A#'cgn 1

A#' := A#'cc3 2

'/$' := '/$' totc 0

'/$' := '/$' totgn 1

'/$' := '/$' totc3 2

A' := A'totc 0

A' := A'totgn 1

A' := A'totc3 2

E' := E'totc 0

E' := E'totgn 1

E' := E'totc3 2

' := 'totc 0

' := 'totgn 1

' := 'totc3 2

W'min :=

i! r < W'

r ← 10

 6 3.40 3.4018 1819 19 × 10 

20

r ← W'

i

i! r > W'

i

ret&rn r 10

8

W'ma- = 2.26 2.2600 0047 47 × 10

W'min = 2.36 2.3662 6237 37 × 10

A#'min :=

r←0 r ← A#'

i

r ← 10

20

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2 i! r < A#'

r ← A#' i

i

i! r > A#'

i

ret&rn r

ret&rn r

5

A#'min = 2.40 2.4073 731 1 × 10

5

A#'ma- = 3.17 3.1711 1167 67 × 10

'/$' ma- :=

8

6

i

ret&rn r

A#'ma- :=

6

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2 i

3.96 3.9689 8999 99 × 10

2.97 2.9729 2942 42 × 10

W' := W'totc3 2

r ← W'

5

7

W' := W'totgn 1

r←0

3.56 3.5642 4218 18 × 10 

2.29 2.2974 7411 11 × 10

W' := W'totc 0

W'ma- :=

6

7

'/$' min :=

r←0

i

20

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2 r ← '/$'

r ← 10

i! r < '/$'

r ← '/$' i

i

i! r > '/$'

i

ret&rn r

ret&rn r 7

'/$' ma- = 1.03 1.0349 4907 07 × 10

5

'/$' min = 7.82 7.8234 3454 54 × 10

#"

A'ma- :=

A'min :=

r←0

i

i! r < A'

r ← A' i

7

A'ma- = 9.31 9.3191 9175 75 × 10

E'min :=

r←0

i

i

i

5

E'min = 2.97 2.9729 2942 42 × 10

6

E'ma- = 2.29 2.2974 7411 11 × 10

'min :=

r←0 r ← '

i

i! r < '

r ← ' i

W' 0 W'n0 := 1 − = 0.98953 W'ma-

A#'

0

=0 A#'n0 := 1 − A#'ma'/$' 0 '/$' n0 := 1 − = 0.920795 '/$' ma-

i

6

W'

1

W'n1 := 1 −

W'ma-

= 0.7

=0

' 0 'n0 := 1 − = 0.99102 'ma-

=0

A#' 1 = 0.240876 A#'n1 := 1 − A#'ma'/$' '/$' n1 := 1 −

A' n1 := 1 −

1

'/$' ma-

A'

E'

E'ma-

i! r > '

'min = 3.40 3.4018 1819 19 × 10

8

'ma- = 3.96 3.9689 8999 99 × 10

E'n0 := 1 −

i

ret&rn r

ret&rn r

0

20

r ← 10

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2

A'ma-

i

ret&rn r

ret&rn r

A'n0 := 1 −

20

r ← E' i! r > E'

r ← E' i! r < E'

0

r ← 10

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2

A'

i

A'min = 2.62 2.6263 6345 45 × 10

7

'ma- :=

i! r > A'

i

ret&rn r

ret&rn r

E'ma- :=

20

!or i ∈ 0 , 1 , 2

!or i ∈ 0 , 1 , 2 r ← A'

r ← 10

1

A'ma-

= 0

=0

E' 1 E'n1 := 1 − = 0.870596 E'ma' 'n1 := 1 −

1

'ma-

=0

W' 2 W'n2 := 1 − = 0.9895 W'ma-

A#' 2 = 0.04556 A#'n2 := 1 − A#'ma'/$' 2 '/$' n2 := 1 − = 0.924 '/$' ma-

A' 2 A' n2 := 1 − = 0.718178 A'ma-

E' 2 E'n2 := 1 − = 0.045564 E'ma' 2 'n2 := 1 − = 0.99142 ' ma-

##

9  valoarea maxima 8 valoarea minima a aceluiasi criteriu

W' := W'n0 5

W' := W'n1 6

W' := W'n2 7

A#' := A#'n0 5

A#' := A#'n1 6

A#' := A#'n2 7

'/$' := '/$' n0 5

'/$' := '/$' n1 6

'/$' := '/$' n2 7

A' := A'n0 5

A' := A' n1 6

A' := A'n2 7

E' := E'n0 5

E' := E'n1 6

E' := E'n2 7

' := 'n0 5

' := 'n1 6

' := 'n2 7

δW' :=

δA' :=

r←0

r←0 !or i ∈ 5 , 6 , 7

!or i ∈ 5 , 6 , 7 r ← W'

i

r ← A'

i! r < W'

i

i

i! r < A'

i

ret&rn r

ret&rn r

δA' = 0.72

δW' = 0.99

δA#' :=

δE' :=

r←0

!or i ∈ 5 , 6 , 7

!or i ∈ 5 , 6 , 7 r ← A#'

i

i! r < A#'

r ← E' i! r < E' i

i

i

ret&rn r

ret&rn r

δA#' = 0.24

δ'/$' :=

r←0

δE' = 0.87 δ' :=

r←0

r←0 !or i ∈ 5 , 6 , 7

!or i ∈ 5 , 6 , 7 r ← '/$'

i

r ← ' i! r < '/$'

i

i

i! r < '

i

ret&rn r

ret&rn r

δ'/$' = 0.92

AWn :=

δ' = 0.99

 W'n0

A#'n0 '/$' n0 A'n0 E'n0 'n0 

 W'n1  W' n2 

A#'n1 '/$' n1 A'n1 E'n1 'n1 



A#'n2 '/$' n2 A'n2 E'n2 'n2 

#+

 0.99 AWn =

0

  0.99

0

0.92

0.7

0

0.24

0

0

0.87

0.99  0



0.05 0.92 0.72 0.05 0.99 

W'

A#'

'/$'

A'

E'

'

1

W'n0 = 0.98953

A#'n0 = 0

2

W'n1 = 0

A#'n1 = 0.240876 '/$' n1 = 0

3

W'n2 = 0.98953

A#'n2 = 0.045564 '/$' n2 = 0.924404 A' n2 = 0.718178 E'n2 = 0.045564 'n2 = 0.991429

'

5

δ

δW' = 0.99

4

δA#' = 0.24

'/$' n0 = 0.920795 A' n0 = 0.704725 E'n0 = 0 A' n1 = 0

'n0 = 0.99102

E'n1 = 0.870596 'n1 = 0

3

2

1

4

δ'/$' = 0.92

δA' = 0.718

δE' = 0.871

δ' = 0.991

Calculul matricii de c oncordanta oncordanta $n prima faza indicele de concordanta se va calcula pentru a calcula matricea de concordanta: Ci;
?P ) P=ai5a;! 8 suma ponderilor criteriilor pentru care actiunea a i5 este mai buna decat actiunea a; Pai5a;! 8 suma ponderilor criteriilor criteriilor pentru care cele doua actiuni sunt ecivalente P0

P8ai5a;! 8 suma ponderilor criteriilor pentru care actiunea a ; este mai buna decat actiunea ai

P)ai5a;!P=ai5a;!=P8ai5a;!=Pai5a;! 88@@ P) Pentru calculul de c oncordanta oncordanta ne uitam in matricea indicatorilor ' := 5 + 4 + 3 + 2 + 1 + 4 = 19

Calculul indicilor de c oncordanta: oncordanta: 14 C12 F15F2! Calculam P=8888@notat: 8888@notat: Pplus

#,

' p&s1 :=

r←0

'ega1 :=

r←0

r ← r + 5 i! W'n0 > W'n1

r ← r + 5 i! W'n0 " W'n1

r ← r + 4 i! A#'n0 > A#'n1

r ← r + 4 i! A#'n0 " A#'n1

r ← r + 3 i! '/$' n0 > '/$' n1

r ← r + 3 i! '/$' n0 " '/$' n1

r ← r + 2 i! A'n0 > A' n1

r ← r + 2 i! A' n0 " A' n1

r ← r + 1 i! E'n0 > E'n1

r ← r + 1 i! E'n0 " E'n1

r ← r + 4 i! 'n0 > 'n1

r ← r + 4 i! 'n0 " ' n1

ret&rn r

ret&rn r

' p&s1 = 14

'ega1 = 0 ' p&s1 + 'ega1

$12 :=

'

= 0.736842

24 C1" F15F" ! Calculam P=8888@notat: 8888@notat: Pplus ' p&s2 :=

r←0

'ega2 :=

r←0

r ← r + 5 i! W'n0 > W'n2

r ← r + 5 i! W'n2 " W'n2

r ← r + 4 i! A#'n0 > A#'n2

r ← r + 4 i! A#'n0 " A#'n2

r ← r + 3 i! '/$' n0 > '/$' n2

r ← r + 3 i! '/$' n0 " '/$' n2

r ← r + 2 i! A' n0 > A' n2

r ← r + 2 i! A'n0 " A' n2

r ← r + 1 i! E'n0 > E'n2

r ← r + 1 i! E'n0 " E'n2

r ← r + 4 i! 'n0 > ' n2

r ← r + 4 i! 'n0 " 'n2

ret&rn r

ret&rn r

' p&s2 = 0 $13 :=

'ega2 = 5 ' p&s2 + 'ega2 '

= 0.263158

"4 C12 F25F1! Calculam P=8888@notat: 8888@notat: Pplus ' p&s3 :=

r←0

'ega3 :=

r←0

r ← r + 5 i! W'n1 > W'n0

r ← r + 5 i! W'n1 " W'n0

r ← r + 4 i! A#'n1 > A#'n0

r ← r + 4 i! A#'n1 " A#'n0

r ← r + 3 i! '/$' n1 > '/$' n0

r ← r + 3 i! '/$' n1 " '/$' n0

r ← r + 2 i! A'n1 > A' n0

r ← r + 2 i! A' n1 " A' n0

r ← r + 1 i! E'n1 > E'n0

r ← r + 1 i! E'n1 " E'n0

r ← r + 4 i! 'n1 > 'n0

r ← r + 4 i! 'n1 " ' n0

ret&rn r

ret&rn r

' p&s3 = 5

'ega3 = 0 #-

' p&s3 + 'ega3

$21 :=

'

= 0.263158

#4 C2" F25F"! Calculam P=8888@notat: 8888@notat: Pplus ' p&s4 :=

r←0

'ega4 :=

r←0

r ← r + 5 i! W'n1 > W'n2

r ← r + 5 i! W'n1 " W'n2

r ← r + 4 i! A#'n1 > A#'n2

r ← r + 4 i! A#'n1 " A#'n2

r ← r + 3 i! '/$' n1 > '/$' n2

r ← r + 3 i! '/$' n1 " '/$' n2

r ← r + 2 i! A'n1 > A' n2

r ← r + 2 i! A' n1 " A' n2

r ← r + 1 i! E'n1 > E'n2

r ← r + 1 i! E'n1 " E'n2

r ← r + 4 i! 'n1 > 'n2

r ← r + 4 i! 'n1 " ' n2

ret&rn r

ret&rn r

' p&s4 = 5 $23 :=

'ega4 = 0 ' p&s4 + 'ega4 '

= 0.263158

+4 C"1 F"5F1 ! Calculam P=8888@notat: 8888@notat: Pplus ' p&s5 :=

r←0

'ega5 :=

r←0

r ← r + 5 i! W'n2 > W'n0

r ← r + 5 i! W'n2 " W'n0

r ← r + 4 i! A#'n2 > A#'n0

r ← r + 4 i! A#'n2 " A#'n0

r ← r + 3 i! '/$' n2 > '/$' n0

r ← r + 3 i! '/$' n2 " '/$' n0

r ← r + 2 i! A' n2 > A' n0

r ← r + 2 i! A'n2 " A' n0

r ← r + 1 i! E'n2 > E'n0

r ← r + 1 i! E'n2 " E'n0

r ← r + 4 i! 'n2 > ' n0

r ← r + 4 i! 'n2 " 'n0

ret&rn r

ret&rn r

' p&s5 = 14 $31 :=

'ega5 = 5 ' p&s5 + 'ega5 '

=1

,4 C"2 F" 5F2! Calculam P=8888@notat: 8888@notat: Pplus

#.

' p&s6 :=

r←0

'ega6 :=

r←0

r ← r + 5 i! W'n2 > W'n1

r ← r + 5 i! W'n2 " W'n1

r ← r + 4 i! A#'n2 > A#'n1

r ← r + 4 i! A#'n2 " A#'n1

r ← r + 3 i! '/$' n2 > '/$' n1

r ← r + 3 i! '/$' n2 " '/$' n1

r ← r + 2 i! A'n2 > A' n1

r ← r + 2 i! A' n2 " A' n1

r ← r + 1 i! E'n2 > E'n1

r ← r + 1 i! E'n2 " E'n1

r ← r + 4 i! 'n2 > 'n1

r ← r + 4 i! 'n2 " ' n1

ret&rn r

ret&rn r

' p&s6 = 14 $32 :=

'ega6 = 0 ' p&s6 + 'ega6 '

= 0.736842

7atricea de concordanta:

1

2

−−−

1

3

$12 = 0.736842

$13 = 0.263158 $23 = 0.263158

2

$21 = 0.263158

−−−

3

$31 = 1

$32 = 0.736842

−−−

Calculul matricii de nondiscordanta: nondiscordanta:

6e vor calcula indicii dupa cum urmeaza:

14

D12 F15F2! 'min&s1 :=

r←0

(

) ( ) r ← A#'n1 − A#'n0 i! r < (A#'n1 − A#'n0) ∧ ( A#'n0 < A#'n1) r ← '/$' n1 − '/$' n0 i! r < ('/$' n1 − '/$' n0) ∧ ( '/$' n0 < '/$' n1) r ← A' n1 − A' n0 i! r < ( A'n1 − A'n0) ∧ ( A' n0 < A' n1) r ← E'n1 − E'n0 i! r < (E'n1 − E'n0) ∧ ( E'n0 < E'n1) r ← ' n1 − ' n0 i! r < (' n1 − 'n0) ∧ ( 'n0 < ' n1) r ← W'n1 − W'n0 i! r < W'n1 − W'n0 ∧ W'n0 < W'n1

ret&rn r 'min&s1 = 0.871

#/

α1 :=

r←0

( ) ( ) r ← δA#' i! r < ( A#'n1 − A#'n0) ∧ ( A#'n0 < A#'n1) r ← δ'/$' i! r < ( '/$' n1 − '/$' n0) ∧ ( '/$' n0 < '/$' n1) r ← δA' i! r < ( A'n1 − A' n0) ∧ ( A' n0 < A'n1) r ← δE' i! r < ( E'n1 − E'n0) ∧ ( E'n0 < E'n1) r ← δ' i! r < (' n1 − ' n0) ∧ ( ' n0 < 'n1) r ← δW' i! r < W'n1 − W'n0 ∧ W'n0 < W'n1

ret&rn r

α1 = 0.871

#12 :=

24

'min&s1

α1

=1

D1" F15F"! 'min&s2 :=

r←0

(

) ( ) r ← A#'n2 − A#'n0 i! r < (A#'n2 − A#'n0) ∧ ( A#'n0 < A#'n2) r ← '/$' n2 − '/$' n0 i! r < ('/$' n2 − '/$' n0) ∧ ( '/$' n0 < '/$' n2) r ← A'n2 − A' n0 i! r < (A'n2 − A' n0) ∧ ( A'n0 < A' n2) r ← E'n2 − E'n0 i! r < (E'n2 − E'n0) ∧ ( E'n0 < E'n2) r ← ' n2 − 'n0 i! r < (' n2 − 'n0) ∧ ( 'n0 < 'n2) r ← W'n2 − W'n0 i! r < W'n2 − W'n0 ∧ W'n0 < W'n2


α2 :=

r←0

( ) ( ) r ← δA#' i! r < (A#'n2 − A#'n0) ∧ ( A#'n0 < A#'n2) r ← δ'/$' i! r < ('/$' n2 − '/$' n0) ∧ ( '/$' n0 < '/$' n2) r ← δA' i! r < (A'n2 − A' n0) ∧ ( A' n0 < A' n2) r ← δE' i! r < ( E'n2 − E'n0) ∧ ( E'n0 < E'n2) r ← δ' i! r < ( ' n2 − 'n0) ∧ ( ' n0 < 'n2) r ← δW' i! r < W'n2 − W'n0 ∧ W'n0 < W'n2

ret&rn r

α2 = 0.241

#13 :=

"

'min&s2

α2

= 0.189

D21 F25F1!

+0

'min&s3 :=

r←0

(



α3 :=

r←0


ret&rn r

α3 = 0.991

#21 :=

#4

'min&s3

α3

= 0.9996

D2" F25F"! 'min&s4 :=

r←0

(



+1

α4 :=

r←0


ret&rn r

α4 = 0.991

#23 :=

+4

'min&s4

α4

=1

D"1 F"5F1! 'min&s5 :=

r←0

(


ret&rn r 'min&s5 = 0

α5 :=

r←0


ret&rn r

α5 = 0

#31 :=

,4

'min&s5

α5

=

D"2 F"5F2!

+2

'min&s6 :=

r←0

(



α6 :=

r←0


ret&rn r

α6 = 0.871

#32 :=

'min&s6

α6

= 0.948

7atricea de nonconcordanta: nonconcordanta:

1 1

2

−−−

3

#12 = 1

#13 = 0.189 #23 = 1

2

#21 = 0.9996

−−−

3

#31

#32 = 0.948

−−−

+"

6

× 10

+#

6

3 × 10

++

3

4

404

9

+,

209808994-Energie-si-Mediu-Proiect-Dinca.pdf

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