calcul 2011

7/21/2019 Calcul 2011

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Dimensionare sistem de purificare a apei prin osmoza inversa - DEBIT APA FILTRATA IMPUS

Debit apa filtrata !"!!Concentratie poluant in apa bruta #$!!!"!!Concentratie poluant in apa filtrata !!"!!

Grad de rejectie membrana GRM %&"!!Grad de recuperare apa GRA '!"!!

Dimensionare sistem de purificare a apei prin osmoza inversa - DEBIT APA PURIFI(ATA IMP

Concentratie poluant in permeat 50.00

Debit recirculat 3.16Debit permeat 16.84

SISTEM RO

11.23 mc/h

950.00 mg/l

Dimensionare sistem de purificare a apei prin osmoza inversa - DEBIT APA BRUTA IMPUS

Debit apa bruta )&"!!Concentratie poluant in apa bruta *+!"!!Concentratie poluant in apa filtrata &!"!!Grad de rejectie membrana GRM %&"!!

Grad de recuperare apa GRA '!"!!

Concentratie poluant in permeat 1 .00

Debit alimentare !i!tem R" #$.3Debit apa filtrata 63.#5

SISTEM RO

% f

C ini.poluant

C fin.poluant

C permeat

% #

% p

% b

C ini.poluant

C fin.poluant

C permeat

% 1

% f

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13.33 mc/h

323.00 mg/l

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mc,-m ,lm ,l

//

S

m ,l

mc,-mc,-

28.07 mc/h 31.23 mc/h

1,000.00 mg/l 1,000.00 mg/l

3.16 mc/h

1,000.00 mg/l

16.84 mc/h 20.00 mc/h

50.00 mg/l 200.00 mg/l

mc,-m ,lm ,l/

/

m ,l

mc,-mc,-

29.37 mc/h 75.00 mc/h

340.00 mg/l 340.00 mg/l

45.63 mc/h

340 00 /l

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17.62 mc/h 63.25 mc/h

17.00 mg/l 250.00 mg/l

S

mc,-m ,lm ,l//

m ,l

16.67 mc/h 32.33 mc/h

333.44 mg/l 333.44 mg/l

15.66 mc/h

333.44 mg/l

10.00 mc/h 25.66 mc/h

16.67 mg/l 210.00 mg/l

S DEBIT APA ,BRUTA, IMPUS

mc,-mc,-m ,l//

m ,l

33.33 mc/h 75.00 mc/h

340.00 mg/l 340.00 mg/l

41.67 mc/h

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20.00 mc/h 61.67 mc/h

17.00 mg/l 235.24 mg/l

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Cantitate ' rolo 2litri #3Debit 2mc,- 0.6 1.0

uprafata filtrare2mp 0.05Debit re!palare,)imp 374 mc,- 215G'M ,#0 6 minute

Greutate 2 5Dimen!iuni 2mm 9 l - 300 300 1800Garantie # ani :

(c-i;alent fier 2m ,l < 1 continut =e 2m ,l > # continut M 2m ,l

Determinarea ;ite?ei de filtrare pe ba?a ec-i;alentului de fier

uprafata de filtrare nece!ara2mp < Debit2mc,- , @ite?a de filtrare 2m,-nter;alul de pB al apei 675 $70

@olum liber min. 40/ din inaltimea filtrului.

(c-i;alent fier @ite?a de filtrare0.# m ,l #0 m,-

0.5 m ,l 18 m,- 1.0 m ,l 15 m,- 1.5 m ,l 1# m,-

#.0 m ,l 10 m,-

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(./STA/TE

Factor de si0uranta #!12ipoc3orit +1 *4"!!2ipoc3orit # 1 #+!"!!

(ontor cu impu3suri #5o3um in6ectie !")%/umar de in6ectii #'!

5ARIABILE

De7it apa # "'/umar ore functionare !p2 )

(oncentratie de amoniu " +&(oncentratie de fier !"&&*(oncentratie de man0an !"!!!(oncentratie 8idro0en su3furat !"!!!(oncentratie su7stante or0anice !"!!!

(AL(UL

(a3cu3 necesar de c3or Cantitate de clor , amoniu 1 .$6Cantitate de clor , fier 0.3$Cantitate de clor , man an 0.00Cantitate de clor , -idro en !ulfurat 0

Cantitate de clor , !ub!tante or anice 0.00Cantitate de clor totala 2teoretic #4"*&

Cantitate de clor totala 2real !"#4Cantitate de clor totala 2real "!#4

Cantitate de clor totala 2real !"#4

Cantitate totala orara de clor &+" %

(L.R LI(2ID - PRE(L.RI/ARE

Con!um orar de -ipoclorit 1#/ #"4Con!um ?ilnic de -ipoclorit 1#/ *'"**

@olum -ipoclorit 1#/ 14.4#@olum -ipoclorit 1#/ 14.4#

umar injectii #%

umar de injectii orar #3$4umar de injectii minut 40

=rec;enta impul!uri receptionate 1 imp,

umar ma injectii la frec;enta calculata 6.1$04 61$

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9a fiecare 4"&)#+ 4&)#

(L.R 9A:.S - PRE(L.RI/ARE

Cantitate clor intr o butelie de clor 50

!

+tili?are butelii de clor 0.00+tili?are butelii de clor 0.00@olum de apa clorinat 0.00

REA(T.R DE (L.RI/ARE

@olum minim ;a! de reactie 1#.60

9RUP DE P.MPARE DE PR.(ES

umar de pompe 21A>1R #.00Debit per pompa 1#.60're!iune rup de pompare 3.50

FILTRU (U (ARBU/E A(TI5

Ina3time strat fi3trant #"

umar de filtre 3Timp de contact *

@ite?a de parcur ere !trat filtrant #4.00

ectiunea de cur ere filtrului cu carbune acti; 0.18Diametru3 fi3tru3ui cu car7une activ !"+)

(L.R LI(2ID +1 - P.ST(L.RI/ARE

Do?a de clor dorita in apa !"&

Debit apa # "'Cant. Cl# '"*

Cant. Cl# , ml -ipoclorit 4/ 0.0380Cant. Cl# , l -ipoclorit 4/ 38

Cant. nece!ara -ipoclorit 4/ 0.013#Cant. nece!ara -ipoclorit 4/ 1.3158

umar injectii teoretic 1.6656umar injectii real 1.83#1

/umar in6ectii setat

Debit apa 1#.6

/ecesar 7ute3ii de c3or NOTA: din 1 buc. butelie de clor 50 Kg se pot extrage maxim 900 g/h clor

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Con!um orar -ipoclorit 0.1

(L.R LI(2ID # 1 - P.ST(L.RI/ARE

Cant. Cl# , ml -ipoclorit 1#/ 0.1400Cant. Cl# , l -ipoclorit 1#/ 140

Cant. nece!ara -ipoclorit 1#/ 0.0036Cant. nece!ara -ipoclorit 1#/ 0.35 1

umar injectii teoretic 0.45#1umar injectii real 0.4$ 3

/umar in6ectii setat Err;&!

Debit apa 1#.6Con!um orar -ipoclorit 45.00Con!um orar -ipoclorit 0.05

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0(3 3 8ipoc3orit0(3 3 8ipoc3orit 150

imp" #!! 3 m3 in6" R'G603in6" min R'G603

mc 88

m0 3m0 3m0 3m0 3m0 3

m Cl#,l apa 4 4"!!m Cl#,l apa !") !"'+m Cl#,l apa #"& #"*!m Cl#,l apa "# "!4 <p2 =4> sau 4"+ <p2 ?4>

m Cl#,l apa "&m Cl#,l apa

m Cl#,l apa Cl#,100 l apa

Cl#,mc apa

0 (3 8

l -ipoclorit , -l -ipoclorit , ?i

ml -ipoclorit , 100 l apaml -ipoclorit , impul!

inj.,100 litri

inj,orainj,min "E

#8.5 14#85 14 !ec

inj "E

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!ecunde !e reali?ea?a #% injectii de -ipoclorit

E

7uc

ore?ilemc

mc

bucmc,-bari

m Ina3time strat fi3trant #"

buc Diametru3 fi3tru3ui cu car7une activ #"'!mim ectiunea de cur ere filtrului cu carbune acti; #.01

m,- @ite?a de parcur ere !trat filtrant #.0$

mp Timp de contact *+"+)m

m Cl#,l apa

mc,-,-

Cl# , ml !ol.m Cl# , ml !ol.

ml -ipoclorit , l apaml -ipoclorit , 100 l apa

inj. , 100 l apainj. , 100 l apa

in6" #!! 3 apa

mc,-

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l -ipoclorit , -


ml -ipoclorit , l apaml -ipoclorit , 100 l apa

inj. , 100 l apainj. , 100 l apain6" #!! 3 apa

mc,-ml -ipoclorit , -l -ipoclorit , -

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#+"+ ml de -ipoclorit

m

mimmp

m,-

min

pt a a;ea concentratia de 0.5 m Cl# , l apapt a a;ea concentratia de 0.5 m Cl# ,100 l apa

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1 pm,!F.ft #.444 4$$#4 mc,2mp -5 pm 1.1356#35 mc,-

FU/(TI./ARE

De7it 30.000 mc,-Diametru recipient 1.600 mSectiune de cur0ere #.010 mp5iteza cur0ere 14.$#8 mc,2mp - '"## gpm/sq.ft

Ina3time strat fi3trant 30 in * RMIna3time strat fi3trant 6.# cmIna3time spatiu 3i7er 38.1 cm

38.10 cm H" A 9 *(RA

10.00 cm Carbune

litri 455.81 6.#0 cm * RM

#0.00 cm C+AR)#++"*! cm

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SPALARE I/5ERSA

De7it spa3are inversa 4$.13 mc,-Diametru recipient 1.600 mSectiune de cur0ere #.010 mp5iteza spa3are inversa #4.44 mc,2mp - #! gpm/sq.ft

1ppm TDS ≈ 2 µS/cm

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#8.31685 0.## 1#4

Mode3 /o"@ Media Service F3o Rate@@ Bac(u" ft" 3itri 9PM mc 8 9PM

I M= 44' 0.3 8.50 1.3 0.30

I M= 844' 0.5 14.16 1. 0.3$I M= $40' 0.6 16.$$ #.# 0.50 1#I M= 1040' 1 #8.3# #. 0.61 1I M= 1054' 1 #8.3# #. 0.61 1I M= 1#5#' 1.5 4#.48 3.$ 0.8$ 1I M= 1354' # 56.63 4.6 1.04 #5I M= 1465' #.5 0. $ 5.3 1.#0 #5I M= 1665' 3 84.$5 1.5$ 30I M= #16#' 4 113.# 1# #. 3 4$I M= #4 #' 6 16$.$0 15. 3.5 60

Tan dia" Tan dia" Supraf" Fi3trare De7itmm in" mp mc 8

36 0.65635$$ 6 8.0#1600 6#.$$ #.00$6000000 #4.56

5 pm per !F. ft. of media i! t-e be!t de!i n condition for filtration. *ac Ja!- floJ rate ba!ed o

1 pm,!F.ft #.444 4$$#4 mc,2mp -5 pm,!F.ft 1#.##3 4$6# mc,2mp -

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0.## 1#4

as8@@ Tan Size Pipe Size Tan dia" Supraf" Fi3trare De7itmc 8 Dia"C 2"C in" in" mp mc 81.5$ K 44 L 0.0#48160 $4 0.30

1.5$ 8 K 44 1 8 0.03#41#8384 0.40#. 3 $ K 40 1 $ 0.0410##4$86 0.503.86 10 K 40 1 10 0.0506450600 0.6#3.86 10 K 54 1 10 0.0506450600 0.6#3.86 1# K 5# 1 1# 0.0 #$#88864 0.8$5.68 13 K 54 1 13 0.0855$01514 1.055.68 14 K 65 1 14 0.0$$#6431 6 1.#16.81 16 K 65 1.5 16 0.1#$6513536 1.58

11.13 #1 K 6# 1.5 #1 0.##3344 146 #. 313.63 #4 K # # #4 0.#$1 155456 3.5

n #5 p!i pre!!ure drop

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'er-idrol 30/ **! "#,l !ol.'er-idrol 15/ ##& "#,l !ol.@olum injectie !"&# ml,inj.Caracteri!tica contor #"!! imp , 100 litri

Debit apa '!"!! mc,-Durata funct. ?ilnic !"!! -

Con!um ?ilnic de apa 17#00.00 mc,?i

Conc. fier "*!!! m ,lConc. man an !"#+&! m ,l

Cantitate de o i en , fier 0.35 m "#,l apa 2 0.143 0.15Cantitate de o i en , man an 0.05 m "#,l apa 2 0.#86 0.35

Cant. totala teoretica de o i en 0.40 m "#,l apa

Cant. totala reala de o i en 0.4$ m "#,l apaCant. totala reala de o i en 0.4$ "#,mc apa

Cant. total ?ilnica de o i en 5$3.63 "#,?i

Cant. totala !ol per-idrol 15/ 5.16# l !ol. , ?i

Con!um per-idrol , mc apa 0.00430 l !ol.,mcCon!um per-idrol , mc apa 4.30163 ml !ol , mcCon!um per-idrol , -l apa 0.43016 ml !ol , 100 l

umar injectii 0.84 inj. , 100 litri

umar injectii 0.84346 inj.,imp./umar in6ectii setat # in6" #!! 3 apa

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(./STA/TE

Factor de si0uranta #!!1

(onc" vo3umetrica . in aer !"%+)1Densitate o i0en #"+ %! 0 mc

5ARIABILE

De7it apa #4 mc 8/umar ore functionare + 8

(oncentratie de fier # m0 3(oncentratie de man0an # m0 3

(AL(UL

(a3cu3 necesar de o i0enCantitate de o i en , fier 0.14 m "#,l apa !"#+*Cantitate de o i en , man an 0.#$ m "#,l apa !" 4'Cantitate totala de o i en 2teoretic !"+* m "#,l apaCantitate totala de o i en 2teoretic !"+* "#,mc apa

@olumul de o i en total 0.00030 mc "#,mc apa

@olumul de aer nece!ar 0.00143 mc aer,mc apa

Debitul de aer nece!ar 2teoretic 0.0#580 mc aer,-

Debitul de aer nece!ar 2real 0.0515$ mc aer,-

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Perox ! Gater and aste ater ca3u3ation manua3 - Second edition - S8un Dar Lin

1 m =e < 0.61 m pero id 50/ 1.01 m pero id 30/1 m Mn < 1.#4 m pero id 50/ #.06 m pero id 30/

Den!itate < 1.463 ,cm3

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Debit 0.000 mc,-Debit 1$.444 l,!

Diametru Suprafata 5iteza naltime !trat filtrant 1.00 m impuinch m mp mc/(mp*h) Diametru recipient metalic 1.30 m impu!

0.1 8 0.0#48 #78#0. 5#8 0.#03 0.03#4 #715$.638 Debit apa 40 mc,- ;ariabil

10 0.#54 0.0506 1738#.1681# 0.305 0.0 #$ $5$.83$ uprafata de filtrare 1.3#6 mp calculat13 0.330 0.0856 81 .851 @ite?a de filtrare 30.151 mc,2mp - calculat14 0.356 0.0$$3 05.188 )imp parcur ere !trat 1.$$ min calculat16 0.406 0.1#$ 53$.$1018 0.45 0.1641 4#6.5$5#1 0.533 0.##33 313.41#4 0.610 0.#$1 #3$.$6030 0. 6# 0.4558 153.5 436 0.$14 0.6564 106.64$4# 1.06 0.8$34 8.35448 1.#1$ 1.166$ 5$.$$0

#.400 4.5#3$ 15.4 3

1 pm,!F.ft #.444 4$$#4 mc,2mp -'"* % 15.4 3

@ite?a 10.000 mc,2mp -

De7it Aria Diametrumc/h mp m inch0.50 0.050 0.#5#4 $.$361.00 0.100 0.356$ 14.05##.00 0.#00 0.5048 1$.8 #

3.00 0.300 0.618# #4.3384.00 0.400 0. 138 #8.1045.00 0.500 0. $81 31.4#16.00 0.600 0.8 43 34.4#0

.00 0. 00 0.$443 3 .1 88.00 0.800 1.00$5 3$. 44$.00 0.$00 1.0 0 4#.155

10.00 1.000 1.1#8 44.43611.00 1.100 1.1838 46.6041#.00 1.#00 1.#364 48.6

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13.00 1.300 1.#86$ 50.66414.00 1.400 1.3355 5#.515.00 1.500 1.38#3 54.4##

@ite?a 40.000 mc/(mp*h) @ite?a 1 .113 mc/(mp*h)

Diametru Suprafata De7it Diametru Suprafata De7itinch m mp mc/h inch m mp mc/h

0.1 8 0.0#48 0.$$ 0.1 8 0.0#48 0.4#8 0.#03 0.03#4 1.30 8 0.#03 0.03#4 0.55

10 0.#54 0.0506 #.03 10 0.#54 0.0506 0.81# 0.305 0.0 #$ #.$# 1# 0.305 0.0 #$ 1.#513 0.330 0.0856 3.4# 13 0.330 0.0856 1.4614 0.356 0.0$$3 3.$ 14 0.356 0.0$$3 1. 016 0.406 0.1#$ 5.1$ 16 0.406 0.1#$ #.##18 0.45 0.1641 6.56 18 0.45 0.1641 #.81#1 0.533 0.##33 8.$3 #1 0.533 0.##33 3.8##4 0.610 0.#$1 11.6 #4 0.610 0.#$1 4.$$30 0. 6# 0.4558 18.#3 30 0. 6# 0.4558 .8036 0.$14 0.6564 #6.#5 36 0.$14 0.6564 11.#34# 1.06 0.8$34 35. 4 4# 1.06 0.8$34 15.#$48 1.#1$ 1.166$ 46.6 48 1.#1$ 1.166$ 1$.$

@ite?a 10.000 mc/(mp*h)

Diametru Suprafata De7itinch m mp mc/h

0.1 8 0.0#48 0.#48#8 0.#03 0.03#4 0.3#41

10 0.#54 0.0506 0.50651# 0.305 0.0 #$ 0. #$313 0.330 0.0856 0.855$14 0.356 0.0$$3 0.$$#6

16 0.406 0.1#$ 1.#$6518 0.45 0.1641 1.640$#1 0.533 0.##33 #.#334#4 0.610 0.#$1 #.$1 #30 0. 6# 0.4558 4.558136 0.$14 0.6564 6.56364# 1.06 0.8$34 8.$338

#"'!! "!!%' !"#

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5iteza 10.000 mc,2mp - 5iteza #0.000 mc,2mp - 5itezaDiametru uprafata Debit Diametru uprafata Debit Diametru

inc- m mp mc,- inc- m mp mc,- inc- m8 0.#03 0.03#4 0.3#4 8 0.#03 0.03#4 0.648 8 0.#03

10 0.#54 0.0506 0.506 10 0.#54 0.0506 1.013 10 0.#5413 0.330 0.0856 0.856 13 0.330 0.0856 1. 1# 13 0.33014 0.356 0.0$$3 0.$$3 14 0.356 0.0$$3 1.$85 14 0.35616 0.406 0.1#$ 1.#$ 16 0.406 0.1#$ #.5$3 16 0.40618 0.45 0.1641 1.641 18 0.45 0.1641 3.#8# 18 0.45#1 0.533 0.##33 #.#33 #1 0.533 0.##33 4.46 #1 0.533#4 0.610 0.#$1 #.$1 #4 0.610 0.#$1 5.834 #4 0.61030 0. 6# 0.4558 4.558 30 0. 6# 0.4558 $.116 30 0. 6#36 0.$14 0.6564 6.564 36 0.$14 0.6564 13.1# 36 0.$14

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Recipient Diametru Suprafata

m m" mc/h mc/h

0844 0.#04 0.03#6$ 0.33 0.651054 0.#53 0.050# 0.50 1.011354 0.33# 0.0865 0.8 1. 31465 0.35$ 0.101## 1.01 #.0#1665 0.40$ 0.13138 1.31 #.631865 0.4$1 0.18$34 1.8$ 3. $#16# 0.555 0.#41$# #.4# 4.84#4 # 0.635 0.3166$ 3.1 6.3330 # 0. 80 0.4 84 4. 8 $.5636 # 0.$38 0.6$103 6.$1 13.8#

Recipient Diametru Ina3time

m m m !e#l 1054 0.#53 1.3 16 0.8# 1.001354 0.33# 1.3 16 0.8# 1.001465 0.35$ 1.6510 0.$$ 1.001665 0.40$ 1.6510 0.$$ 1.001865 0.4$1 1.6510 0.$$ 1.00#16# 0.555 1.5 48 0.$4 1.00#4 # 0.635 1.8#88 1.10 1.00

30 # 0. 80 1.8#88 1.10 1.0036 # 0.$38 1.8#88 1.10 1.00

De7it#! mc mp 8

De7it! mc mp 8

Ina3timemat" 0ranu3ar

Ina3timemat" 0ranu3ar

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mc/h

1.31#.013.464.055.#6

.5$.68

1#.61$.11# .64

Suprafata

m" m $ m $ m $0.050# 1.#41 0.$$3 0.8# 1 1.50.0865 #.13 1. 10 1.4#5 # #.40.101## 3.008 #.40 #.005 3 30.13138 3.$04 3.1#4 #.603 4 40.18$34 5.6# 4.50# 3. 51 50.#41$# 6.858 5.486 4.5 # 60.3166$ 10.4#5 8.340 6.$50 $

0.4 84 15. 30 1#.584 10.486 11 10.60.6$103 ##. 48 18.1$8 15.165 15 15

De7it+! mc mp 8

Timp contact min

Timp contact"& min

Timp contact* min

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Densitate vrac 40 45 lbs/cu.ft640.61 #0.68 Kg/mc

5iteza fi3trare funct" 5.5 gpm/sq.ft13.45 1 .11 mc/(mp*h)

5iteza spa3are inversa 10 5.3 gpm/sq.ft#$.36 15.56 mc/(mp*h)

Ina3time strat fi3trant 30 36 in0. 6 0.$1 m

Ina3time recipient 45 54 in1.14 1.3 m

5iteza fi3trare' gpm/sq.ft 6.000

#+"') mc/(mp*h)

Deferizator Diametru Suprafata De7it apa

inch m mp mc/hABL !4 T-( <#!&+> 10 0.#54 0.0506 0. 43ABL #* T-( <#*&+> 13 0.330 0.0856 1.#55ABL #' T-( <#+'&> 14 0.356 0.0$$3 1.456ABL # T-( <#''&> 16 0.406 0.1#$ 1.$0#ABL ) T-( <#4'&> 18 0.45 0.1641 #.40ABL *) T < #' > #1 0.533 0.##33 3.# 6ABL +& T < +) > #4 0.610 0.#$1 4.# $ABL ) T <*!) > 30 0. 6# 0.4558 6.686ABL #!& T <*') > 36 0.$14 0.6564 $.6#8

ABLM#& 1.#00 1.1304 16.581ABLM ! 1.300 1.3#6 1$.460ABLM & 1.500 1. 663 #5.$08ABLM*! 1.600 #.00$6 #$.4 8

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Minim

@ite?a =+ C). 13.446 mc,2mp -

De7it Aria Diametrumc/h mp m inch1.00 0.0 4 0.30 8 1#.118#.00 0.14$ 0.4353 1 .1383.00 0.##3 0.5331 #0.$8$4.00 0.#$ 0.6156 #4.#365.00 0.3 # 0.6883 # .0$6.00 0.446 0. 53$ #$.683

.00 0.5#1 0.8144 3#.0618.00 0.5$5 0.8 06 34.# 5

$.00 0.66$ 0.$#34 36.35410.00 0. 44 0.$ 33 38.3#111.00 0.818 1.0#0$ 40.1$11#.00 0.8$# 1.066# 41.$ 813.00 0.$6 1.10$8 43.6$#14.00 1.041 1.151 45.34#15.00 1.116 1.1$#1 46.$33

20.00 1.48 1.3 65 54.1$4

Minim@ite?a . . 1#.00 mc,2mp -

Diametru Suprafata De7it S"I"inch m mp mc/h

0.1 8 0.0#48 0.#$88 0.#03 0.03#4 0.38$

10 0.#54 0.0506 0.6081# 0.305 0.0 #$ 0.8 513 0.330 0.0856 1.0#

14 0.356 0.0$$3 1.1$116 0.406 0.1#$ 1.55618 0.45 0.1641 1.$6$#1 0.533 0.##33 #.680#4 0.610 0.#$1 3.50130 0. 6# 0.4558 5.4 036 0.$14 0.6564 .8 64# 1.06 0.8$34 10. #1

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48 1.#1$ 1.166$ 14.00#

1.600 #.00$6 #4.115

naltime !trat filtrant 0. 6 m

Diametru Suprafata 5o3um uti3inch m mp litri

0.1 8 0.0#48 18.$18 0.#03 0.03#4 #4. 0

10 0.#54 0.0506 38.5$1# 0.305 0.0 #$ 55.513 0.330 0.0856 65.##14 0.356 0.0$$3 5.6416 0.406 0.1#$ $8. $18 0.45 0.1641 1#5.04#1 0.533 0.##33 1 0.1$

#4 0.610 0.#$1 ###.#$30 0. 6# 0.4558 34 .3#36 0.$14 0.6564 500.154# 1.06 0.8$34 680. 548 1.#1$ 1.166$ 88$.15

;ite?a optima de ;iltrare J<1# mc,cp.-;ite?a de !plare in;er!a ;<#4 mc,mp.- re?ulta rad de e pan!iune !trat 35/

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#! gpm/sq.ft 10.000+"+& mc/(mp*h)

De7it spa3are

mc/h mc/h mc/h0.80 6.#10 5.501.30 8.0 3 .501.60 8.6$4 8.00#.10 $.$35 $.00#. 0 11.1 10.003. 0 13.040 1#.004.50 14.$03 13.50

.#0 18.6#$ 1 .0010.50 ##.355 #0.00

15.00 #$.33 #5.00#0.00 31. 8# 30.00#5.00 36.6 1 36.0030.00 3$.116 40.00

5iteza spa3areinversa

De7itcata3o0

De7it spa3arecata3o0

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Ma im Recomandat

@ite?a =+ C). 1 .113 mc,2mp - @ite?a =+ C).

De7it Aria Diametru De7itmc/h mp m inch mc/h1.00 0.058 0.# #8 10. 4# 1.00#.00 0.11 0.3858 15.1$1 #.003.00 0.1 5 0.4 #6 18.605 3.004.00 0.#34 0.545 #1.483 4.005.00 0.#$# 0.6101 #4.01$ 5.006.00 0.351 0.6683 #6.311 6.00

.00 0.40$ 0. #1$ #8.41$ .008.00 0.46 0. 1 30.38# 8.00

$.00 0.5#6 0.8185 3#.##5 $.0010.00 0.584 0.86#8 33.$68 10.0011.00 0.643 0.$04$ 35.6#6 11.001#.00 0. 01 0.$451 3 .#10 1#.0013.00 0. 60 0.$83 38. #$ 13.0014.00 0.818 1.0#0$ 40.1$1 14.0015.00 0.8 1.056 41.60# 15.00

30.00 1. 53 1.4$44 58.834 30.00

Ma im Recomandat@ite?a . . 15.56 mc,2mp - @ite?a . .

Diametru Suprafata De7it S"I" Diaminch m mp mc/h inch

0.1 8 0.0#48 0.3868 0.#03 0.03#4 0.504 8

10 0.#54 0.0506 0. 88 101# 0.305 0.0 #$ 1.135 1#13 0.330 0.0856 1.33# 13

14 0.356 0.0$$3 1.545 1416 0.406 0.1#$ #.01 1618 0.45 0.1641 #.553 18#1 0.533 0.##33 3.4 5 #1#4 0.610 0.#$1 4.53$ #430 0. 6# 0.4558 .0$3 3036 0.$14 0.6564 10.#14 364# 1.06 0.8$34 13.$0# 4#

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48 1.#1$ 1.166$ 18.15 48

1.600 #.00$6 31.# 1

naltime !trat filtrant 0.$1

Diametru Suprafata 5o3um uti3inch m mp litri

0.1 8 0.0#48 ##.6$8 0.#03 0.03#4 #$.64

10 0.#54 0.0506 46.311# 0.305 0.0 #$ 66.6$13 0.330 0.0856 8.#614 0.356 0.0$$3 $0.16 0.406 0.1#$ 118.5518 0.45 0.1641 150.04#1 0.533 0.##33 #04.#3

#4 0.610 0.#$1 #66. 430 0. 6# 0.4558 416. $36 0.$14 0.6564 600.184# 1.06 0.8$34 816.$148 1.#1$ 1.166$ 17066.$8

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1#.000 mc,2mp -

Aria Diametrump m inch

0.083 0.3#58 1#.8#0.16 0.4608 18.1410.#50 0.5643 ##.#180.333 0.6516 #5.6550.41 0. #86 #8.6830.500 0. $81 31.4#10.583 0.86#0 33.$380.66 0.$#16 36.#8#

0. 50 0.$ 5 38.48#0.833 1.0303 40.5640.$1 1.0806 4#.5441.000 1.1#8 44.4361.083 1.1 48 46.#501.16 1.#1$1 4 .$$61.#50 1.#61$ 4$.681

#.500 1. 846 0.#5$

13. 8 mc,2mp -

etru Suprafata De7it S"I"m mp mc/h

0.1 8 0.0#48 0.34#0.#03 0.03#4 0.440.#54 0.0506 0.6$80.305 0.0 #$ 1.0050.330 0.0856 1.1 $

0.356 0.0$$3 1.3680.406 0.1#$ 1. 80.45 0.1641 #.#610.533 0.##33 3.0 80.610 0.#$1 4.0#00. 6# 0.4558 6.#810.$14 0.6564 $.0451.06 0.8$34 1#.311

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1.#1$ 1.166$ 16.080

1.600 #.00$6 # .6$3

r. aci real r. aci @olum * RM B !trat B bac Ja!- B rec

#.30458#8 5# # 56.6 0.661#$1 0.$#580 45# 111#.6 # 06 18 3 84.$ 0.855#$# 1.1$ 40$1#8 13663.4$0$65 54 4 113.# 0.8 3111 1.###35515# 136#4.418#5355$5 5 141.5 0.86#33# 1.#0 #6434 13506.013 340115 6 16$.8 0. 60#6 1.0643636 1151

.8546 #$$46 8 ##6.4 0. 60$$ 1.08653 $13 13#8

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B"A" apaitrati #!"!! m ,l #10.00 ppm 3.3$ meF,lulfati #**"!! m ,l 133.00 ppm #. meF,l

De7it #!"!! mc,-

(apacitatea de 7azaC* 0.56

51(apacitatea de operare $

0.10 0.310.#0 0.3#0.30 0.330.40 0.350.50 0.380.60 0.400. 0 0.45

0.80 0.500.$0 0.55

%O !"+#

0.10 0.500.#0 0.30.30 0.#80.40 0.#50.50 0.#00.60 0.180. 0 0.15

0.80 0.1#0.$0 0.10

P&&R #%1

5o3um teoretic de apa tratata pentru # 3itru rasina A& !E@A)r),19 148.58 litri apa

5o3um rea3 de apa tratata pentru # 3itru rasina A& !E@A)rR,19 133. # litri apa

CR 3$.$6 m ,l

DenitrificatoareMo!el '&(15 '&(25 '&(50 '&(75 '&(100 )ol. r#* $# 15 #5 50 5 100

)ol #"# +r#+.#7005.80 37343.00 67686.00 1070#$.00 1373 #.00

#.01 3.34 6.6$ 10.03 13.3

Pondere /. * neretinut

(oncentratie rezidua3a /. *

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T m" $+re rege$er#r 0.#0 0.33 0.6 1.00 1.34

Denitrificatoare - simu3ari)ol. r#* $# 4000

)ol #"# +r#+. 5347880T m" $+re rege$er#r 53.4$

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16$.35135. 1

calcul tact debitmetru

t pemc,- l,- l,m l,!ec 1tact,10l

60 60000 1000 16.66666 0.610 10000 166.666 #. 8 3.6

normal 50 50000 833.3333 13.88888$ 0. #

'&(150 '&(200 '&(300 '&(500 '&(700 150 #00 300 500 00 l +r

#07058.00 #67 44.00 407116.00 667860.00 $37604.00 l +r #0.06 #6. 4 40.1# 66.86 $3.60 mc

ppm CaC" 3

ppm CaC" 3

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#.01 #.6 4.01 6.6$ $.36 ore

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1tact,100l6

36

.#

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Duritate apa 81.05 d=Debit apa 6.00 mc,-)imp functionare coloana #4.00 -Capacitate de retinere !c-. ioni 1.50 eF,l

Duritate apa 810.50 m ,l CaC"3Capacitate de retinere !c-. ioni 5.00 CaC"3 , l !c-

@olum total apa , coloana 1447000.00 litri

Duritate retinuta , coloana 1167 1#7000.00 m CaC"3Duritate retinuta , coloana 1167 1#.00 CaC"3

@olum !c-. ioni , coloana 17556.16 litri TE.RETI(@olum !c-. ioni , coloana 17600.00 litri REAL

naltime !trat !c-. ioni 1.00 m

Diametru coloana !c-. ioni 1.43 m

1 litru !aramura !aturata 0.11$8#64# E aC9

Cantitate de aCl , litru !c-. 0.150 E

@olum !aramura !aturata , litru !c-. 1.#5 litri !aramura

Cantitate de aCl , re enerare #40.00 E@olum !aramura !aturata , re enerare #700#.$0 litri

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%#"#c +#+e !e *ch m o$ c #"% 53#0 $500 $5d2 dF eH 3

- r +#+e #"# !"!! 35. 1 0.35 14#$ 0.00 14#$

)ol m *ch m #+or !e o$ &! litri

eH d2 dF%#"#c +#+e +o+. !e *ch m o$ c %& #667000 4 57000 47 50

)ol m +o+#l !e #"# !e! r #+# +eore+ c 13.30 mc

Con!tanta calcul 0.6315 $)ol m +o+#l !e #"# !e! r #+# re#l 8.40 mc

Debit apa # mc,-

Durata intre re enerari 8.40 -

eH 3s d2 3s dF 3s 0 (a(. * 3s

0 (a(. *

0 (a(. *

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(oncentratiiConc. =e 0.10 m ,l 0.00$6 dBConc. Mn 0.#0 m ,l 0.01$# dBConc. a 100.00 m ,l 1#.# dB

Conc. B4 0.100 m ,lDuritate 35.00 dB 35 dB 630 ppmTota3 +)" 44 d2 )*!"*! ppm

Conducti;itate $0# 1804 ppm)otal )D 30.30 ppm

Parametrii insta3atieDebit de apa 1.00 mc,-Con!um ?ilnic 1.50 mc,?i'erioada re enerare 1 ?ileCon!um intre re enerari 1.50 mc

Capacitate de !c-imb CR100 #") mc,dBCap. de ret. amoniu %4! m B4 , litru CR100Concentratie !aramura #& 1

capt 0.843# mc dB

@)CR100 41.6 litri

@RCR100 45.84 litri

/r" de saci (R#!! <5o3" (R#!! 4"* 3itri>r. de !aci CR100 1.6# !aci

/r" rea3 de saci (R#!!r. de !aci CR100 #.00 !aci

@ol. real. CR100 56.6 litri

Cant. de !are 5.66 E

(ant" de apa din saramuraCant. apa 3#.0 E

/ecesar capacite tratare %o$* m l$ c To+#l

5o3umu3 teoretic de (R#!! necesar < &ece*#r c#"#c +#+e +r#+#re / %#". !e *ch m %R100 >

5o3umu3 rea3 de (R#!! necesar < )ol m l +eore+ c %R100 1.1 >

5o3um rea3 (R#!! < &r. !e *#c 28.3 l +r /*#c >

(ant" sare pt" o re0enerare < )ol. %R100 0.1 g &#%l / 1 l +r %R100 >

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5o3um vas saramura@olum ;a! !aramura 48 litri

5erificare a7sor7tie amoniac

Camoniu 150 m

@)CR100 0.15 litri

@RCR100 0.1 litri

Rezu3tat verificare .

palare in;er!a 10 min

A!piratie !aramura 30 minpalare lenta 60 min

(antitatea tota3a de amoniu retinuta < %#$+. +o+#l# !e #"# +r#+#+# %o$c. #mo$ >

5o3umu3 teoretic de (R#!! necesar pt" a retine cantitatea tota3a de amoniu < %#$+. +o+#l#

5o3umu3 rea3 de (R#!! necesar < )ol m l +eore+ c %R100 1.1 >

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#

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e #mo$ / %#". !e re+ $ere %R100 >

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Dimensionare de7it

1 du! 1# l,min #0 l,-1 robinet cada #5 l,min 1500 l,-

1 robinet bucatarie 1# l,min #0 l,-

umar du!uriumar robinet cadaumar robinet bucatarie

Debit nece!ar 57880 l,-Debit nece!ar 5.88 mc,-

(oeficienti?i 1.6o #p 1.10! 1.05

2.TELumar loc. ca?are #5 locuri

Con!um apa 300 l,om

/ecesar de apa /ec

Con!umul mediu ?ilnic N Cn ?i med. < umar loc. ca?are Con!um apa OCn ?i med. .50 mc,?i

Con!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . 1#.00 mc,?i

Debitul orar ma . N %n orar ma < o Cn ?i ma .,6 O%n orar ma 4.00 mc,-

(erinta de apa (eriCon!um mediu ?ilnic N C! med. ?i< p ! Cn med. ?i O

C! med. ?i 8.66 mc,?iCon!umul ma im ?ilnic N C! ?i ma . < p ! Cn ?i ma . O

C! ?i ma . 13.86 mc,?i

Debitul orar ma . N %! orar ma < p ! Cn orar ma .O%n orar ma 4.6# mc,-

Restitutia de apa ResCon!um mediu ?ilnic N Cu med. ?i < 0.8 C! med. ?i O

C! med. ?i 6.$3 mc,?iCon!umul ma im ?ilnic N Cu ?i ma . < 0.8 C! ?i ma . O

C! ?i ma . 11.0$ mc,?i

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Debitul orar ma . N %u orar ma < 0.8 C! orar ma . O%n orar ma 3. 0 mc,-

/umar 3oc" cazare + pers"Con!um apa turi!ti #50 l,om,?i

/umar pers" deservire 4+ pers"Con!um apa turi!ti 50 l,om,?i

/umar 3oc" restaurant #!!! pers"Con!um apa re!taurant 15 l,om,?i

/umar masini spa3at * 7ucCon!um apa re!taurant #500 l,?i

E?i 1.#Ep 1.15E! 1.03Eo #

/ecesar de apaTURISTI <STAS #*+*-# !!'>

Con!umul mediu ?ilnic N Cn ?i med. < umar loc. ca?are Con!um apa turi!ti OCn ?i med. 105.50 mc,?iCon!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . 1#6.60 mc,?i

PERS./AL DESER5IRE <STAS #*+*-# !!'>Con!umul mediu ?ilnic N Cn ?i med. < umar per!. de!er;. Con!um apa per!. de!er;. OCn ?i med. 4.#0 mc,?iCon!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . 5.04 mc,?i

MASA SER5ITA I/ RESTAURA/T <STAS #*+*-# !!'>Con!umul mediu ?ilnic N Cn ?i med. < umar loc. re!taurant Con!um apa re!taurant OCn ?i med. 15.00 mc,?iCon!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . 18.00 mc,?i

SPALAT.RIE <STAS #*+*-# !!'>Con!umul mediu ?ilnic N Cn ?i med. < umar ma!ini !palat Con!um apa ma!ina !palat OCn ?i med. .50 mc,?iCon!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . $.00 mc,?i

T.TAL /E(ESAR APA

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Con!umul mediu ?ilnic 13#.#0Con!umul ma im ?ilnic 158.64Con!um anul mediu 487#53.00Con!um anul ma im 5 7$03.60

STAS #*+*-# !!'

/umar persoane#00 per!.

De7ite de consum

60 litri,con!umator pe ?i0 litri,con!umator pe ?i0 litri,con!umator pe ?i0 litri,con!umator pe ?i

#00 litri,con!umator pe ?i

(oeficienti de variatieE?i 1.60Eor #.00E! 1.0#Ep 1.10

De7it zi3nic mediu ---- zi med" J </p Hs> #!!!% ?i 40.00 mc,?i

De7it zi3nic ma im ---- zi ma " J </p Hs zi> #!!!% ?i 64.00 mc,?i

De7it ma im orar ---- or ma " J </p Hs or zi> <#!!! +>% or 5.33 mc,-

/ p

HHpH!pH!;H!

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RESTAURA/Tumar loc. #5 locuri

Con!um apa 5 l,om

sar de apa

Con!umul mediu ?ilnic N Cn ?i med. < umar loc. Con!um apa OCn ?i med. 1.88 mc,?i

Con!umul ma im ?ilnic N Cn ?i ma . < ?i Cn ?i med OCn ?i ma . 3.00 mc,?i

Debitul orar ma . N %n orar ma < o Cn ?i ma .,6 O%n orar ma 1.00 mc,-

nta de apaCon!um mediu ?ilnic N C! med. ?i< p ! Cn med. ?i O

C! med. ?i #.1 mc,?iCon!umul ma im ?ilnic N C! ?i ma . < p ! Cn ?i ma . O

C! ?i ma . 3.4 mc,?i

Debitul orar ma . N %! orar ma < p ! Cn orar ma . O%n orar ma 1.16 mc,-

itutia de apaCon!um mediu ?ilnic N Cu med. ?i < 0.8 C! med. ?i O

C! med. ?i 1. 3 mc,?iCon!umul ma im ?ilnic N Cu ?i ma . < 0.8 C! ?i ma . O

C! ?i ma . #. mc,?i

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Debitul orar ma . N %u orar ma < 0.8 C! orar ma . O%n orar ma 0.$# mc,-

(erinta de apaTURISTI <STAS #*+*-# !!'>

Con!umul !p. med. ?ilnic N C!p ?i med. < Ep E! Cn ?C!p ?i med. 1#4.$6 mc,?iCon!umul !p. ma . ?ilnic N C!p ?i ma . < Ep E! Cn ?iC!p ?i ma . 14$.$6 mc,?i

PERS./AL DESER5IRE <STAS #*+*-# !!'>Con!umul !p. med. ?ilnic N C!p ?i med. < Ep E! Cn ?C!p ?i med. 4.$ mc,?iCon!umul !p. ma . ?ilnic N C!p ?i ma . < Ep E! Cn ?iC!p ?i ma . 5.$ mc,?i

MASA SER5ITA I/ RESTAURA/T <STAS #*+*-# !!'>Con!umul !p. med. ?ilnic N C!p ?i med. < Ep E! Cn ?C!p ?i med. 1 . mc,?iCon!umul !p. ma . ?ilnic N C!p ?i ma . < Ep E! Cn ?iCn ?i ma . #1.3# mc,?i

SPALAT.RIE <STAS #*+*-# !!'>Con!umul !p. med. ?ilnic N C!p ?i med. < Ep E! Cn ?C!p ?i med. 8.88 mc,?iCon!umul !p. ma . ?ilnic N C!p ?i ma . < Ep E! Cn ?iC!p ?i ma . 10.66 mc,?i

T.TAL (ERI/TA APA

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Con!umul mediu ?ilnic 156.5$Con!umul ma im ?ilnic 18 .$1Con!um anul mediu 5 7155.68Con!um anul ma im 687586.81

orar ma " J (sp zi ma " o + orar ma " #&"'' mc 8

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i med O

i ma O

i med O

i ma O

i med O

i ma O

i med O

i ma O

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N O T E D E C A L C U L SONA

. *AHA '")(H(9( D( D M( " AR(

1). Baza de calcul)A 1343,1 $1 Determinarea cantitatii de apa pentru centre populate)A 14 8 $1 Alimentarea cu apa a centrelor populate)A 4163,1 $5 Retele de di!tributie)A 85$1 5 Ampla!area in localitate a retelelor )A 1061 ,# 84 )e;i din polietilena de mare den!itate)A 6054, Adancimea ma ima de in -etormati; $ $4 ormati; pentru proiectarea !i e ecutarea in!talatiilor !anitare

2). Ipoteze de calcula . Modul de alimentare cu apa al locuitorilor7 in functie de radul cu dotare cu in!t. de apa e!te

15% din locuitori !e ;or alimenta de la ci!mele ampla!ate in curti

85% din locuitori !e ;or alimenta de la in!talatii !anitare interioare

). Note de calculDefalcarea numarului de locuitori functie de radul de dotare al cladirilor cu in!t. alimentare apa

umar locutori anul 1$$8 7646umar locutori anul #0#0 9100

r locuitori alimentati cu apa de la ci!mele ampla!ate in curti 1365r locuitori pre;a?uti cu in!talatii interioare de apa !i canal 35

Con!um pentru indu!tria mica 1!

ece!arul Cerinta %! ?i mediu %! ?i ma %!de apa %! de apa %! %o

mc,?i l,! mc,?i l,! mc,?i l,! mc,?i l,! mc,?imc,! mc,! mc,!

#48 #8. $ #$#8 33.8$ #$#8 33.8$ 3301 38.#0 5611.1$0.033886 0.038#03 0.064$44

ece!arul de apa !e determina conform )A 1343,1 $1 cu relatia

N=Ng + Np + Ns + Nim [mc/zi]< ece!ar de apa pentru ne;oi o!podare!ti in mc,?i

p< ece!ar de apa pentru ne;oi publice in mc,?i!< ece!ar de apa pentru !tropit !tra?i7 !patii ;er?i in mc,?iim< ece!ar de apa pentru indu!tria mica in mc,?i

<1,1000 !uma2+i n i < 1 33.55 mc,?i+i <numar de locuitori permanenti !i flotantin i <nece!arul de apa !pecific pentru ne;oi o!podare!ti in functie de radul de dotare 2cf. tabel 17 )A 1

p<1,1000 !uma2+i npi p< 6$8.43 mc,?inpi <nece!arul de apa !pecific pentru ne;oi publice 2cf. tabel 17 )A 1343,1 $1

!<1,1000 2+i 5 l,om ?i !< 45.50 mc,?i

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npi <nece!arul de apa !pecific pentru ne;oi publice 2cf. tabel 17 )A 1343,1 $1i< 10.00 mc,?i

ece!arul de apa N= 2487 mc/zi

Cerinta de apa %! !e determina conform aceluia!i !tandard7 cu relatia

Qs=Ks x Kp x NE!< 170 coeficient care tine !eama de ne;oile te-nolo ice ale !i!temului de alimentare cu apaEp< 1710 coeficient care tine !eama de pierderile de apa admi!e in !i!tem

Qs= 2928 mc/zi

Debitul ?ilnic mediu al cerintei de apa %! ?i med%! ?i ma <22E! Ep ,86400 221,1000 !uma2E?i +i 2n i>npi > ! ?i ma > im ?i ma

E?i< coeficient de neuformitate a debitului ?ilnic

Qs zi max= 0.038203 mc/s

Qs zi max= 3301 mc/zi

Qs zi max= 38.20 l/s

Debitul ?ilnic mediu al cerintei de apa %! ?i med%! ?i med < 22E! Ep ,86400

Qs zi m != 0.033886 mc/s

Qs zi m != 2927.76 mc/zi

Debitul orar ma im al cerintei de apa %! orar ma%! orar ma < Eo %! ?i ma 2mc,! unde

Eo < coeficient de ;ariatie a con!umului orar pentru $100 locuitori < 1."!

Qs "#a# max= 0.064944 mc/s

Qs "#a# max= 233.80 mc/$

Qs "#a# max= 64.94 l/s

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arar

l,!

64.$4

343,1 $1

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input data /umar persoanecon!t. @olum de apa u?ata , omcon!t. =actor corectie ?ilnic

con!t. =actor corectie orar calc. data Debit mediu ?ilniccalc. data Debit ma im ?ilniccalc. data Debit ma im orar

con!t. ncarcare ma!ica pt calcul

calc. data Debit ma!ic influent

calc. data Concentratii in influent ptr. %u? ?i med

calc. data Concentratii in influent ptr. %u? ?i ma

con!t. Conditii medii de e;acuare

con!t. Conditii ma ime de e;acuare

calc. data Debit ma!ic medii e;acuate

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calc. data Debit ma!ic medii e;acuate

calc. data Grad de epurare nece!ar la debit mediu

DI

con!t.

" i enul di?ol;at "D)emperatura )'-E"#@ite?a mm2 pentru apa potab.@ite?a cre!tere ma .or .nitrif.Coef. !inte?a a celulelor nitrifiante@ite?a ma . de utili?. a !ub!tratului@ite?a de de!comp. a nitrifiantelor @ar!ta namolului @ 2min@ar!ta namolului adoptata acoperitor =ractia bacteriei fConcentratia P@

calc. data @ite?a de red. a amoniuluicalc. datacalc. datacalc. datacalc. data Durata proce! denitrificare

con!t.calc. data @olum teoretic denitrificator calc. data @olum real denitrificator

calc. data @ite?a de nitrificare a !ub!tratuluicalc. data @ar!ta namolului in nitrificator

con!t. Coef. de !inte?a pt. celule -eterotrofecalc. data ncarcarea or anica a namoluluicalc. data Durata aerare pt o idarea !ub!t. or .calc. data Cantitate ma . amoniu o idat la a?otcalc. data @ite?a de o idare amoniucalc. data Durata nitrificariicalc. data @olum teoretic nitrificator calc. data @olum real nitrificator

con!t. )imp de retentie -idraulicacalc. data @olum !elector

Dcon!t. " i en nece!ar pt o idarea 1 C*"5con!t. " i en nece!ar pt o idarea 1 B3

calc. datacalc. datacalc. data Debit teoretic de o i en nece!ar

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calc. data Debit real de o i en nece!ar calc. datacalc. data

DIcalc. data Debit

con!t. ncarcarea -idraulic de calculcalc. data uprafata decantor !ecundar

Con!um ?ilnic de o i en QQQCon!um orar de o i en KKK

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STATIE DE EPURARE

/r"PE pers" $!!!@u? l,om,?i 160.00E?i 1.#0

Eor 1. #%u? ?i med < r.'( @u? 2mc,?i #56.00%u? ?i ma < E?i %u? ?i med 2mc,?i 308.00%u? or ma < Eor %u? ?i ma 2mc,- ##.10C*"5

,loc,?i

30.00)E 2 B4 5.30

CC" 55.00M) 30.00%m.C*"5 < r.'( nc.C*"5

,?i

60.00%m. )E 2 B4 < r.'( nc. )E 10.60%m.CC" < r.'( nc. CC" 110.00%m.M) < r.'( nc. M) 60.00

Cmed.C*"5 < %m.C*"5 %u? ?i med

m ,l

#34.38Cmed. )E 2 B4 < %m. )E %u? ?i med 41.41Cmed.CC" < %m.CC" %u? ?i med 4#$.6$Cmed.M) < %m.M) %u? ?i med #34.38Cmed.C*"5 < %m.C*"5 %u? ?i ma

m ,l

1$4.81Cmed. )E 2 B4 < %m. )E %u? ?i ma 34.4#Cmed.CC" < %m.CC" %u? ?i ma 35 .14Cmed.M) < %m.M) %u? ?i ma 1$4.81C*"5infl , )Einfl < %mC*"5 , %m. )E 5.66Cmed.de;.C*"5

r,mc

#0.00Cmed.de;.CC" 0.00Cmed.de;. B4 1.80

Cmed.de;. )E 8.00Cmed.de;.M) 35.00Cmed.de;. "3 #0.00Cmed.de;. "# 0.80Cma .de;.C*"5

r,mc

#5.00Cma .de;.CC" 1#5.00Cma .de;. B4 #.00Cma .de;. )E 10.00Cma .de;.M) 60.00Cma .de;. "3 #5.00Cma .de;. "# 1.00%m.C*"5 < %u? ?i med Cmed.de;.C*"5

,?i

5.1#

%m.CC" < %u? ?i med Cmed.de;.CC" 1 .$#%m. B4 < %u? ?i med Cmed.de;. B4 0.46%m. )E < %u? ?i med Cmed.de;. )E #.05%m.M) < %u? ?i med Cmed.de;.M) 8.$6%m. "3 < %u? ?i med Cmed.de;. "3 5.1#%m. "# < %u? ?i med Cmed.de;. "# 0.#0%m.C*"5 < %u? ?i ma Cma .de;.C*"5 . 0%m.CC" < %u? ?i ma Cma .de;.CC" 38.50

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%m. B4 < %u? ?i ma Cma .de;. B4,?i

0.6#%m. )E < %u? ?i ma Cma .de;. )E 3.08%m.M) < %u? ?i ma Cma .de;.M) 18.48%m. "3 < %u? ?i ma Cma .de;. "3 . 0%m. "# < %u? ?i ma Cma .de;. "# 0.31Gr.ep.C*"5 < 1 Cma .de;.C*"5,Cmed.C*"5

/

8$.33

Gr.ep. )E < 1 Cma .de;. )E,Cmed. )E 5.85Gr.ep.M) < 1 Cma .de;.M) ,Cmed.M) 4.40

ME/SI./AREA DE/ITRIFI(AT.RULUI#.50

1#.00.#0

1.301,?ile 0.50

m m 0.#4S 0.#0

1.#5Ed 0.06@ ?ile 5.55@ A ?ile 10.50f 0.05P@ 47000.00R < P@ f m ,l,?i #50.00

< Cmed. )E 41.41o < 0.$# Cmed. )E 38.10e < Cma .de;. )E 10.00

)D < 2 o e , R ?ile 0.11%>%r<#% #.00

@)D < )D #% %u? ?i ma mc 6 . 6@RD < @)D 1.1 mc 4.60

IME/SI./AREA /ITRIFI(AT.RULUIF < 21,@ A>Ed ,S 0. 8@ < 1,2S F Ed ?ile 10.50

C!int.cel. 0.50" < 21,@ >Ed ,C!int.cel. 0.31

)a < 2Cmed.C*"5 Cma .de;.C*"5 ,P@, " 0.14o <07$# 2Cmed. )Ei Cma .de;. )E m B4,l #8.$0

R < F f P@ m B4,l,?i 155.#0)a2 < o ,R ?ile 0.1$

@) < # %u? ?i ma )a2 mc 114.60@R < @) 1.1 mc 1#6.10

DIME/SI./ARE SELE(T.R

)RB ore 0.50@!elector < # %u? ma ?i )RB mc 1#.$0IME/SI./AREA SISTEM DE AERARE@"#. C*"5 mc 1.50@"#. B3 mc 4.609obiol 9ebiol < %mC*"52if %mC*"52ef ,?i 5#.30

e2med e < 2%m )E > %m B4 2in 2%m B4>%m "3 2ef #.#8%)."# < 2@"#.C*"5 9obiol 9ebiol > @"#. B3 e2med e ,?i 88.$4

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%R."# < %)."# 1.1 $ .84C?i."# < %R."# # ,?i 1$5.68Cor."# < C?i."# , #4 ,- 8.15E/SI./ARE DE(A/T.R SE(U/DAR

%calcul < 2# %u? ?i ma ,#4 mc,- #5.6B mc,mp 1.80D < %calcul , B mp 14.#6

7/21/2019 Calcul 2011


TIPURI DE MATERIALE FILTRA/TE 9RA/U

Densitate De7it in functionare37s" cu"ft 0 mc 9PM sH"ft" mc mp@8

BIRM <re0u3ar> 50 800.$# 3.50 5.00 8.56 1#.##

BIRM <fine> 50 800.$# 3.50 5.00 8.56 1#.##M9" 9REE/SA/D 85 1361.5 5.00 1#.##(ARB./ 35 560.65 5.00 1#.##FILTER A9" #5 400.46 5.00 1#.##(AL(ITE 100 1601.85 3.00 6.00 .33 14.6(.R.SE 100 1601.85 3.00 6.00 .33 14.6FIL. 1#0 1$##.##P R.L. 1#0 1$##.## 10.00 1#.00 #4.45 #$.34ALS.RB 45 #0.83RESI/ <re0u3ar> 50 800.$# #0.00 30.00 48.8$ 3.34RESI/ <FI/E MES2> 50 800.$# 15.00 #0.00 36.6 48.8$

MATERIAL FILTRA/T9RA/ULAR

7/21/2019 Calcul 2011


ARE DEBITUL DE SPALARE I/5ERSA

De7it spa3are inversa Ina3time strat fi3trant9PM sH"ft" mc mp@8 Inc8 m N 1 O

10 1# #4.45 #$.34 30 36 0. 6 0.$# 35 50

8 10 1$.56 #4.45 30 36 0. 6 0.$# 35 50 8 1# 1$.56 #4.45 30 0. 6 35 50 8 10 1$.56 #4.45 #6 30 0.66 0. 6 30 40 8 10 1$.56 #4.45 #4 36 0.61 0.$# 35 50 8 1# 1$.56 #4.45 #4 30 0.61 0. 6 35 8 1# 1$.56 #4.45 #4 30 0.61 0. 6 35

15 36.6 30 5018 #3 44.01 56.#3 30 36 0. 6 0.$# 30 50 5 1#.## 1 .11 30 50 3 8 .33 1$.56 #4 30 0.61 0. 6 50

#75 4 6.11 $. 8 #0 30 0.51 0. 6 50

7/21/2019 Calcul 2011


11$ mc,- debit ma im de apa1.3 m ,l conc. fier ce trebuie o idata

0.15 m ,l conc. de fier la ie!ire

5 cantitatea de o i en re idual in a0.#3# pondere o i en in aer 1.#04 E , mc den!itate aer

5/ eficienta !pecifica a ab!orbtiei o i

1.8 m CaC"3 , m =e1.$ m . . , m =e

Dimensionarea o idarii fieru3ui prin aerare

0.14 Con!um !pecific de o i en pentr

0.18# m ,l Cantitatea de o i en nece!ar pen

0.0## Debitul de o i en nece!ar pentru

44.15 Debitul de aer nece!ar o idarii

A3ca3initate consumata

6.68304 CaC"3 , ?i Con!umul ?ilnic de alcalinitate

Productia de namo3 estimata

.0543# E . . , ?i 'roductia de namol ?ilnica

Timpu3 necesar pentru o idarea fieru3ui cu o i0en

Er 0.168 1,min Con!tanta de ordin 1 a timpului d

51.5$ min )imp nece!ar o idarii fierului in c

1#.85 min )imp nece!ar o idarii fierului in c

3#.## min

Dimensionare 7azin de aerare pentru o idarea fieru3ui

63.$0 mc @olum apa in ba?inul de aerare

%ma

C=e

C=e.e

R"# m "# ,l apa"# aer E "# , E aer ρ aer η "#

Al !.=e"#

!.=e"#

C !.=e"# m "# ,m =e

C"#

%"# E "# ,-

%aer mc aer , -

Al =e"#

=e"#

're!upunand cele mai defa;orabile conditii7 o temp. a apei brute de 10 °C7 un pB al apei de

) CM=R

) '=R

) o idare )imp de o idare minim recoman

@apa

7/21/2019 Calcul 2011


$0/ Grad umplere ba?in de aerare

1.00 mc

GR umplere

@ba?in @olum minim ba?in de aerare

7/21/2019 Calcul 2011


a

enului in apa

o idarea 1 m fier

tru o idarea fierului C"#

o idarea fierului

reactie

?ul unui reactor complet mi at

?ul unui reactor tip pi!ton

C"# < C =e C!.=e"#

%"# < C "# %ma

%aer < 2%"# > 0.001 R "# %ma ,2"# aer ρaer η " #

Al =e"# < C =e Al !.=e"# #4,1000

=e"# < C =e %ma !.=e"# #4,1000

!i e i!tenta unui proce! !tationar

) CM=R < C =e , 2Er C=e.e

) '=R < 1,E r ln 2C=e ,C =e. i

at ) o idare < 2) CM=R >) '=R ,#

@apa < %ma ) o idare ,60

7/21/2019 Calcul 2011


@ba?in < @apa , GR umplere

7/21/2019 Calcul 2011


(a3cu3 cant" de c3or in functie de caracteristici3e apei 7rute

(./STA/TE

Factor de si0uranta #!12ipoc3orit +1 *4"!!2ipoc3orit # 1 #+!"!!(ontor cu impu3suri #5o3um in6ectie !"'4

5ARIABILE

De7it apa/umar ore functionare #!p2 )

(oncentratie de amoniu %"+!!(oncentratie de fier %"!4!(oncentratie de man0an !"#!!(oncentratie 8idro0en su3furat !"!!!(oncentratie su7stante or0anice !"!!!

(AL(UL

(a3cu3 necesar de c3or Cantitate de clor , amoniu 5.#0Cantitate de clor , fier 6.36

Cantitate de clor , man an 0.15Cantitate de clor , -idro en !ulfurat 0Cantitate de clor , !ub!tante or anice 0.00Cantitate de clor totala 2teoretic 4#")#

Cantitate de clor totala 2real 4%"44Cantitate de clor totala 2real 4"%44

Cantitate de clor totala 2real 4%"44

Cantitate totala orara de clor #)%")&

Con!um orar de -ipoclorit 4/ +")*Con!um ?ilnic de -ipoclorit 4/ +)"*!

@olum -ipoclorit 4/ #36.5#@olum -ipoclorit 4/ #36.5#

umar injectii *+4

7/21/2019 Calcul 2011


*utelie de clor 50+tili?are o butelie de clor # 8.16+tili?are o butelie de clor 11.5$

Do?a de clor dorita in apa !"&Debit apa &

Cant. Cl# # "&

Cant. Cl# , ml -ipoclorit 4/ 0.0380Cant. Cl# , l -ipoclorit 4/ 38

Cant. nece!ara -ipoclorit 4/ 0.013#Cant. nece!ara -ipoclorit 4/ 1.3158

umar injectii teoretic 1.$350umar injectii real #.1#85

/umar in6ectii setat

#0.0#63

7/21/2019 Calcul 2011


0(3 3 8ipoc3orit BC100 2AFua 0. $0(3 3 8ipoc3orit 150 BC300 2AFua 1.38imp" #!! 3 m3 in6"

mc 88

m0 3m0 3m0 3m0 3m0 3

m Cl#,l apa 4 4"!!m Cl#,l apa !") !"'+

m Cl#,l apa #"& #"*!m Cl#,l apa "# "!4 <p2 =4> sau 4"+ <p2 ?4>m Cl#,l apa "&m Cl#,l apa

m Cl#,l apa Cl#,100 l apa

Cl#,mc apa

0 (3 8

l -ipoclorit , - Con!um orar de -ipoclorit 1#/ #" 4l -ipoclorit , ?i Con!um ?ilnic de -ipoclorit 1#/ # "4+

ml -ipoclorit , 100 l apa @olum -ipoclorit 1#/ 64.#0ml -ipoclorit , impul! @olum -ipoclorit 1#/ 64.#0

inj. umar injectii %&

7/21/2019 Calcul 2011


umar de injectii orar 1$00E umar de injectii minut 3#ore =rec;enta impul!uri receptionate 1 imp,?ile

umar ma injectii la frec;enta calculata 360

9a fiecare #4!

m Cl#,l apamc,-

,-

Cl# , ml !ol. Cant. Cl# , ml -ipoclorit 1#/ 0.1400m Cl# , ml !ol. Cant. Cl# , l -ipoclorit 1#/ 140

ml -ipoclorit , l apa Cant. nece!ara -ipoclorit 1#/ 0.0036ml -ipoclorit , 100 l apa Cant. nece!ara -ipoclorit 1#/ 0.35 1

inj. , 100 l apa umar injectii teoretic 0.5#5#inj. , 100 l apa umar injectii real 0.5in6" #!! 3 apa /umar in6ectii setat Err;&!

litri apa Debit apa #5ml -ipoclorit Con!um orar -ipoclorit 8$.#$

Con!um orar -ipoclorit 0.0$

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1051#0

l -ipoclorit , -l -ipoclorit , ?i

ml -ipoclorit , 100 l apaml -ipoclorit , impul!

inj.

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inj,orainj,min "E180 !ec

inj "E

!ecunde !e reali?ea?a %& injectii de -ipoclorit'+" ! ml de -ipoclorit


ml -ipoclorit , l apa pt a a;ea concentratia de 0.5 m Cl# , l apaml -ipoclorit , 100 l apa pt a a;ea concentratia de 0.5 m Cl# ,100 l apa

inj. , 100 l apainj. , 100 l apain6" #!! 3 apa

mc,-ml -ipoclorit , -l -ipoclorit , -

calcul 2011

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