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agitator-power-requirement-and-mixing-intensity-calculation.xls
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agitator-power-requirement-and-mixing-intensity-calculation.xls
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Reactor Geometry 4
Diameter of the reactor
T
=
50.0
4
Height of the cylindrical portion
H
=
80.0
4
Liquid level height in the reactor from bottom
=
!0.0
"
=
#.8
Total Total "olume "olume of the reactor reactor
$
Select the type of Agitator
4
D'T (atio )gitator rpm
%itched &lade T 0.5 *
=
$$0
, -
= =
$$00 $00
Diameter of the agitator
D
=
0.
(eynold+ *umber
(e
=
8$ 8$/#
*p
=
$./!
%
=
$.$
%umping *umber
*q
=
0.
quivalent Diameter
Teq
=
5.00
"olumetric o rate
6
=
7.7
ro++ +ectional area
)
=
$/.
"elocity
"
=
0.!#7
Fluid Properties Den+ity "i+co+ity
Calculation 1) Reynolds Number
2)Poer Re!uirement %oer *umber %oer (equired 1)++uming 802 Loading3
") #i$ing %ntensity
&) Agitator re!uired *o of )gitator+ (equired 'T
= =
# $.40
in in in
m/
rbine
rpm
9g'm/ cp
m
Select the 'alue from Poer number chart based on Reynolds number hp
(se * for Rushton si$ blade turbine + "*2 for conca'e 1,- degree turbine
Select the 'alue from Pumping number chart based on Reynolds number ft
(se -*.2 for Rushton si$ blade turbine + -*. for conca'e 1,- degree turbine
ft/'+ec ft# lic9 here ft'+ec
lic9 Here
0.#5 0./ 0.4 0.5
hemineer HD/ :ide Hydrofoil %itched &lade Turbine (u+hton &lade Turbine $80 Degree oncave
:ide Hydrofoil
%itched &lade turbine
$80 degre
concave
&ac9 to data +heet
&ac9 to data +heet
%oer *umber *arro Hydrofoil 0.8 %oer *o
Poer Number Cur'e for
(eynold+ *o
D'T=0.#5
D'T=0./
D'T=0.4
D'T=0.5
$00 #00 0. /00 500 800 0.5 $#00 /000 0.4 $0000
0.!/ 0.5/ 0.4! 0.4$ 0./8 0./ 0.// 0.//
0.!$ 0.5# 0.45 0./7 0./! 0./4 0./# 0./#
0.7 0.47 0.4# 0./! 0./4 0./# 0./ 0.#7
0.8 0.4 0.4 0./5 0./# 0./ 0.#8 0.#!
0.!
r e b m u N r e o P
0./
0.#
0.$
0 $00
$$00
#$00
/$00 D'T = 0.#5
4$00
5$00
$00
D'T =Reynolds 0./ D'T = 0.4 Number
!
hemineer /0"
00 'T = 0.5
8$00
7$00
$0$00
$$$00
:ide Hydrofoil %oer *o (eynold+ *o #.5
$00 #00 /00 # 500 r 800 e b $.5 $#00 m u/000 N r$0000 $ e
Poer Number Cur'e f
D'T=0.#5
D'T=0./
D'T=0.4
D'T=0.5
#.#8 $.!8 $.5 $./ $.$4 $.07 $.0 $.0
#.#4 $.!5 $.5/ $.#7 $.$# $.08 $.05 $.05
#.$5 $.7 $.48 $.#4 $.07 $.05 $ $
#.$$ $.5 $.45 $.#/ $.08 $.0/ 0.78 0.78
o P
0.5
0 $00
$$00
#$00
/$00 D'T=0.#5
4$00
5$00
Nu D'T=0./ Reynolds D'T=0.4
r ide /ydrofoil
$00
!$00
mber D'T=0.5
8$00
7$00
$0$00
$$$00
Poer Number cur'e f
%itched &lade #.5
%oer *o (eynold+ # *o $00 r #00 e $.5 b /00 m 500 u N 800 r e $#00 $ o /000 P $0000
D'T=0.#5
D'T=0./
D'T=0.4
D'T=0.5
#.$4 $.!5 $. $.4 $./8 $./! $./! $./!
#.$4 $.!5 $. $.4 $./8 $./! $./! $./!
#.$4 $.!5 $. $.4 $./8 $./! $./! $./!
#.$4 $.!# $. $.4 $./8 $./! $./! $./!
0.5
0 $00
$$00
#$00
/$00
4$00
5$00
$
Reynolds Num
r Pitched blade turbine
D'T=0. #5 D'T=0. /
00 ber
!$00
8$00
7$00
$0$00
$$$00
Rushton 3lade (eynold+ *o $00 #00 /00 500 800 $#00 /000 $0000
D'T=0.#5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5
%oer *o D'T=0./ D'T=0.4 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5
D'T=0.5 5.5 5.4 5.5 5.5 5.5 5.5 5.5 5.5
%oer *o D'T=0./ D'T=0.4 /. /. /.# /.# /.# /.# /.# /.# /.# /.# /.# /.# /.# /.# /.# /.#
D'T=0.5 /. /.$5 /.# /.# /.# /.# /.# /.#
1,- 4egree Conca'e (eynold+ *o $00 #00 /00 500 800 $#00 /000 $0000
D'T=0.#5 /. /.# /.# /.# /.# /.# /.# /.#
Chemineer /0" (eynold+ 0. *o $00 #00 0.5 /00 500 r 0.4 e 800 b m $#00 u N /000 0./ g $0000 n i p m u P
Pumping Number c
D'T=0.#5 0.// 0./4 0./ 0./8 0.4/ 0.45 0.5$ 0.5!
%oer *o D'T=0./ D'T=0.4 0./$ 0./ 0.// 0./# 0./5 0./4 0./ 0./ 0.4# 0.4$ 0.44 0.4/ 0.4! 0.45 0.55 0.5/
D'T=0.5 0./ 0./# 0./4 0./5 0./7 0.4$ 0.44 0.5$
0.#
0.$
0 $00
$$00
#$00
/$00
4$00
5$00 Reynolds Nu
ur'e for /0" %mpeller
D'T=0. #5 D'T=0. /
$00 ber
!$00
8$00
7$00
$0$00
$$$00
ide /ydrofoil
r e b m u N g n i p m u P
(eynold+ 0.7 *o $00 0.8 #00 /00 0.! 500 800 0. $#00 /000 $0000 0.5
Pumping Number cur %oer *o D'T=0.#5 0.44 0.54 0.58 0.4 0.! 0.!$ 0.!! 0.8
D'T=0./ 0.4$ 0.48 0.5$ 0.5! 0. 0.# 0.7 0.!/
D'T=0.4 0./ 0.4/ 0.45 0.5$ 0.54 0.5! 0.# 0./
D'T=0.5 0./5 0.4 0.4/ 0.4 0.48 0.5 0.55 0.5
Pitched 3lade
0.4
%oer *o (eynold+ *o D'T=0.#5 D'T=0./ D'T=0.4 D'T=0.5 $00 0.45 0.4# 0./! 0./ 0.# #00 0.55 0.5 0.45 0.4$ /00 0. 0.54 0.48 0.44 0.$ 500 0. 0.$ 0.54 0.4! 800 0.! 0.5 0.5! 0.5 0 $#00 0.!4 0.! 0. 0.5# $00 $$00 #$00 /$00 4$00 $0 /000 0.8# 0.!5 0. 0.5! 5$00 $0000 0.88 0.8 0.8 0. Reynolds Numb 0./
e for ide /ydrofoil
D'T=0. #5 D'T=0. /
!$00 r
8$00
7$00
$0$00
$$$00
Pitched 3lade $ (eynold+ *o 0.7 $00 #000.8 /00 0.! r500 e b8000. m $#00 u N 0.5 /000 g n $0000 i 0.4 p m u P
Pumping Num
D'T=0.#5 0.45 0.55 0. 0. 0.! 0.!4 0.8# 0.88
%oer *o D'T=0./ D'T=0.4 0.4# 0./! 0.5 0.45 0.54 0.48 0.$ 0.54 0.5 0.5! 0.! 0. 0.!5 0. 0.8 0.8
D'T=0.5 0./ 0.4$ 0.44 0.4! 0.5 0.5# 0.5! 0.
0./ 0.# 0.$ 0 $00
$$00
#$00
/$00
4$00
5$00 Reynolds N
ber cur'e for P35
D'T=0. #5 D'T=0. /
$00
mber
!$00
8$00
7$00
$0$00
$$$00
Rushton blade (eynold+ *o $00 #00 /00 500 800 $#00 /000 $0000
D'T=0.#5 0.! 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!#
%oer *o D'T=0./ D'T=0.4 0.! 0.! 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!#
D'T=0.5 0.! 0.!# 0.!# 0.!# 0.!# 0.!# 0.!# 0.!#
D'T=0./ 0.8 0.! 0.! 0.! 0.! 0.! 0.! 0.!
D'T=0.5 0.8 0.! 0.! 0.! 0.! 0.! 0.! 0.!
1,- 4egree Conca'e (eynold+ *o $00 #00 /00 500 800 $#00 /000 $0000
%oer *o D'T=0.#5 0.8 0.! 0.! 0.! 0.! 0.! 0.! 0.!
D'T=0.4 0.8 0.! 0.! 0.! 0.! 0.! 0.! 0.!
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