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7/23/2019 21080114120029_sely Oktaviolita Asri_kelas A
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SELY OKTAVIOLITA ASRI KELAS A TEKNIK LINGKUNGAN
21080114120029
Nama : Sely Oktaviolita Asri
Problem 8.1
Problem: A rapid-mixing basin is to be designed for a water coagulation plant,
and the design
ow for the basin is 4.0 MGD. he basin is to be s!uare with depth e!ual to ".#$
times the
width. he %elocit& gradient is to be '00 s -" (at $0) *+, and the detention time is
0 sec.
Determine
a+ he basin dimensions if increments of " in. are used.b+ he input horsepower.c+ he impeller speed if a %ane-disc impeller with six at blades is emplo&ed and
the tan is
ba/ed. he impeller diameter is to be $0 of the basin width.
Approach *irst, we sol%e for the %olume of the tan b& using the ow rate and
the detention
time. 1e then use this %olume to compute basin dimensions. hen, we use the
%elocit& gradient
and the inematic %iscosit& to obtain power. 2astl&, we use the nowledge of
impeller relations
to obtain impeller speed.
Variables:
3 detention time
x length and width of basin
G %elocit& gradient
d depth of basin
5 ow rate6 6ower input
7 absolute %iscosit& of water
D diameter of impeller
n impeller %elocit&
8 9olume of basin
1 6ower imparted: water densit&
Solution:
a+ *irst, we need to calculate the %olume of the basin. 1e accomplish this
through the following
∀=Q x θ=4 x 10
6gals
1day x
1day
24 hours x 1 hour
60min x 1min
60sec x
1 ft 3
7.48 gal x 30 seconds=185.68 ft
3
1e now tae this %olume and e!uate it to the following
∀= x2 x d d=1.25 x∴∀=1.25 x3
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SELY OKTAVIOLITA ASRI KELAS A TEKNIK LINGKUNGAN
21080114120029
x=3
√ ∀
1.25=
3
√185.68 ft
3
1.25 =5.3 feet ≈ 5 ft −4∈¿
;ow, sol%ing for depth
d=1.25 x=1.25 x5.3 feet =6.675 feet ≈ ft −8∈¿
<ummar&
=asin Dimensions $ft-4in x $ft-4in x >ft-?in
b+ *irst, we need to calculate the power imparted
2.73 x10−5=22.113
ft −lb
sec−ft 3
W =G2 x μ=(900s
−1)2 x ¿
;ow, we can sol%e for the total power
P=W x ∀=22.113 ft −lb
sec−ft 3 x (5.33' )3 x (6.67' )=4193
ft −lb
sec
2astl&, we con%ert to horsepower
P=419 as3 ft −lb
sec x
sec
550 ft −lb x hp=7.62 hp
c+ *or this, we simpl& need the following e!uation2.667 ft
¿
¿4193
ft −lb
sec
5.75 x (¿5 x 1.936¿¿)1 /3=1.41
rev
sec x
60sec
1min =84.5 rpm
¿
n=( P
K t D5 )
1/3
=¿
Problem 8.2
a+ he =asin Dimensions
! =15140m
3
1440min x
1min
60s x30 s
! =5.26m3
he dimensions as gi%en b&
" x " x (1.25" )=5.26m3
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SELY OKTAVIOLITA ASRI KELAS A TEKNIK LINGKUNGAN
21080114120029
1.25"3=5.26m
3
"3=4.208m
"=1.61m
;ow, sol%ing for length
# =1.25"=1.25 (1.61 )=2.0125m
he basin dimensions
"=1.61m
# =2.0125 m
b+ *irst, we need to calculate the power imparted
W =G2 x μ=(900s
−1)2 x 0.00131=1061.1 $ −m
s−m3
;ow, we can sol%e for the total power
P=W x ∀=
1061.1 $ −m
s−m3 x 5.26m
3
m3
=5581.38 $ −m
s =5581
%
s =5581 "
c+ he impeller speed is a %ane-disc impeller with six at blade is emplo&ed and
the tan is ba/ed. he impeller diameter is to be 0 of the bacin width Kr=5.75 d=50 "=0.5 x 1.61=0.805 m
*or this, we simpl& need the following e!uation
n=( P
K t D5 )
1/3
=( 5581"
5.75 x 0.806m x999.7 &g/m2 )
1/3
=1.20 rev
sec x 60 sec
1min =72rps
Problem 8.3
Problem A occulation basin is to be designed for a water coagulation
plant, and the design
ow is ".0 MGD. he basin is to be a cross-ow hori@ontal-shaft, paddle-
wheel t&pe with a
mean %elocit& gradient of #>. s-" (at $00*+, a detention time of 4$ min,
and a G %alue from
$0,000 to "00,000. apered occulation is to be pro%ided, and three
compartments of e!ual
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SELY OKTAVIOLITA ASRI KELAS A TEKNIK LINGKUNGAN
21080114120029
depth in series are to be used, as shown in *igure ?."'(b+. he
compartments are to be separated
b& slotted, redwood ba/e fences, and the basin oor is le%el. he G
%alues are to be $0, #0, and "0s-"
. he occulation basin is to ha%e a widthof '0ft to adBoin the settling basin. he paddle wheels are to ha%e blades
with a > in width and a length of "0ft. he outside blades should clear the
oor b& " ft and be " ft below the water surface. here are to be six
blades per paddle wheel, and the blades should ha%e a spacing of " ft.
AdBacent paddle wheels should ha%e a clear spacing of 0 to > in.
between blades. he wall clearance is "# to "? in. Determine
a+ he basin Dimensionsb+ he paddle-wheel designc+ he power to be imparted to the water in each compartment and the
total power re!uired for the basin.d+ he range in rotational speed for each compartment if "4 %ariable
speed dri%es are
emplo&ed.
Approach: o begin, weCll sol%e for the G %alue. Also, weCll sol%e for the
dimensions of thebasin using a %olume e!uation compared with the ow. *rom this, we will
assume s!uare
compartments in prole (depth length for each prole+. his will gi%e us
our dimensions.
Esing those dimensions, we can sol%e for the paddle wheel design
relati%el& easil& with the
restrictions gi%en. *rom here, we can use the %iscosit& of the water, the
separate G %alues and the %olume of each compartment to sol%e for the
power (in hp+ re!uired for each compartment. 1e then simpl& add those
up to obtain total power. 2astl&, we can use relations of water speed
%ersus rotational speed to obtain the rotations in rpms (the range+.
Variables:
3 detention time
x width of basin
G %elocit& gradient
d depth of basin
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SELY OKTAVIOLITA ASRI KELAS A TEKNIK LINGKUNGAN
21080114120029
5 ow rate
7 absolute %iscosit& of water
dC diameter of paddle wheel
% blade %elocit& relati%e towater
8 9olume of basin
6 6ower imparted
2 2ength of =asin
G G %alue
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Solution:
a+ o begin, we need to chec that the G %alue will fall in the appropriate
range ($0,000-
"00,000+
¿=G x θ=26.7
sec x 45min x
60 sec
1min =72.090
50.000 72.090 100.000 ( o&
;ext, we compute the %olume of the entire basin
∀=Qθ=13.0 #GD
24 x
1hour
60 min x 45 min x
1 ft
7.48=5.43 x 10
4ft
3
1e alread& now the width of the basin, so we can di%ide that out to
obtain the prole area of
the basin
d x )=∀
x =
5.43 x 104
ft 3
90 ft =603.4610
4ft
3
o obtain that each of proles of the compartments is a s!uare, we
assume that per compartment,
length depth. herefore
d x 3 s=603.46104
ft 3
( d=14 ft −2∈¿ )tot =42 ft −6∈¿
inal basin !imensions:} =54187.5 {ft} ^ {3}∀
)=42' 6
'' x=90
' d=14
' 2¿
b+ Ff we assume a six-blade paddle wheel design and that both clearances
from the top and
bottom of " ft, we will tr& and get our D" to match accordingl&.
D1=d−2 (1 ft )−21
2( d
' )=14.17 ft −2 (1 ft )−2( 12 x0.5 ft )=11.67 ft ≈11.6 ft
1e also now that each of the other diameters is e!ual to twice the
spading between blades plus
the width of each blade multiplied b& two.
D2= D1−2 (1 ft )−2 ( d' )=11.6 ft −2 (1 ft )−2 (0.5 ft )=8.6 ft
D3= D2−2 (1 ft )−2 ( d' )=8.6 ft −2 (1 ft )−2 (0.5 ft )=5.6 ft
;ow that the wheel dimensions are nown, we need to calculate howman& paddle wheels per arm. o accomplish this, we tae the total
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width of the basin and subtract out the minimum wheel spacing
between wheels and the minimum spacing between the walls. ;ote the
spacing between wheels will be a function of the number of wheels
themsel%es, but the wall spacing will remain constant. )nce we ha%ethis number, we will round down to the nearest whole integer. 1e
cannot round up because this would mean we ha%e exceeded our basin
width.
x=90 ft =n (10 ft )+2 (1 ft )+(n−1)(2.5 ft )
∴n=7 "heels
1e must now chec our answer to mae sure this number of wheels will
wor. *irst, attempt to hold the wall clearances constant at "ft and
increase wheel spacing, being sure not to cross the > in. clearance
limit.
x=90 ft =7 (10 ft )+2 (1 ft )+(7−1)( y)
∴ y=3 ft
c+ *irst, we must chec that the total paddle blade areas are between "$
and #0 of the total
cross-sectional area of each compartment. 1e start b& calculating out
the total cross-sectional area of the blades in each compartment
*= )' x d
' x 6 x7=(10 ft ) (0.5 ft ) (6 ) (7 )=210 ft
2
1e now compare this to the area of each compartment that the blades
co%er (width times depth+
occupied=
* blades
x x d x 100=
210 ft 2
90 ft x 14.17 ft x 100=16.5
his falls rml& between the bounds of "$-#0. herefore, the following
e!uation can be used in sol%ing for the power imparted on each shaft
P1= μ x G2 ∀
3=(2.73 x10
−5 lb−s
ft 2 )( 50
sec )2
( 54187.5 ft 3
3 )=1233 ft −lb
s
1e simpl& repeat this step for compartments # and , changing the G
%alues to match
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P2= μ x G2 ∀
3=(2.73 x10
−5 lb−s
ft 2 )( 20sec )
2
( 54187.5 ft 3
3 )=197 ft −lb
s
P3= μ x G2 ∀
3
=
(2.73 x10
−5 lb−s
ft 2
)( 10
sec
)
2
(54187.5 ft
3
3
)=49
ft −lb
s
o obtain the total energ& re!uired, we simpl& sum these
"otal po#er $ 1%&'ft −lb
s
Problem 8.%
Solution:
a+ he =asin Dimensions
! =
19,200m
3
d
1440min x 1min
60 s x2700 s
! =0.0133 x 0.0166 x 2.700=5.985
he dimensions as gi%en b&
" x " x (26.7 " )=5.985m3
26.7"3=5.985m
3
"3=0,224m
"=0.473 m
;ow, sol%ing for length
# =26.7 "=26.7 (0.473 )=12.6291m
he basin dimensions
"=0.473
# =12.6291m
b+ he paddle wheel design
D1=d−2 (1 ft )−21
2
( d' )=27.43 ft −2 (1 ft )−2
1
2
x 3.054=32.38 ft
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D2= D1−2 (1 ft )−2 ( d' )=32.38 ft −2 (1 ft )−2 (6 ft )=18.38 ft
D3= D2−2 (1 ft )−2 ( d' )=18.38 ft −2 (1 ft )−2 (3.05 ft )=10.28 ft
x=27.43 ft =n (10 ft )+2 (1 ft )+(n−1)(3.05 ft )
n=6 "heels
c+ he power to be imparted to the water in each compartment
*= )' x d
' x 6 x7=(10 ft ) (0.5 ft ) (6 ) (7 )=210 ft
2
occupied= * blades
+ x d x100=
210 ft 2
27.43 x18.38 x 100=12.38
P1= μ x G2 ∀3=(3.05 x10−5 lb−s
ft 2 )(
50sec )
2
(50000
3 )=1270.832 ft −lbs
P2= μ x G2 ∀
3=(3.05 x10
−5 lb−s
ft 2 )( 20sec )
2
( 500003 )=203.33ft −lb
s
P3= μ x G2 ∀
3=(3.05 x10
−5 lb−s
ft 2 )( 10sec )
2
( 500003 )=50.833ft −lb
s
otal power "$4.''$ft −lb
s
Problem 8.(
Problem A pneumatic occulation basin is to be designed for a tertiar&
treatment plant ha%ing a ow of $.0 MGD. he plant is to emplo& high-p
lime coagulation, and the pertinent data for the occulation basin are as
follows detention time $min, G "$0s-" (at $0) *+, length # timeswidth, depth 'ft-"0in, diHuser depth 'ft-0in, and air ow 4 cfm per
diHuser.
Determine
a+ he basin dimensions if "in increments are used.
b+ he total air ow in ftImin.
c+ he number of diHusers.
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Approach: *irst, weCll sol%e for the basin dimensions the same wa& as
was sol%ed for in the pre%ious problem. hen, we can sol%e for the total air
ow b& using a relation between power
Solution:a+ *irst, we need to calculate the %olume of the basin. 1e accomplish this
through the following
∀=Q x θ=5 x 10
6gals
1day x
1day
24 hours x 1hour
60min x 5 x10
6gals
7.48gal x5minutes=2321 ft
3
1e now tae this %olume and e!uate it to the following
∀=" x ) x d )=2" d=9 ft −10∈(9.8333 ft )∴ ∀
9.833 ft =2"
2
"=√ ∀
2 x 9.8333=√
2321 ft 3
2 x 9.8333=10.86 feet ≈10 ft −10∈¿
;ow, sol%ing for length
)=2"=2 x 10.86 feet =21.72 feet ≈21 ft −9∈¿
<ummar&
=asin Dimensions "0ft-"0in x #"ft-'in x 'ft-"0in
b+ o begin, weCll sol%e for the power
P=G2
+ ∀= (150 s−1 )2 x (2.73 x 10
−5 ) x (10.8333 ft x 21.75 ft x 9.8333 ft )
¿1423,2ft −lb
sec
;ow, we use this power in the following e!uation to sol%e for air ow
P=, 1Ga log ( h+c2
c2)
1here
h height of diHuser
J" ?".$ (=ritish Enits+
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c# 4 (=ritish Enits+
Kearranging and sol%ing
Ga= P
, 1 log
(h+c2
c2 )=
1423.2
81.5 x log
(9 ft +34
34 )
=171.2 ft
3
min
c+ *or this, we simpl& di%ide the total air ow pro%ided b& the amount
re!uired per diHuser (4
cfm+
Diffusers=171.2
ft 3
min
4 ft
3
min per diffuser
=42.8diffusers⇾ 43diffusers
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Problem 8.&
a+ =asin Dimension
! =875 m
3
20 min x
1min
60 s x 35 s
! =43.75 x 0.0166 x35=25.520m3
he dimensions as gi%en b&
" x " x (1.25" )=25.520m3
1.25 "3=25.520 m
3
"=2.247 m
;ow, sol%ing for length
# =1.25"=1.25 (2.247 )=2.809m
he basin dimensions
"=2.247
# =2.809m
b+ Fmpeller Diameter
c+ Fmpeller <peed
Kr=1.54 K t =7.0 d=30
*irst, we need to calculate the power imparted
W =G2 x μ=(35)2 x(0.00131)=1.604
$ −m
s−m
;ow, we can sol%e for the total power
P=W x ∀=1.60475 x 25,520=40.95322
*or this, we simpl& need the following e!uation
n=( 40.95322
1.65 x 0.3 x 94600 )1/3
=( 40.95322
46827 )1/ 3
=3√ 8.7456=0,00295=1.74 rpm
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Problem 8.8
a. =asin Dimension
! = 94600
20min x 1 min
60s x 35s
! =4730 x0.0166 x35=2759.167 m3
he dimensions as gi%en b&
" x " x (1.25" )=2759.167m3
1.25"3=2759.167 m
3
"=6.854 m
;ow, sol%ing for length
# =1.25"=1.25 (6.854 )=8.567m
he basin dimensions
"=6.854
# =8.567m
b. Fmpeller Diameter
c. Fmpeller <peed
Kr=1.65 Kt =7.0 d=30
*irst, we need to calculate the power imparted
W =G2 x μ=6.854 x 1.25=8.5675 m
;ow, we can sol%e for the total power
P=W x ∀=8.5675 x 2759.167=19355.413
*or this, we simpl& need the following e!uation
n=( 19355.413
1.65 x 0.3 x94600 )1/3
=( 19355.41346827 )1 /3
=0,64 rps=38.57rpm