Hidroestatica
"
" $ #
" #
% " $ ' " ( " ) " *
" &
" +
"
,
∆x1 = v1∆t ∆x2 = v2 ∆t
∆m1 = ρ A1v1∆t
dV
∆m2 = ρ A2 v2 ∆t
dV
Por conservacio′n de la masa : ∆m1 = ∆m2A1v1 = A2 v2 ecuacio′n de la continuidad
Av = constante.
Q = Av donde Q es el gasto o caudal.
# ! . ! /
-
$
De acuerdo al teorema del trabajo y la energia 1 1 2 P A1 (∆x1 ) − P2 A2(∆x2 ) − ∆mg ( y2 − y1 ) = ∆mv2 − ∆mv12 1 2 2
P A(∆x ) − P2 A(∆x ) − ∆mg ( y2 − y1 ) = 1
1 1 2 ∆mv2 − ∆mv12 2 2
∆m = ρ∆V = ρA∆x
1 1 2 P A(∆x ) − P2 A(∆x ) − ρA∆xg ( y2 − y1 ) = ρA∆xv2 − ∆mv12 1 22
P A(∆x ) − P2 A(∆x ) − ρA∆xg ( y2 − y1 ) = 1 P − P2 − ρg ( y2 − y1 ) = 1
0
1 1 2 ρA∆xv2 − ρA∆xv12 2 2 1 2 1 2 ρv2 − ρv1 2 2
1 2 1 2 P + ρv1 + ρgy1 = P2 + ρv2 + ρgy2 1 2 2 1 2 P + ρv +ρgy = constante 2
"
1 2 4 5 " 6"04 3 3
2
,
!
1 2 P + ρv = constante 2
" + #
!
(P3 − P4 ) = ρ ′gh
P+ 1
(1)
ρ ρ
1 2 1 ρv1 = P2 + ρv 2 2 2 2
1 (P1 − P2 ) = ρ 2
A1A2
2
−1 v
2 1
(2)
(
P3 = P + ρgy1 1 P4 = P2 + ρgy2
0 7 )8 7 (8
(3) (4)
2 1 A12 − A2 2 ρ ′gh = ρ v1 + ρgh 2 A2 2
(P3 − P4 ) = (P1 − P2 ) + ρg ( y1 − y2 )
v1 = A2
2 gh(ρ′ − ρ ) ρ A12 − A22
(
)
Aplicando Bernoulli entre (1) y(2) : 1 P0 + ρv12 + ρgy1 = P0 + ρgy2 2
+
1 2 ρv1 = + ρgy2 − ρgy1 2 1 2 ρv1 = + ρgh 2
+
1 2 ρv1 = + ρg ( y2 − y1 ) 2
+v1 = 2 gh
"
1 2 1 2 Pa + ρva = Pb + ρvb 2 2 Pb = Pa + 1 2 ρva 2
=0
Pb = Pa + ρ ′gh
1 2 ρva = ρ ′gh 2
va =
2 ρ ′gh
ρ
P+ 1
1 2 1 2 ρv1 + ρgH = P2 + ρv2 + 0 2 2
P =3atm = 3.04 ×105 Pascal 1
P+ 1
9(
v2 =
1 2 1 2 ρv1 + ρgH = P2 + ρv2 2 2
2 P − 2 P2 + 2 gH 1
ρ
=
2 P − 2 ρgh + 2 ρgH 1
ρ
v2 =
2 P + 2 ρg (H − h ) 1
ρ
2 3.04 ×105 +2(1000)(9.8)(5 − 0.5) m/s = 1000
(
)
v2 = 25.5 m
s
Q = Av2 =
πd 2
4
v2 =
π (0.03m )2
4
m3 25.5 m = 0.018 s s
:
1
Av = av2
9; #<
A −
dy = a 2 gy dt
#
v2...
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