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7/23/2019 Recipientes Horizontales-Volumen http://slidepdf.com/reader/full/recipientes-horizontales-volumen 1/15 Input Calculated  Di LLL L  b b/Di =  1/ 4 K1 =  1/ 2 Di= 1350 L= 3900 NL= 1080 b = 337 1/ 2 alpha = 2.21 V total = 6226354828.13 mm3 = 6.23 m3 f(Ze)2= 0.90 f(Zc)= 0.8576468043 V2= 5364716831.45 mm3 5.36 m3 189.45 Verificación de Velocidad de la tabla 111 de M40-1D t ()= 300 N!"(#in)= 1 0.63 Din (in)= 1.939 (Schedule 80 N!" 2 a(in2)= 2.95 0.0205 !t2 $%ull pipe= 75.00" aefect(in2)= 2.21 0.0154 !t2 &el(ft/) 41.063 '(ft/)= total =1 / 6 × π ×  K 1 ×  D 3 + 1 / 4 × π ×  D 2 ×  L  K 1 = 2 ×( b /  D )  parcial =1 / 6 × π ×  K 1 ×  D 3 ×  ( Ze 2 )+ 1/ 4 × π ×  D 2 ×  L× f  ( Ze )=− (  NL  D  ) 2 × ( 3 +  NL  D  ) α =2×  A tan (  NL 2×  NL×  D 2  NL 2 )

Recipientes Horizontales-Volumen

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Input

Calculated

  Di

LLL

L

  b

b/Di =   1/ 4K1 =   1/ 2Di= 1350L= 3900

NL= 1080

b = 337 1/ 2

alpha = 2.21V total = 6226354828.13 mm3 = 6.23 m3

f(Ze)2= 0.90

f(Zc)= 0.8576468043

V2= 5364716831.45 mm3 5.36 m3 189.45

Verificación de Velocidad de la tabla 111 de M40-1D

t ()= 300 N!"(#in)= 1

0.63

Din (in)= 1.939 (Schedule 80 N!" 2

a(in2)= 2.95 0.0205 !t2

$%ull pipe= 75.00"

aefect(in2)= 2.21 0.0154 !t2

&el(ft/) 41.063

'(ft/)=

V total=1/6×π × K 1× D3+1/4×π × D2× L

 K 1=2×(b/ D )

V  parcial=1/6×π × K 1× D3×f  (Ze2 )+1/4×π × D2× L×f

f  ( Ze)=−( NL D )2

×(−3+ NL

 D )α =2× A tan

(

  NL

√2× NL×

 D

2

− NL2

)

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!t3

1/4×π × D2× L

4×π × D2× L×f (Zc )

−3+ NL

 D )

D

2

− NL2

)

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Input

Calculated

  Di

LLL

L

  b

b/Di =   1/ 4K1 =   1/ 2Di= 1900L= 5700

NL= 1080

b = 475

alpha = 1.71V total = 17956290416.67 mm3 = 17.96 m3

f(Ze)2= 0.60

f(Zc)= 0.5868610423

V2= 10565015030.66 mm3 10.57 m3 373.10

Verificación de Velocidad de la tabla 111 de M40-1D

t ()= 300 N!"(#in)= 1

1.24

Din (in)= 1.939 (Schedule 80 N!" 2

a(in2)= 2.95 0.0205 !t2

$%ull pipe= 75.00"

aefect(in2)= 2.21 0.0154 !t2

&el(ft/) 80.867

'(ft/)=

V total=1/6×π × K 1× D3+1/4×π × D2× L

 K 1=2×(b/ D )

V  parcial=1/6×π × K 1× D3×f  (Ze2 )+1/4×π × D2× L×f

f  ( Ze)=−( NL D )2

×(−3+ NL

 D )α =2× A tan

(

  NL

√2× NL×

 D

2

− NL2

)

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!t3

/4×π × D2× L

×π × D2× L×f (Zc )

3+ NL

 D )

− NL2

)

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Input

Calculated

  Di

LLL

L

  b

b/Di =   1/ 4K1 =   1/ 2Di= 2134L= 9144

NL= 700

b = 533 1/ 2

alpha = 1.22V total = 35248222459.67 mm3 = 35.25 m3

f(Ze)2= 0.25

f(Zc)= 0.2854374247

V2= 9976618461.09 mm3 9.98 m3 352.32

Verificación de Velocidad de la tabla 111 de M40-1D

t ()= 300 N!"(#in)= 1

1.17

Din (in)= 1.939 (Schedule 80 N!" 2

a(in2)= 2.95 0.0205 !t2

$%ull pipe= 75.00"

aefect(in2)= 2.21 0.0154 !t2

&el(ft/) 76.364

'(ft/)=

V total=1/6×π × K 1× D3+1/4×π × D2× L

 K 1=2×(b/ D )

V  parcial=1/6×π × K 1× D3×f  (Ze2 )+1/4×π × D2× L×f

f  ( Ze)=−( NL D )2

×(−3+ NL

 D )α =2× A tan

(

  NL

√2× NL×

 D

2

− NL2

)

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!t3

/4×π × D2× L

×π × D2× L×f (Zc )

3+ NL

 D )

− NL2

)

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#$S% D% D$&'S $)$ D*$M%&)'S D% &+#%),$S

SS 1/8 1/4 3/8 1/2 3/4 1

10203040 0.269 0.364 0.493 0.622 0.824 1.04960

80 0.215 0.302 0.423 0.546 0.742 0.957100120

140160 0.466 0.612 0.815

S&D 0.269 0.364 0.493 0.622 0.824 1.049S 0.215 0.302 0.423 0.546 0.742 0.957

S 0.252 0.434 0.5995S 0.71 0.92 1.185

10S 0.307 0.41 0.545 0.674 0.884 1.097

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1 1/4 1 1/2 2 2 1/2 3 3 1/2 4

1.38 1.61 2.067 2.469 3.068 3.548 4.026

1.278 1.5 1.939 2.323 2.9 3.364 3.826

3.624

1.16 1.338 1.687 2.125 2.624 3.4381.38 1.61 2.067 2.469 3.068 3.548 4.026

1.278 1.5 1.939 2.323 2.9 3.364 3.8260.896 1.1 1.503 1.771 2.3 3.1521.53 1.77 2.245 2.709 3.334 3.834 4.334

1.442 1.682 2.157 2.635 3.26 3.76 4.26

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5 6 8 10 12 14 16

13.5 15.58.125 10.25 12.25 13.376 15.3768.071 10.136 12.09 13.25 15.25

5.047 6.065 7.981 10.02 11.938 13.124 157.813 9.75 11.626 12.812 14.688

4.813 5.761 7.625 9.562 11.374 12.5 14.3127.437 9.312 11.062 12.124 13.938

4.563 5.501 7.187 9.062 10.75 11.812 13.562

7.001 8.75 10.5 11.5 13.1244.313 5.187 6.813 8.5 10.126 11.188 12.8125.047 6.065 7.981 10.02 12 13.25 15.254.813 5.761 7.625 9.75 11.75 13 154.063 4.897 6.875 8.75 10.755.345 6.407 8.407 10.482 12.438 13.688 15.675.295 6.357 8.329 10.42 12.39 13.624 15.624

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18 20 22 24 26 28 30

17.5 19.5 21.5 23.5 25.376 27.376 29.37617.376 19.25 21.25 23.25 25 27 2917.124 19 21 22.876 26.75 28.7516.876 18.812 22.624

16.5 18.376 20.25 22.062

16.124 17.938 19.75 21.56215.688 17.438 19.25 20.93815.25 17 18.75 20.376

14.876 16.5 18.25 19.87614.438 16.062 17.75 19.31217.25 19.25 21.25 23.25 25.25 27.25 29.25

17 19 21 23 25 27 29

17.67 19.624 21.624 23.564 29.517.624 19.564 21.564 23.5 29.376

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32 34 36

31.376 33.312 35.37631 33 3531.75 32.75 34.75

30.624 32.624 34.5

31.25 33.25 35.2531 33 35

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'l ate Input

Calculated

  Di

LLL

L

  b

b/Di =   1/ 4K1 =   1/ 2

Di= 2000L= 1400LLL= 704.80

b = 500

alpha = 1.27V &'&$= 6492433333.33 mm3 = 6.49 m3

f(Ze)2= 0.29

f(Zc)= 0.3148454344

V2= 1981671956.61 mm3 1.98 m3 69.98 !t31384721704.82 1.381683196830.72 1.68 0.30 1.68

Verificación de Velocidad de la tabla 111 de M40-1D

t ()= 2100 N!"(#in)= 2

0.03

Din (in)= 3.068 S&D N!"

a(in2)= 7.39 0.0513 !t2

$%ull pipe= 75.00"

aefect(in2)= 5.54 0.0385 !t2

&el(ft/) 0.866

'(ft/)=

V total=1/6×π × K 1× D3+1/4×π × D2× L

 K 1=2×(b/ D )

V  parcial=1/6×π × K 1× D3×f  (Ze2 )+1/4×π × D2× L× f (Zc )

f  ( Ze)=−( LLL D )2

×(−3+2× LLL

 D   )

α =2× A tan (  LLL

√2× LLL× D

2− LLL2 )

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Input

Calculated

  Di

LLL

L

  b

b/Di =   1/ 4K1 =   1/ 2

Di= 4700L= 10500

LLL= 1050

b = 1175

alpha = 0.98

f(Ze)2= 0.13

f(Zc)= 0.1667252641

V2= 33834812143.73 mm3 33.83 m3 1194.87 !t3

Vhc= 31853140187.12 mm3 31.85 m3 1124.88 !t3

Verificación de Velocidad de la tabla 111 de M40-1D

t ()= 500 N!"(#in)= 2

2.25

Din (in)= 6.065 (S&D N!"

a(in2)= 28.89 0.2006 !t2

$%ull pipe= 75.00"

aefect(in2)= 21.67 0.1505 !t2

&el(ft/) 14.952

'(ft/)=

V total=1/6×π × K 1× D3+1/4×π × D2× L

 K 1=2×(b/ D )

V  parcial=1/6×π × K 1× D3×f  (Ze2 )+1/4×π × D2× L×f (Zc )

f  (Ze)=−( LLL D )2

×(−3+2× LLL

 D   )

α =2× A tan(  LLL

√2× LLL× D

2− LLL2 )

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×f (Zc )

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×f (Zc )