discusion 1 (1)
TRANSCRIPT
-
8/16/2019 Discusion 1 (1)
1/20
RESULTADOS
TABLA DE DATOS TEÓRICOS
Tabla 1
Condiciones de Laboratorio
Tabla 2
Propiedades físicas del fluido y delsólido
TABLA DE DATOS
EXPERIMENTALES
TABLA 3
Datos experimentales en columna sinlecho
T(°C) P(mm
Hg)21 756
Densidad del agua a 22ºC(Kg/m3)
997.77
Viscosidad del agua a 22ºC(Kg/ms)
0.000958
Peso espec!co del CCl"(Kg#/m3)
1595
Peso espec!co del H2$ (Kg#/m3) 997.8
%&a'edad (Kgmm/Kg#s2) 9.81
Dime*&o de pa&*cula (m) 6.2*10^-4
Densidad del s+lido Kg/m3) 2198.424
,P (mmCCl")
V (ml) T (seg) - (m/s)
35 5.31 6.591
36 5.77 6.239
37 5.88 6.293
37 5.99 6.177
2 92 5.46 16.850
93 5.64 16.489
85 5.09 16.699
96 5.74 16.725
92 5.45 16.881
83 5.01 16.567
88 5.31 16.573
86 5.24 16.412
3 124 5.48 22.628
124 5.46 22.711
118 5.31 22.222
110 4.91 22.403
120 5.39 22.263
" 155 5.59 27.728
140 4.91 28.513
146 5.09 28.684
140 4.93 28.398
140 4.91 28.513
150 5.31 28.249
160 5.63 28.419
154 5.41 28.466
180 5.18 34.749
184 5.32 34.586
168 4.90 34.286
186 5.44 34.191
0 200 5.21 38.388
204 5.32 38.346
210 5.47 38.391
198 5.19 38.150
192 5.03 38.171
198 5.19 38.150
200 5.22 38.314
1 256 6.00 42.667
210 4.91 42.770218 5.11 42.661
210 4.93 42.596
206 4.83 42.650
222 5.19 42.775
9 226 4.94 45.749
212 4.65 45.591
222 4.88 45.492
204 4.32 47.222
244 4.76 51.261
250 4.90 51.020244 4.74 51.477
300 5.16 58.140
280 4.81 58.212
310 5.28 58.712
305 5.34 57.116
310 5.43 57.090
-
8/16/2019 Discusion 1 (1)
2/20
TABLA 4.
Datos experimentales en columna con lecho
TABLA 4.1
Datos experimentales en columna con lecho en ascenso
H a&ena
(cm)
,P (cm
CCl")
V (ml) T (seg)
2" 0 0 0
2" 2.5 15 40.52
2" 4.2 14 27.29
2" 6.5 46 28.75
2" 7.8 48.5 21
2" 9.3 72 23.81
2" 11 77 27.52
2" 14 108 29.23
2" 15.6 96 27.52
2" 16.4 92 19.892" 18.1 98 19.75
-
8/16/2019 Discusion 1 (1)
3/20
2" 19.1 97 17.24
2" 20.9 75 15.72
2" 22.3 97 14.57
2" 23.8 110 15.77
2" 25.5 103 13.76
2" 26.5 77 11.03
2" 28.1 97 10.56
2" 29.4 86 10.03
2" 30.7 95 10.3
2" 33.1 100 10.39
2" 34.5 97 9.17
2".2 33.4 122 10.95
2". 33.4 136 11.32
2".1 33.5 138 11.24
2 33.5 152 11.75
2.2 33.3 159 11.9
2." 33.3 193 14.4
2.0 33.3 160 11.2
2.1 33.1 164 10.91
20 33.1 172 11.48
20.2 33.1 171 10.92
20.3 33 190 12.03
20.7 33 194 11.26
20.1 32.9 179 10.26
27 32.8 196 11
27. 32.75 199 10.71
27.2 32.8 190 10.21
27." 32.8 231 11.82
27. 32.8 203 10.26
27.7 32.8 230 11.38
27.1 32.7 219 9.38
21 32.7 212 9.56
21. 32.8 234 10.42
21.2 32.8 245 10.69
21. 32.8 168 7.1421.7 32.8 180 7.25
21.9 32.95 222 8.73
29 33 160 6.18
29.2 32.9 200 7.51
29." 33 217 8
29.0 33 155 5.66
29.7 33 207 7.31
29.1 33.2 228 7.76
3. 33.2 230 7.71
3.2 33.2 148 4.793." 33.3 170 5.38
-
8/16/2019 Discusion 1 (1)
4/20
3.0 33.5 190 6.11
3.9 33.6 208 6.3
3. 33.7 208 6.35
3.7 33.9 158 4.46
32.2 34.1 200 5.54
32.3 34.3 246 6.61
32. 34.3 210 5.45
32.1 34.4 206 5.28
33.1 35.1 228 5.69
3".2 35.1 224 5.49
3".9 35.3 244 5.91
3." 35.3 204 4.66
30 35 240 5.45
30.0 35.6 185 4.16
37. 35.6 234 5.2
37.0 35.9 206 4.4
31.2 36 203 4.27
39.3 36.2 249 5.11
39.9 36.3 226 4.37
". 36.4 154 3.08
".2 36.4 229 4.3
".1 36.5 244 4.58
"2." 36.6 250 4.47
"3.2 36.7 178 3.15
"". 36.7 222 3.72
""." 36.8 198 3.28
".7 38.9 154 2.55
TABLA 4.1
Datos experimentales en columna con lecho en reersa
H a&ena(cm)
,P (cmCCl")
V (ml) T (seg)
".2 37.0 180 2.93
"". 37.0 239 4.03
"".2 37.0 213 3.7
"3.0 37.0 238 4.27
"3. 37.0 235 4.29
"2.1 37.0 198 3.56
"2. 37.0 189 3.54
". 36.9 219 4.09
".0 36.7 212 4.1
".2 36.7 194 3.81
39.1 36.7 200 3.85
39. 36.7 216 4.44
31. 36.5 166 3.34
31 36.5 198 4.26
-
8/16/2019 Discusion 1 (1)
5/20
37. 36.5 204 4.59
30.0 36.3 172 3.8
3.9 36.3 190 4.43
3. 36.1 173 4.05
3".1 36.0 176 4.34
32.3 35.9 186 4.69
33." 35.8 248 6.56
32.9 35.6 194 5.34
32. 35.1 177 5.08
3.7 35.0 190 5.43
3." 34.9 194 5.96
3.9 34.7 192 6.05
3." 34.6 174 5.66
29.9 34.5 197 6.78
29. 34.3 207 7.38
29. 34.2 198 7.3
21.0 34.2 198 8.1
21.2 34.1 202 8.24
27.7 34.1 153 7.32
27 34.0 146 7.55
20. 33.7 137 7.95
2.3 33.4 142 9.24
2".9 32.6 108 7.93
2".7 31.2 109 9.05
2".0 25.8 102 9.3
2"." 28.0 73 7.31
2".3 24.7 74 8.04
2".2 21.4 66 8.36
2" 19.3 60 8.9
2" 17.8 54 8.9
2" 16.2 42 7.65
2" 14.4 45 8.9
2" 13.0 35 7.92
2" 11.6 32 8.33
2" 10.2 33 9.182" 8.9 32 10.26
2" 7.5 31 11.12
2" 6.4 31 13.58
2" 5.4 26 13.82
2" 3.6 23 16.7
2" 2.6 16 17.13
2" 1.5 14 19.54
2" 1.0 12 26.37
2" 0.6 13 49.77
2" 0.4 10 94.222" 0.0 0 0
-
8/16/2019 Discusion 1 (1)
6/20
TABLA 5
Datos de la columna
Dime*&o
Dime*&o e*e&no(mm)
57
4speso& (mm) 2.2
Dime*&o in*e&no(mm)
52.6
TABLA 6Datos de la arena
TABLA 6.1
Datos para calcular la densidad aparente
P&ue5a P&ue5a
2
6 p&o5e*a (g) 90.4 112
6 p&o5e*a a&ena (g)
157.2 239.4
Volumen a&ena(ml)
50 100
6 a&ena 66.8 127.4TABLA 6.2
Datos para calcular la densidad absoluta
P&ue5a
P&ue5a2
6 p&o5e*a (g) 90.4 91.8
6 p&o5e*a agua(g)
120.4 119.3
Volumen agua (ml) 31 27.5
6 p&o5e*a agua a&ena (g)
159 233.4
Volumen agua
a&ena (ml)46 85
6 agua a&ena(g)
68.6 141.6
TABLA 6.3
!n"lisis #ranulom$trico de la arena
8allaPeso(g)
1 2
0
2 3 408.33 " 271.7
-
8/16/2019 Discusion 1 (1)
7/20
" 0
TABLA DE RESULTADOS
TABLA 7
C"lculo del di"metro de partículas
8allaPeso(g&)
Diam.P&om.(mm)
&accion:e*enida
(;i)
;i /Dpm
(mm)
12 0 0 0 0
23 408.3 0.725 0.600 0.828
3" 217.7 0.513 0.400 0.78
" 0 0 0 0
< 680 1.000 1.608Dp (m) 6.20E-04
TABLA 8
C"lculo del Caudal% flu&o m"sico% numero de 'eynold y la caída de presión experimental en ascenso
H(arena ) cm
∆P (cm CCl4) V(ml)
T(seg)
Q(ml/s)
G(kg/s)
Gs(Kg/s.m
2)
:e =Pepe&im
e*al(>g#/m2
)
Total Lecho
24 0 0.0 0.0 0 0 0 0 0 0
24 2.5 2.5 15.0 40.52 0.37 0.0004 0.18 0.12 14.93
24 4.2 4.2 14.0 27.29 0.51 0.0005 0.23 0.15 25.08
24 6.5 6.5 46.0 28.75 1.6 0.0016 0.74 0.48 38.82
24 7.8 7.8 48.5 21 2.31 0.0023 1.06 0.69 46.58
24 9.3 9.3 72.0 23.81 3.02 0.003 1.38 0.89 55.54
24 11 11.0 77.0 27.52 2.8 0.0028 1.29 0.83 65.69
24 14 14.0 108.
0
29.23 3.69 0.0037 1.71 1.11 83.61
24 15.6 15.6 96.0 27.52 3.49 0.0035 1.61 1.04 93.16
24 16.4 16.4 92.0 19.89 4.63 0.0046 2.12 1.37 97.94
24 18.1 18.0 98.0 19.75 4.96 0.0049 2.26 1.46 107.5
-
8/16/2019 Discusion 1 (1)
8/20
24 19.1 19.0 97.0 17.24 5.63 0.0056 2.58 1.67 113.47
24 20.9 20.8 75.0 15.72 4.77 0.0048 2.21 1.43 124.22
24 22.3 22.2 97.0 14.57 6.66 0.0066 3.04 1.97 132.58
24 23.8 23.7 110.
0
15.77 6.98 0.007 3.23 2.09 141.54
24 25.5 25.4 103.0
13.76 7.49 0.0075 3.46 2.24 151.69
24 26.5 26.4 77.0 11.03 6.98 0.007 3.23 2.09 157.66
24 28.1 28.0 97.0 10.56 9.19 0.0092 4.24 2.74 167.22
24 29.4 29.3 86.0 10.03 8.57 0.0086 3.96 2.56 174.98
24 30.7 30.6 95.0 10.3 9.22 0.0092 4.24 2.74 182.74
24 33.1 33.0 100.
0
10.39 9.62 0.0096 4.42 2.86 197.08
24 34.5 34.4 97.0 9.17 10.58 0.0106 4.88 3.16 205.44
24.2 33.4 33.3 122.
0
10.95 11.14 0.0111 5.12 3.31 198.87
24.5 33.4 33.2 136.0
11.32 12.01 0.012 5.53 3.58 198.27
24.8 33.5 33.3 138.
0
11.24 12.28 0.0123 5.67 3.67 198.87
25 33.5 33.3 152.
0
11.75 12.94 0.0129 5.94 3.84 198.87
25.2 33.3 33.1 159.
0
11.9 13.36 0.0133 6.13 3.97 197.67
25.4 33.3 33.1 193.
0
14.4 13.4 0.0134 6.18 4 197.67
25.6 33.3 33.1 160.
0
11.2 14.29 0.0143 6.59 4.26 197.67
25.8 33.1 32.9 164.
0
10.91 15.03 0.015 6.91 4.47 196.48
26 33.1 32.9 172.
0
11.48 14.98 0.0149 6.87 4.45 196.48
26.2 33.1 32.9 171.
0
10.92 15.66 0.0156 7.19 4.65 196.48
26.3 33 32.8 190.
0
12.03 15.79 0.0158 7.28 4.71 195.88
26.7 33 32.8 194.
0
11.26 17.23 0.0172 7.93 5.13 195.88
26.8 32.9 32.7 179.
0
10.26 17.45 0.0174 8.02 5.19 195.28
27 32.8 32.5 196.
0
11 17.82 0.0178 8.2 5.31 194.09
27.1 32.75 32.5 199.
0
10.71 18.58 0.0185 8.53 5.52 194.09
27.2 32.8 32.5 190.
0
10.21 18.61 0.0186 8.57 5.55 194.09
27.4 32.8 32.5 231.
0
11.82 19.54 0.0195 8.99 5.82 194.09
27.5 32.8 32.5 203.
0
10.26 19.79 0.0197 9.08 5.88 194.09
27.7 32.8 32.5 230.
0
11.38 20.21 0.0202 9.31 6.03 194.09
27.8 32.7 32.3 219.
0
9.38 23.35 0.0233 10.74 6.95 192.9
28 32.7 32.4 212.
0
9.56 22.18 0.0221 10.18 6.59 193.49
-
8/16/2019 Discusion 1 (1)
9/20
28.1 32.8 32.5 234.
0
10.42 22.46 0.0224 10.32 6.68 194.09
28.2 32.8 32.5 245.
0
10.69 22.92 0.0229 10.55 6.83 194.09
28.5 32.8 32.4 168.
0
7.14 23.53 0.0235 10.83 7.01 193.49
28.7 32.8 32.4 180.
0
7.25 24.83 0.0248 11.43 7.4 193.49
28.9 32.95 32.6 222.
0
8.73 25.43 0.0254 11.71 7.58 194.69
29 33 32.6 160.
0
6.18 25.89 0.0258 11.89 7.69 194.69
29.2 32.9 32.5 200.
0
7.51 26.63 0.0266 12.26 7.93 194.09
29.4 33 32.6 217.
0
8 27.13 0.0271 12.49 8.08 194.69
29.6 33 32.6 155.
0
5.66 27.39 0.0273 12.58 8.14 194.69
29.7 33 32.6 207.0
7.31 28.32 0.0283 13.04 8.44 194.69
29.8 33.2 32.7 228.
0
7.76 29.38 0.0293 13.5 8.74 195.28
30.1 33.2 32.7 230.
0
7.71 29.83 0.0298 13.73 8.89 195.28
30.2 33.2 32.7 148.
0
4.79 30.9 0.0308 14.19 9.18 195.28
30.4 33.3 32.8 170.
0
5.38 31.6 0.0315 14.52 9.4 195.88
30.6 33.5 33.0 190.
0
6.11 31.1 0.031 14.29 9.25 197.08
30.9 33.6 33.1 208.
0
6.3 33.02 0.0329 15.16 9.81 197.67
31.1 33.7 33.2 208.
0
6.35 32.76 0.0327 15.07 9.75 198.27
31.7 33.9 33.3 158.
0
4.46 35.43 0.0354 16.31 10.5
6
198.87
32.2 34.1 33.5 200.
0
5.54 36.1 0.036 16.59 10.7
4
200.06
32.3 34.3 33.7 246.
0
6.61 37.22 0.0371 17.1 11.0
7
201.26
32.5 34.3 33.7 210.
0
5.45 38.53 0.0384 17.7 11.4
6
201.26
32.8 34.4 33.7 206.
0
5.28 39.02 0.0389 17.93 11.6 201.26
33.8 35.1 34.4 228.
0
5.69 40.07 0.04 18.43 11.9
3
205.44
34.2 35.1 34.4 224.
0
5.49 40.8 0.0407 18.76 12.1
4
205.44
34.9 35.3 34.6 244.
0
5.91 41.29 0.0412 18.99 12.2
9
206.63
35.4 35.3 34.6 204.
0
4.66 43.78 0.0437 20.14 13.0
3
206.63
36 35 34.2 240.
0
5.45 44.04 0.0439 20.23 13.0
9
204.24
36.6 35.6 34.8 185.
0
4.16 44.47 0.0444 20.46 13.2
4
207.83
37.1 35.6 34.8 234.
0
5.2 45 0.0449 20.69 13.3
9
207.83
-
8/16/2019 Discusion 1 (1)
10/20
37.6 35.9 35.1 206.
0
4.4 46.82 0.0467 21.52 13.9
3
209.62
38.2 36 35.2 203.
0
4.27 47.54 0.0474 21.84 14.1
3
210.21
39.3 36.2 35.3 249.
0
5.11 48.73 0.0486 22.4 14.5 210.81
39.9 36.3 35.4 226.
0
4.37 51.72 0.0516 23.78 15.3
9
211.41
40.5 36.4 35.5 154.
0
3.08 50 0.0499 23 14.8
9
212.01
41.2 36.4 35.5 229.
0
4.3 53.26 0.0531 24.47 15.8
4
212.01
41.8 36.5 35.6 244.
0
4.58 53.28 0.0532 24.52 15.8
7
212.6
42.4 36.6 35.6 250.
0
4.47 55.93 0.0558 25.71 16.6
4
212.6
43.2 36.7 35.7 178.
0
3.15 56.51 0.0564 25.99 16.8
2
213.2
44.1 36.7 35.6 222.0
3.72 59.68 0.0595 27.42 17.75
212.6
44.4 36.8 35.7 198.
0
3.28 60.37 0.0602 27.74 17.9
5
213.2
45.7 38.9 37.8 154.
0
2.55 60.39 0.0603 27.79 17.9
9
225.74
TABLA 9
C"lculo del Caudal% flu&o m"sico% numero de 'eynold y la caída de presión experimental en reersa
Harena (cm)
,P (cmCCl")
V(ml)
T(seg)
-(ml/s)
%(>g/s)
%s(Kg/s.m2)
:e =Pepe&im
e*al(>g#/m2)To*al ?ec@o
45.2 37.00 35.87 180 2.93 61.43 0.0613 28.25 18.34
214.23
44.5 37.00 35.92 239 4.03 59.31 0.0592 27.28 17.711
214.53
44.2 37.00 35.96 213 3.7 57.57 0.0574 26.45 17.172
214.76
43.6 37.00 36.00 238 4.27 55.74 0.0556 25.62 16.633
215
43.1 37.00 36.02 235 4.29 54.78 0.0547 25.21 16.367
215.12
42.8 37.00 36.00 198 3.56 55.62 0.0555 25.58 16.607
215
42.1 37.00 36.05 189 3.54 53.39 0.0533 24.56 15.945
215.3
41.1 36.85 35.90 219 4.09 53.55 0.0534 24.61 15.977
214.41
40.6 36.70 35.79 212 4.1 51.71 0.0516 23.78 15.438
213.75
40.2 36.70 35.80 194 3.81 50.92 0.0508 23.41 15.198
213.81
39.8 36.70 35.78 200 3.85 51.95 0.0518 23.87 15.4
97
213.69
39.1 36.65 35.80 216 4.44 48.65 0.0485 22.35 14.5 213.81
-
8/16/2019 Discusion 1 (1)
11/20
1
38.5 36.50 35.63 166 3.34 49.7 0.0496 22.86 14.841
212.79
38 36.50 35.70 198 4.26 46.48 0.0464 21.38 13.88
213.21
37.5 36.50 35.74 204 4.59 44.44 0.0443 20.41 13.25
213.45
36.6 36.30 35.52 172 3.8 45.26 0.0452 20.83 13.523
212.14
35.9 36.30 35.57 190 4.43 42.89 0.0428 19.72 12.803
212.43
35.5 36.10 35.37 173 4.05 42.72 0.0426 19.63 12.744
211.24
34.8 36.00 35.32 176 4.34 40.55 0.0405 18.66 12.114
210.94
32.3 35.90 35.24 186 4.69 39.66 0.0396 18.25 11.8
48
210.46
33.4 35.80 35.17 248 6.56 37.8 0.0377 17.37 11.277
210.05
32.9 35.60 35.00 194 5.34 36.33 0.0362 16.68 10.829
209.03
32.1 35.10 34.53 177 5.08 34.84 0.0348 16.04 10.413
206.22
31.7 35.00 34.43 190 5.43 34.99 0.0349 16.08 10.439
205.63
31.4 34.90 34.38 194 5.96 32.55 0.0325 14.98 9.725
205.33
30.9 34.70 34.19 192 6.05 31.74 0.0317 14.61 9.485
204.19
30.4 34.60 34.11 174 5.66 30.74 0.0307 14.15 9.186
203.72
29.9 34.50 34.04 197 6.78 29.06 0.029 13.36 8.674
203.3
29.5 34.30 33.86 207 7.38 28.05 0.028 12.9 8.375
202.22
29.1 34.20 33.78 198 7.3 27.12 0.0271 12.49 8.109
201.74
28.6 34.20 33.83 198 8.1 24.44 0.0244 11.24 7.297
202.04
28.2 34.10 33.73 202 8.24 24.51 0.0245 11.29 7.33 201.4527.7 34.10 33.79 153 7.32 20.9 0.0209 9.63 6.25
2201.8
27 34.00 33.72 146 7.55 19.34 0.0193 8.89 5.772
201.39
26.1 33.70 33.46 137 7.95 17.23 0.0172 7.93 5.148
199.83
25.3 33.40 33.19 142 9.24 15.37 0.0153 7.05 4.577
198.22
24.9 32.60 32.42 108 7.93 13.62 0.0136 6.27 4.071
193.62
24.7 31.20 31.04 109 9.05 12.04 0.012 5.53 3.59 185.3824.6 25.80 25.66 102 9.3 10.97 0.0109 5.02 3.25 153.25
-
8/16/2019 Discusion 1 (1)
12/20
9
24.4 28.00 27.87 73 7.31 9.99 0.01 4.61 2.993
166.45
24.3 24.70 24.59 74 8.04 9.2 0.0092 4.24 2.753
146.86
24.2 21.40 21.31 66 8.36 7.89 0.0079 3.64 2.363
127.27
24 19.30 19.22 60 8.9 6.74 0.0067 3.09 2.006
114.79
24 17.80 17.73 54 8.9 6.07 0.0061 2.81 1.824
105.89
24 16.20 16.14 42 7.65 5.49 0.0055 2.53 1.643
96.39
24 14.40 14.34 45 8.9 5.06 0.005 2.3 1.493
85.64
24 13.00 12.95 35 7.92 4.42 0.0044 2.03 1.31
8
77.34
24 11.60 11.56 32 8.33 3.84 0.0038 1.75 1.136
69.04
24 10.20 10.16 33 9.18 3.59 0.0036 1.66 1.078
60.68
24 8.90 8.87 32 10.26 3.12 0.0031 1.43 0.928
52.97
24 7.50 7.47 31 11.12 2.79 0.0028 1.29 0.837
44.61
24 6.40 6.38 31 13.58 2.28 0.0023 1.06 0.688
38.1
24 5.40 5.38 26 13.82 1.88 0.0019 0.88 0.571
32.13
24 3.60 3.59 23 16.7 1.38 0.0014 0.65 0.422
21.44
24 2.55 2.54 16 17.13 0.93 0.0009 0.41 0.266
15.17
24 1.50 1.49 14 19.54 0.72 0.0007 0.32 0.208
8.9
24 1.00 1.00 12 26.37 0.46 0.0005 0.23 0.149
5.97
24 0.55 0.55 13 49.77 0.26 0.0003 0.14 0.091
3.28
24 0.40 0.40 10 94.22 0.11 0.0001 0.05 0.032
2.39
24 0.00 0.00 0 0 0 0 0 0 0
TABLA 1
Calculo de la caída de presión por ecuaciones de Carman% Lea y (r)un en ascenso
=Pca&man(>g#/m2)
=P ?e'a(>g#/m2
)
=P4&gun(>g#/m
2) 0 0
-
8/16/2019 Discusion 1 (1)
13/20
1.9" 9.9 7.44
.39 12.66 9.51
30.0"7 40.72 30.77
2."9" 58.32 44.23
01.3" 75.93 57.77
03.11" 70.98 53.95
1".01" 94.09 71.82
79.73 88.59 67.55
".911 116.65 89.42
.92 124.35 95.46
27.701 141.96 109.33
9."" 121.6 93.3
."9 167.27 129.42
9.91 177.73 137.77
7.3"1 190.38 147.92
TABLA 11Calculo de la caída de presión por ecuaciones de Carman% Lea y (r)un en descenso
=Pca&man(>g#/m2)
=P?e'a
(>g#/m2)
=P4&gun
(>g#/m2)
1.70 201.95 157.2
3.2 170.02 131.61
39. 154.62 119.35
2.29 139.21 107.15
3.9 126.55 97.18
.3 111.7 85.54
10.00 96.29 73.53
12.2 91.34 69.69
7.12 78.68 59.89
03.11 70.98 53.95
2."9 58.32 44.23
"3.1 48.42 36.65
32.9 35.77 27.01
2.3 22.56 16.99
.1 17.61 13.25
.39 12.66 9.51
0.93 7.7 5.79
2."1 2.75 2.06
0 0
TABLA 12
Calculo de la desiación de la caída de presión por ecuaciones de Carman% Lea y (r)un en ascenso
-
8/16/2019 Discusion 1 (1)
14/20
%es!"ac"#n
Carman
%es!"ac"#n
Le!a
%es!"ac"#n
$rgn
40.29 33.69 50.17
54.59 49.52 62.085.6 4.89 20.74
12.7 25.2 5.05
23.05 36.71 4.02
2.75 8.05 17.87
1.28 12.53 14.1
14.41 4.91 27.49
7.2 19.1 8.7
4.11 15.67 11.2
12.6 25.11 3.6511.89 2.11 24.89
13.55 26.17 2.38
13.01 25.57 2.66
12.96 25.51 2.49
TABLA 13
C"lculo de la desiación de la caída de presión por ecuaciones de Carman% Lea y (r)un en reersa
ADes'iaci+n
Ca&man
ADes'iaci+n?e'a
ADes'iaci+n
4&gun
42.81 58.68 23.52
33.3 48.11 14.65
31.41 46.02 12.71
29.98 44.42 11.16
33 47.77 13.48
29.98 44.43 10.6
25.52 39.47 6.535.48 50.53 14.85
33.7 48.54 13.06
43.2 59.11 20.94
37.77 53.07 16.09
35.64 50.7 14.07
50.14 66.84 25.98
33.82 48.71 12
78.09 97.87 48.88
90.79 112.06 59.3111.28 134.76 76.52
-
8/16/2019 Discusion 1 (1)
15/20
3.77 15.06 13.81
0 0 0
TABLA 14
C"lculo del punto mínimo de fluidi*ación
Con'e&sion%m#
(l5/@.#*2)
%m# (>g/s.m
2)
%m# (cm3/se
g)
Dp (m) 0.00062 Dp (plg) 0.025
3135.39 4.252 9.247
B# (>g/m3)
2278.84 ƿf (lb/ft3)160.18
1Bp
(>g/m3)997.8
ƿp(lb/ft3)
62.291
(>g/ms)0.00095
8μ (cp) 0.958
!R"#ICAS
!$%&'(a 1 Caida de presión ersus Caudal +,P s -. en escala lo)arítmica para columna sin lecho
-
8/16/2019 Discusion 1 (1)
16/20
1 10 100 10000.1
1
10
f(x) = 0.01 x^1.21! = 0.98
D"t#$ %#&' (D"t#$)
Caudal cm3/s
=P cm CCl"
!$%&'(a 2
Caida de presión ersus Caudal +,P s -. de los datos experimentales en ascenso y descenso
& '& 2& & 4& & *& +&&.&
.&
'&.&
'.&
2&.&
2.&
&.&
.&
4&.&
D"t#$ 't## D"t#$ 't##
Ca,al cm/s
P cm CCl4
!$%&'(a 3
Caida de presión ersus Caudal +,P s -. en escala lo)arítmica de los datos experimentales en
ascenso y descenso
-
8/16/2019 Discusion 1 (1)
17/20
' '& '&&'.&
'&.&
'&&.&
D"t#$ 't## D"t#$ 't##
Ca,al cm/s
P cm CCl4
%&a!ca "
lt+" ,'l l'c# $ l" 'l#c,", ,' l#$ ,"t#$ 'xp''t"l'$ ,' "$c'$#
,'$c'$#
0 5 10 15 20 25 3020
25
30
35
40
45
50
"$c'$# ,'$c'$#
$(g/2$)
(c)
%&a!ca
-
8/16/2019 Discusion 1 (1)
18/20
0 1 2 3 4 5 60
50
100
150
200
250
300
% 'xp''t"l
""
l'"
Eg+
$ (g/$.2)
% 'xp''t"l (gf/2)
#p""c ,' % c"lc+l","$ c# l" 'xp''t"l ("$c'$#)
%&a!ca 0
#p""c ,' % c"lc+l","$ c# l" 'xp''t"l ( ,'$c'$#)
0 1 2 3 4 50
50
100
150
200
250
300
'xp''t"l
""
'"
Eg+
$ (g/$.2
% 'xp''t"l (gf/2)
Discusi+n de &esul*ados
-
8/16/2019 Discusion 1 (1)
19/20
-
8/16/2019 Discusion 1 (1)
20/20
" >+' '$t'