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8/10/2019 Folien_SFPS_5
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Fig. 5.1
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.1
5. Silo and bunker pressure calculations5.1 shaft pressures
5.2 hopper pressures
5.3 wall thickness of concrete and metal sheet silos
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Fig. 5.2
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.2
Vertikal and Horizontal Pressures at Mass Flow Silo
height level of flattened
free bulk surface
intersection between
shaft and hopper
height level of
discharge opening
filling
discharging
siloheightH
silo pressures pv and ph
pv
pv
ph
ph
pv
ph
radial stress field r
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Fig. 5.3
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.3
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Fig. 5.5
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.5
positi
ono
factive
sh
ear
pla
ne
Active and Passive Rankine's Stress State Limits
Yield locus: = tan i+c= tan i( + Z)
or R= sin i(M+ Z)
ph,a
activepassive
shea
rstress
tensile
strength Z
cohesion c
i
2,a
a=
i
4 2+
iR,a
2a
pv
1,a
yieldlocus
ph,p
1,p
p = i
4-
2
M,p =1,p+ 2,p
2
positionofpassiveshearplane
R,p=1,p 2,p
2
-
active passive
principal stresses
lateral or
horizontal
stress ratio
2,a= 1+ c1 - sin i
1 + sin i
2 cos i
1 + sin i
1,p= 2,p+ c1 + sin i
1 - sin i
2 cos i
1 - sini
lower limit for c= 0 upper limit for c= 0
ph,p
pv= = = tan2
1 + sin i
1 - sin i(
4+
i
2
p
ph,a
pv= = = tan2
1 - sin i
1 + sin i(
4-
i
2a
active
i4 2
+
pv
ph,a pv
ph,p
passive
i4 2
-
pv
ph,a
pvph,p
normal stress
given: pv= 1= b.g y
c, i
searched: 2 stress states which meet the yield condition
y
x
2,p
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Fig. 5.6
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.6
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Fig. 5.7
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.7
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Fig. 5.8
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.8
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Fig. 5.9
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.9
storage time tL = 22 h
mFill = 11,5 t
b = 0,8 t/m3
e = 33
w = 23 steel sheet (CF)
w
= 18 steel sheet (MF)
mass flow, switch load pn = (c4- c1) pn cos ,
TGL 32274/09
mass flow, switch load pn = b g (H or D),DIN 1055 part 6
0 5 10 15 20 25 30 35 40
wall normal pressures ph, pn in kPa
0
1
2
3
4
5
heigh
tH,
H'inm
mass flow (MF)
core flowflow
bondary
silo
G 807
pn
Wall Normal Pressures ph, pnof Wheat
measured, filling
measured, discharging
calculated, filling
calculated, discharging,
load factors c1= 1,4, c4= 3,0
calculated, DIN 1055 part 6
c3= 1.8(CF)
23
30
phD = 2,4 m
measurements according to Scholz
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Fig. 5.10
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.10
Maximum Normal Pressures (Discharging) versus
Effective Angle of Internal Friction
1
2
3
4
5
6
7
8
9
10
11
w= 10
boundariesrough wall
w=10
2030 4050
0 10 20 30 40 50 60
p*h shaft
p*n hopper
20
30
405060
p*h
,max,
p*n,max
12
e in deg
Maximum Vertical Pressures (Filling) versus Effektive
Angle of Internal Friction
p*v,max
0 10 20 30 40 50 60
1
2
3
4
5
6
7
8
9
10
11
w= 10
20
30
40
50
boundary
rough wall
= 10 mass flow
=0,725
= 2,414
AUHD
shafthopper
w
=10
2030 40
50
12
13
14
e in deg
Maximum Vertical Pressures (Filling) versus
Wall Friction Angle
0 10 20 30 40 50 60
1
2
3
4
5
6
7
8
9
10
11
e=30 4050
12
13
isostatic pressure
boundaryrough wall
p*v,max
14
shaft
hopper
60
w in deg
Maximum Normal Pressures (Discharging)
versus Wall Friction Angle
1
2
3
4
5
6
7
8
9
10
11
30
4050
0 10 20 30 40 50 60
boundariesrough wall
p*h,max
,
p*n,max
12
13
14
60e
=30
w in deg
605040
p*h shaft
p*n hopper
Maximum Wall Friction Loads (Discharging)
versus Effective Angle of Internal Friction
0 10 20 30 40 50 60
w=10
20
30
40
-50
p*h
shaft
p*n hopper
20
10
30
20
40
50
-10
e=30
1
2
1,5
2,5
0 0
0,5
0,6
0,7
0,4
0,3
0,2
0,1
p*
w,max
boundaries
rough wall
0,5
60
4050
p*
w,max
e in deg
p*
w,max
p*
w,max
Maximum Wall Friction Loads (Discharging) versus
Wall Friction Angle
e=3040
50
5040
0
0,5
1
1,5
2
2,5
0
0,5
0,6
0,7
0,4
0,3
0,2
0,1
boundariesrough wall
0 10 20 30 40 50 60
60
60
e=
30
w in deg
p*w shaftp*w hopper
p* = p U
bg A
.. .
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Fig. 5.11
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.11
1
2
3
4
5
6
78
p*v,max
9
10
11
w= 10
20
30
40
50
boundary
rough wall
= 30 core flow
=0,725
= 2,414
A
UH
D
shaft
hopper
w=10
2030 40
50
0 10 20 30 40 50 60e in deg
Maximum Vertical Pressures (Filling) versus Effektive
Angle of Internal Friction
1
2
3
4
5
6
7
8
9
10
11
e=30 4050
0 10 20 30 40 50 60
12
13
shaft
hopper
isistatic pressure
boundary
rough wall
p*v,max
60
w in deg
Maximum Vertical Pressures (Filling)
versus Wall Friction Angle
1
2
3
4
5
6
7
8
9
10
11w= 10
boundaries
rough wall
w
=10
2030
4050
0 10 20 30 40 50 60
p*h shaft
p*n hopper
20304050
60
p*h,max,
p*n,max
60
e in deg
Maximum Normal Pressures (Discharging) versusEffective Angle of Internal Friction
1
2
3
4
5
6
7
8
9
10
11
e
=30 40 50
0 10 20 30 40 50 60
e
=30
4050
60
60
boundariesrough wall
p*h,max,
p*n,max
w in deg
p*h shaft
p*n hopper
Maximum Normal Pressures (Discharging)versus Wall Friction Angle
e=30 40 50
50
40e=
30
0 0
Ip*
w,max
0,5
0,6
0,7
0,8
0,9
1,0
0,4
0,3
0,2
0,10,5
1
1,5
2
2,5
3
p*
w,max boundaries
rough wall
0 10 20 30 40 50 60
60
60
w in deg
p*h shaft
p*n hopper
Maximum Wall Friction Loads (Discharging)
versus Wall Friction Angle
3
w=10 20
30
40
50
20
10
30
2030
40
50
10
e=60
1
2
1,5
2,5
0
0 10 20 30 40 50 600
0,5
0,6
0,7
0,8
0,9
1,0
0,4
0,3
0,2
0,1
Ip*
w,max
boundaries
rough wall
0,5
e in deg
p*
w,max
p*h shaft
p*n hopper
Maximum Wall Friction Loads (Discharging)
versus Effective Angle of Internal Friction
p* = p U
bg A
.
. .
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Fig. 5.12
Prof. Dr. J. Tomas, chair of Mechanical Process Engineering
Fig_SFPS_5Storage and Flow of Particulate Solids Silo pressure calculations Prof. Dr. J. Tomas 05.05.2014 Figure 5.12
Necessary Steel Reinforcement of Concrete ASt
Di,1
pn
ASt
H
Di
Di,2
pn
Di= Di,1+ Di,2 2
(1)
(2)
(3)
(4)
load factors according to TGL 32 274/09
( ) coscc1c14or3j +=
cj= c1 or c3or c4
with c1= 1,2 ... 1,6 c3= 1,7 ... 2,1
c4= 2,1 ... 4,0
hopper
shaft
dischargingcore flow
mass flow
H2cos/DHp0FStAin ==
cos2
cDpA
StF,
jsin
St
=
= iwF
StF,w
js
2
ib
StD
H
tan4exp1tan8
cDg
A
and for the cylindrical shaft:
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