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Mixer Shaft Design and Stress Analysis

The document discusses the process for designing mixing shafts. It outlines how to calculate stresses on the shaft from torque (torsional stress) and fluid forces (bending stress). Equations are provided to calculate pure torsional stress, pure bending stress, and combined stresses. Additional considerations discussed include critical speed, deflection, and support structure design loads.

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Steve Wan
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50% found this document useful (2 votes)
954 views7 pages

Mixer Shaft Design and Stress Analysis

The document discusses the process for designing mixing shafts. It outlines how to calculate stresses on the shaft from torque (torsional stress) and fluid forces (bending stress). Equations are provided to calculate pure torsional stress, pure bending stress, and combined stresses. Additional considerations discussed include critical speed, deflection, and support structure design loads.

Uploaded by

Steve Wan
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as PDF, TXT or read online on Scribd
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HAYWARD GORDON LTD.

SECTION:
PAGE:
DATE:
REV.:

Shaft Design

TG8
8.01
7/00
0

The process requirements determine the overall mixer size and configuration, ie. HP,
RPM, number and style of impeller(s) etc.; the next step is to design an appropriately
sized shaft system. The absorbed Horsepower of the impeller(s) creates torsional and
bending stresses on the mixing shaft. The torsional stress is due to the transmitted
torque (BHP at the speed of rotation) and the bending stress is due to the fluid hydraulic
forces acting on the impeller(s).
Pure Torsional Stress
If a mixer shaft and impeller assembly had no fluid hydraulic forces acting at the
impeller we would only be concerned with torsional stress which is the torque
transmitted by the shaft divided by its Polar Section Modulus. The formula for Pure
Torsional Stress is:

TQ
=
=
Z
Where:

HP ( 63025 )
RPM

d3
16

[ ]
lbs
in 2

HP is motor HP
RPM is impeller speed
d is shaft diameter [in.]

Pure Bending Stress


If we were interested in determining the stress in the shaft due only to the unbalanced
hydraulic forces acting on the mixing impellers (ignoring torsional stress) it would be a
matter of determining the magnitude of these hydraulic forces and where along the
shaft they were acting (impeller location).
The hydraulic forces, created by the action between the fluid and the impeller, produce
side loads on the shaft causing this tensile or bending stress. The fluid hydraulic force
acting at an impeller is random in both direction and magnitude, we therefore must
calculate the maximum possible hydraulic load to determine the shaft stress. The
equation for hydraulic loading at an impeller is:

FH =
Where:

24 , 000 ( HP )( CF )
RPM ( D )

[ lbs.]

HP is Impeller Power
CF is a Condition Factor based on impeller style and application (Typ. 1 to 3)
RPM is impeller speed
D is impeller diameter [in.]

HAYWARD GORDON LTD.

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Shaft Design

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After the hydraulic force is found at the impeller(s), the total Bending Moment can be
calculated by using the following:

M = {FH1( L1)} + {FH 2( L 2)}+ ... {FHn( Ln )} [ in . lbs.]


Where:

FH1, FH2 ... FHn are Fluid Hydraulic Forces at each Impeller [lbs.]
L1, L2 ... Ln are the distances from the lower gearbox bearing to the impeller [in.]

Finally the Pure Bending Stress can be calculated by dividing the total bending moment
(M) by the shaft rectangular section modulus.

[ ]

M M
=
= d3
Z
32
Where:

lbs
in 2

M is the Bending Moment calculated above [in.lbs.]


d is shaft diameter [in.]

Combined Stresses
When a mixer is operating the shaft is experiencing both bending and torsional
stresses, therefore the final step in shaft design is to calculate the combined stresses in
the shaft. The combined torsional stress can be found by using the following equation:

=
Max

( )

2
2

+ ( )

[ ]
lbs
in 2

And the combined bending stress can be found by using:

=(
Max

)+ ( )

2
2

2
(
)
+

[ ]
lbs
in 2

HAYWARD GORDON LTD.


Shaft Design

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Critical Speed
If a shaft and impeller assembly were struck with a hammer, the assembly would begin
to vibrate. The vibratory mode with the lowest frequency is defined as the first natural
frequency of the system, the next highest is the second natural frequency and so on.
Critical Speed is defined as the mixer rotational speed (RPM) which coincides with its
first natural frequency (Hz).
Rotating a mixer assembly at a rate equal to its natural frequency is like hitting it with a
hammer. However, unlike a hammer which provides a momentary influx of energy, the
mixer motor continues to pump energy into the vibrating assembly causing it to oscillate
at higher and higher amplitudes until failure occurs. We therefore must calculate the
first natural frequency of each mixer assembly to ensure we are not operating near this
critical point.
The following equation can be used to determine the first natural frequency (NC) of a
mixer with a uniform solid shaft.

d2
E
NC = 146.4 2
4.13We
L L + a

WB +

L
L
3

Where:
And:

L2
LN
We = W1 + W 2 + ...+ WN
L
L

d is the shaft diameter (in)


L shaft length from lower gearbox bearing (in)
L2 ,... LN is the distance from the lower gearbox bearing to the impeller (in)
a is the gearbox bearing span (in)
W 1, W 2, ... W N are impeller weights (lbs)
W B is the shaft weight (lbs/in3)
E is the Modulus of Elasticity (lbs/in2), ie. E=30,000,000 psi for steel.

Note: All calculations for critical speed assume that the mixer is rigidly
supported.

TG8
8.03
7/00
0

HAYWARD GORDON LTD.


Shaft Design

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Deflection
When a mixer is supplied with a shaft seal for closed tank applications or when tank
internals (heating coils, draft tube, limit ring, etc.) are in relatively close proximity of the
mixer wet end, it is necessary to check the shaft deflection due to hydraulic forces at
the impeller(s).
The following equations can be used to check shaft deflection in the seal area or at the
bottom of a uniform solid shaft:

Deflection at seal:

FHX
y =
( 2La + 3LX X 2 )
6EI
Deflection at end of shaft (X=L):

FHL2
( a + L)
y =
3EI

Where,

d4
I=
64

And: L shaft length from lower gearbox bearing (in)


a is the gearbox bearing span (in)
FH is the hydraulic force acting on the impeller (lbs)
E is the Modulus of Elasticity (lbs/in2), ie. E=30,000,000 psi for steel
d is the shaft diameter (in)
y is shaft deflection at point of interest (TIR is two times y)

TG8
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HAYWARD GORDON LTD.


Shaft Design

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Mixer Support Design Loads


The mixer support structure is to be designed so that dynamic angular deflection of
drive is limited to 0.25 degrees in any direction.

Where:

D is Impeller Dia. in [In.]


N is Impeller Speed [RPM]
NI is the Number of Impellers
HP is Nameplate Horse Power
LX is distance from impeller to mounting surface [In.]
FHX is the fluid hydraulic force at each impeller (see Pg. 8.01) [lbs.]

TG8
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HAYWARD GORDON LTD.

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Shaft Design

TG8
8.06
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Open Tank Mixer Support Structures


For purposes of use during preliminary investigations, information on practical support
construction for mixers mounted above open tanks is outlined here. Suggested beam
sizes are rather conservative, and apply for use with the highest output torque capacity
of each drive and at the longest agitator shaft overhangs practical for each size. For
maximum economy in a specific installation, it is recommended that the Processor or
Engineering Contractor apply his own beam support design standards to the specific
mixer that will be utilized.
Some degree of cross bracing between main beams always represents a sound
engineering approach. The user is encouraged to apply more sophisticated designs of
cross bracing particularly with the larger tanks where cost of supports can become
substantial. It is normal to apply floor plate or grating between the main support beams
which provides walkway access while providing additional rigidity in the support
structure. This information is intended as a guideline and does not relieve the user of
completely analysing the entire mounting system for each mixing application.

BB Dimension (inches)
Drive Size
HRFs

ST-10

ST-11

ST-12

MB-53

MB-54

MB-55

MB-56

MB-57

MB-58

MB-59

LH-9

LH-10

11

10

12

14

12

13

15

17

21

23

23

19

19

HAYWARD GORDON LTD.

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Shaft Design

Tank Diameter (inches)


Drive Size

HRFs

ST-10

ST-11
ST-12
MB-53

MB-54

MB-55
MB-56

MB-57

MB-58
MB-59

LH-9

LH-10

Beam Function
120

180

240

300

360

Main Support

6C10.5

8WF24

10WF33

12WF45

12WF79

Drive Support

4C7.25

5C9.0

7C9.8

8C11.5

8C11.5

Cross Bracing

4C7.25

5C9.0

7C9.8

8C11.5

8C11.5

Main Support

6WF20

10WF25

10WF60

12WF72

12WF120

Drive Support

4C7.25

7C9.8

7C9.8

8C11.5

8C11.5

Cross Bracing

4C7.25

7C9.8

7C9.8

8C11.5

8C11.5

Main Support

6WF25

10WF29

10WF60

12WF79

12WF133

Drive Support

4C7.25

7C9.8

7C9.8

8C11.5

8C11.5

Cross Bracing

4C7.25

7C9.8

7C9.8

8C11.5

8C11.5

Main Support

8WF20

10WF33

12WF53

12WF92

14WF119

Drive Support

5WF16

8C11.5

8C11.5

8C11.5

9C13.4

Cross Bracing

5C6.7

8C11.5

8C11.5

8C11.5

9C13.4

Main Support

8WF31

10WF45

12WF58

14WF87

14WF142

Drive Support

5WF16

8C11.5

8C11.5

9C13.4

9C13.4

Cross Bracing

5C9.0

8C11.5

8C11.5

9C13.4

9C13.4

Main Support

8WF35

10WF49

12WF72

14WF103

14WF167

Drive Support

6WF15.5

6WF15.5

8WF31

10WF33

10WF33

Cross Bracing

6C13

6C13

8C11.5

10C15.3

10C15.3

Main Support

8WF40

10WF60

14WF68

14WF127

14WF202

Drive Support

6WF15.5

6WF15.5

10WF33

10WF33

10WF33

Cross Bracing

6C13

6C13

10C15.3

10C15.3

10C15.3

Main Support

10WF45

12WF58

14WF95

14WF167

14WF264

Drive Support

8WF31

8WF31

10WF33

10WF33

10WF33

Cross Bracing

8C11.5

8C18.75

10C15.3

10C15.3

10C15.3

Main Support

10WF45

12WF58

14WF95

14WF167

14WF264

Drive Support

8WF31

8WF31

10WF33

10WF33

10WF33

Cross Bracing

8C11.5

8C18.75

10C15.3

10C15.3

10C15.3

TG8
8.07
7/00
0

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