The
CAESAR IIQuick Reference Guideis intended to aid users in quickly identifying
needed information and to resolve common questions and problems. This
Reference Guide is distributed with each copy of the software and users are urged
to copy the Reference Guide as necessary.
Comments and suggestions concerning
CAESAR II, the User Guide, or the Quick
Reference Guide are always welcome. Users with problems, questions, or
suggestions can contact the
COADEDevelopment/Support staff at:
[email protected]
.
CAESAR II Quick Reference Guide Table of Contents
CAESAR II Quick Reference Guide Version 5.10...1
CAESAR II Software ...2
CAESAR II Pipe Stress Seminars ...2
System Requirements ...3
Troubleshooting...3
CAESAR II Interfaces ...3
Piping Codes...4
Restraints ...5
Setup File Directives List ...6
List of Materials...11
CAESAR II Intersection Types ...12
Code Stresses ...13
Node Locations on Bends...24
CAESAR II Quality Assurance Manual ...26
Mechanical Engineering News ...26
Additional COADE Software Programs...26
CAESAR II Software
CAESAR II
is an advanced PC based tool for the engineer who designs or analyzes
piping systems.
CAESAR IIuses input spreadsheets, on-line help, graphics, and
extensive error detection procedures to facilitate timely operation and solution.
CAESAR II
is capable of analyzing large piping models, structural steel models, or
combined models, both statically and dynamically. ASME, B31, WRC, and
rotating equipment reports combine to provide the analyst with a complete
description of the piping system’s behavior under the applied loading conditions.
Additional technical capabilities such as out-of-core solvers, force spectrum
analysis (for water hammer and relief valve solutions), time history, and large
rotation rod hangers provide the pipe stress engineer with the most advanced
computer based piping program available today.
CAESAR II
is continuously enhanced to incorporate new technical abilities, to
provide additional functionality, and to modify existing computation procedures as
the piping codes are updated. A complete list of the most recent changes to
CAESAR II
can be found in the Chapter 1 of the User Guide. Users wanting
software sales are urged to contact the
COADESales staff at:
Phone:281-890-4566 E-mail: [email protected]
FAX: 281-890-3301 Web: http://www.coade.com/product_overview.asp?varflag=CAESARII
CAESAR II Pipe Stress Seminars
COADE
offers seminars periodically to augment the Engineers knowledge of
CAESAR IIand Pipe Stress Analysis. The general seminar is held in our Houston
office and covers five days of Statics. Twice yearly we also cover five days of
Statics and three days of Dynamics. These seminars emphasize the piping codes,
static analysis, dynamic analysis, and problem solving.
Custom seminars held at client locations are also available. For additional seminar
details, please contact the
COADESupport staff at:
seminars @coade.com
.
System Requirements
CAESAR II
requires Windows 2000, or Windows XP Professional, with a
minimum graphic card capability of 1024x768 resolution. However, for more
efficient usage of the software, higher graphics resolutions are necessary. Usually
any hardware capable of running these operating systems will be sufficient to run
CAESAR II.
For effective use of
CAESAR II,
COADErecommends as a minimum
configuration:
2+ Ghz processor 1+ Gbytes of RAM
1280x1024 graphics resolution or better 256+ Mbytes of video RAM
Windows 2000 or Windows XP Professional
Please note that Windows XP Home Edition, Windows Vista Professional and Windows Vista Home Edition are not supported.
Troubleshooting
For troubleshooting and problem solving issues, refer to the
CAESAR IIFrequently
Asked Questions (FAQ) located on the
COADEWebsite. To access the FAQ:
(http://www.coade.com/product_faq.asp?varflag=CAESARII&varflagmaster=)
.
CAESAR II Interfaces
There are several external interfaces which allow data transfer between
CAESAR IIand other software packages. Users can access these interfaces via the Tools menu
on the
CAESAR II Main Menu.
CADWorx requires AUTOCAD
AUTOCAD DXF Output
COMPUTER VISION mainframe
INTERGRAPH mainframe
CADPIPE requires AUTOCAD
ISOMET mainframe PDMS mainframe
PCF Alias format
Users interested in these interfaces should contact
COADEfor further information.
We anticipate other interfaces in the future keep users updated via the newsletter or
revised documentation.
Piping Codes
The table below displays the Piping Code, publication and/or revision date.
PIPING CODE PUBLICATION REVISIONANSI B31.1 (2004) December 15, 2006
ANSI B31.3 (2006) May 31, 2007
ANSI B31.4 (2006) October 20, 2006
ANSI B31.4 Chapter IX (2006) October 20, 2006
ANSI B31.5 (2001) May 30, 2005
ANSI B31.8 (2003) February 6, 2004
ANSI B31.8 Chapter VIII (2003) February 6, 2004
ANSI B31.11 (2002) May 30, 2003
ASME SECT III CLASS 2 (2004) July 1, 2005
ASME SECT III CLASS 3 (2004) July 1, 2005
U.S. NAVY 505 (1984) N/A
CANADIAN Z662 (6/2003) N/A
CANADIAN Z662 Ch 11 (6/2003) N/A
BS 806 1993, ISSUE 1, SEPTEMBER 1993 N/A
SWEDISH METHOD 1 2ND EDITION STOCKHOLM 1979 N/A SWEDISH METHOD 2 2ND EDITION STOCKHOLM 1979 N/A
ANSI B31.1 (1967) N/A STOOMWEZEN (1989) N/A RCC-M C (1988) N/A RCC-M D (1988) N/A CODETI (2001) June 2004 NORWEGIAN (1999) N/A FDBR (1995) N/A BS7159 (1989) N/A UKOOA (1994) N/A IGE/TD/12 (2003) N/A DnV (1996) N/A EN-13480 (12/2006) Issue 9 GPTC/192 (1998) N/A
Restraints
No. Restraint Type Abbreviation
1 Anchor A
2 Translational Double Acting X,Y, or Z
3 Rotational Double Acting RX, RY, or RZ
4 Guide, Double Acting GUI
5 Double Acting Limit Stop LIM
6 Translational Double Acting Snubber XSNB, YSNB, ZSNB
7 Translational Directional +X, -X, +Y, -Y, +Z, -Z
8 Rotational Directional +RX, -RX, +RY, etc.
9 Directional Limit Stop +LIM, -LIM
10 Large Rotation Rod XROD, YROD, ZROD
11 Translational Double Acting Bilinear X2, Y2, Z2 12 Rotational Double Acting Bilinear RX2, RY2, RZ2 13 Translational Directional Bilinear -X2, +Y2, -Y2, etc. 14 Rotational Double Acting Bilinear -RX2, +RY2, - RY2, etc.
15 Bottom Out Spring XSPR, YSPR, ZSPR
Setup File Directives List
The following list represents the possible directives which can be controlled by the
user via the
CAESAR IIconfiguration file CAESAR.CFG. These directives can be
changed by the user through the use of the CONFIGURE-SETUP program,
accessed via Main Menu option #9. Directives are listed in groups corresponding
to the configuration program's menu options.
Geometry Directives
GEOMETRY DIRECTIVESCONNECT GEOMETRY THRU CNODES = YES 34
MIN ALLOWED BEND ANGLE = .5000000E+01 36
MAX ALLOWED BEND ANGLE = .9500000E+02 37
BEND LENGTH ATTACHMENT PERCENT = .1000000E+01 38
MIN ANGLE TO ADJACENT BEND PT = .5000000E+01 39
LOOP CLOSURE TOLERANCE = .1000000E+01 42
THERMAL BOWING HORIZONTAL TOLERANCE = .1000000E-03 92
AUTO NODE NUMBER INCREMENT= 1000000E+02 109
Z AXIS UP NO 129
Computation Control
COMPUTATION CONTROLUSE PRESSURE STIFFENING = DEFAULT 65
ALPHA TOLERANCE = .5000000E-01 33
HANGER DEFAULT RESTRAINT STIFFNESS = .1000000E+13 49
DECOMPOSITION SINGULARITY TOLERANCE = .1000000E+11 50
BEND AXIAL SHAPE = YES 51
FRICTION STIFFNESS = .1000000E+07 45
FRICTION NORMAL FORCE VARIATION = .1500000E+00 47
FRICTION ANGLE VARIATION = .1500000E+02 48
FRICTION SLIDE MULTIPLIER = .1000000E+01 46
ROD TOLERANCE = .1000000E+01 59
COMPUTATION CONTROL
INCORE NUMERICAL CHECK = NO 60
DEFAULT TRANSLATIONAL RESTRAINT STIFFNESS .1000000E+13 98
DEFAULT ROTATIONAL RESTRAINT STIFFNESS = .1000000E+13 99
IGNORE SPRING HANGER STIFFNESS = NO 100
MISSING MASS ZPA = EXTRACTED 101
MINIMUM WALL MILL TOLERANCE = .1200000E+02 107
WRC-107 VERSION = MAR 79 1B1/2B1 119
WRC-107 INTERPOLATION = LAST VALUE 120
INCLUDE_INSULATION_IN_HYDROTEST= NO 147
AMBIENT TEMPERATURE = 70.00 135
BORDER PRESSURE = NONE 136
COEFFICIENT OF FRICTION = 0. 140
INCLUDE SPRING STIFFNESS IN FREE THERMAL
CASES = NO 141
SIFS and Stresses
SIFS AND STRESSESREDUCED INTERSECTION = B31.1 POST1980 32
USE WRC329 = NO 62
NO REDUCED SIF FOR RFT AND WLT NO 53
B31.1 REDUCED Z FIX = YES 54
CLASS 1 BRANCH FLEXIBILITY NO 55
ALL STRESS CASES CORRODED = NO 35
ADD TORSION IN SL STRESS = DEFAULT 66
ADD F/A IN STRESS = DEFAULT 67
OCCASIONAL LOAD FACTOR = .000000E+00 41
DEFAULT CODE = B31.3 43
B31.3 SUSTAINED CASE SIF FACTOR = 100000E+01 40
ALLOW USERS BEND SIF = NO 52
USE SCHNEIDER = NO 63
YIELD CRITERION STRESS = MAX 3D SHEAR 108
SIFS AND STRESSES
BASE HOOP STRESS ON = NO 57
EN-13480 use in-plane/out-plane SIF NO 133
LIBERAL ALLOWANCE = YES 137
STREE STIFFENING DUE TO PRESS = NO 138
B31.3 WELDING/CONTOUR TEE MEET B16.9 = NO 139
IMPLEMENT _B31.3_APPENDIX_P NO 144
IMPLEMENT_B31.3_CODECASE NO 145
B31.3 Sec 319.2.3(c), Saxial NO 146
PRESSURE VARIATION IN EXPANSION CASE DEFAULT =
DEFAULT 143
FRP Properties
FRP PROPERTIESUSE FRP SIF = YES 110
USE FRP FLEXIBILITY = YES 11
BS 7159 PRESSURE STIFFENING = DESIGN STRAIN 121
FRP PROPERTY DATA FILE = CAESAR.FRP 122
AXIAL MODULUS OF ELASTICITY 3200000E+07 113
RATIO SHEAR MOD : AXIAL MOD = 2500000E+00 114
AXIAL STRAIN : HOOP STRESS 1527272E+00 115
FRP LAMINATE TYPE = THREE 116
FRP ALPHA = .1200000E+02 117
FRP DENSITY = .6000000E-01 118
EXCLUDE F2 FROM BENDING STRESS (UKOOA) NO 134
Plot Colors
PLOT COLORS PIPES LIGHTCYAN 1 HIGHLIGHTS GREEN 2 LABELS GREEN 3 BACKGROUND BLACK 5 AXES LIGHTRED 15PLOT COLORS
HANGER/NOZZLES BROWN 16
RIGID/BENDS LIGHTGREEN 17
NODES YELLOW YELLOW 18
STRUCTURE LIGHTRED 31
DISPLACED SHAPE BROWN 30
STRESS > LEVEL 5 RED 24
STRESS > LEVEL 4 YELLOW 25
STRESS > LEVEL 3 GREEN 26
STRESS > LEVEL 2 LIGHTCYAN 27
STRESS > LEVEL 1 BLUE 28
STRESS < LEVEL 1 DARKBLUE 29
STRESS LEVEL 5 .3000000E+05 19
STRESS LEVEL 4 .2500000E+05 20
STRESS LEVEL 3 .2000000E+05 21
STRESS LEVEL 2 .1500000E+05 22
STRESS LEVEL 1 .1000000E+05 23
Database Definitions
DATABASE DEFINITIONSSTRCT DBASE = AISC89.BIN 70
VALVE & FLANGE = CADWORX.VHD 90
EXPANSION JT DATABASE = PATHWAY.JHD 91
PIPING SIZE SPECIFICATION = ANSI 88
DEFAULT SPRING HANGER TABLE = 1 112
SYSTEM DIRECTORY NAME = SYSTEM 123
UNITS FILE NAME = .ENGLISH.FIL 124
LOAD CASE TEMPLATE = .LOAD.TPL 142
ENABLE ODBC OUTPUT NO 128
APPEND RE-RUNS TO EXISTING DATA NO 126
Miscellaneous Computations
MISCELLANEOUS COMPUTATIONSOUTPUT REPORTS BY LOAD CASE YES 87
DISPLACEMENT NODAL SORTING YES 89
DYNAMIC INPUT EXAMPLE TEXT MAX 94
TIME HIST ANIMATE YES 104
OUTPUT TABLE OF CONTENTS ON 105
INPUT FUNCTION KEYS DISPLAYED YES 106
MEMORY ALLOCATED 12 NA
USER ID " " NA
List of Materials
The CAESAR II Material Table contains 17 different isotropic materials.
Properties and allowed temperature ranges for each isotropic material are listed
below.
Material
No. Material Name Elastic Modulus Poisson's Ratio Pipe Density (lb./cu.in) Temperature Range (deg. F)
1 Low Carbon Steel 29.5 E6 0.292 0.28993 -325 1400
2 High Carbon Steel 29.3 E6 0.289 0.28009 -325 1400
3 Carbon Moly Steel 29.2 E6 0.289 0.28935 -325 1400
4 Low Chrome Moly Steel 29.7 E6 0.289 0.28935 -325 1400
5 Med Chrome Moly Steel 30.9 E6 0.289 0.28935 -325 1400
6 Austenitic Stainless 28.3 E6 0.292 0.28930 -325 1400
7 Straight Chromium 29.2 E6 0.305 0.28010 -325 1400
8 Type 310 Stainless 28. 3 E6 0.305 0.28990 -325 1400
9 Wrought Iron 29.5 E6 0.300 0.28070 -325 1400
10 Grey Cast Iron 13.4 E6 0.211 0.25580 70 1000
11 Monel 67% Ni/30% Cu 26.0 E6 0.315 0.31870 -325 1400 12 K-Monel 26.0 E6 0.315 0.30610 -325 1400 13 Copper Nickel 22.0 E6 0.330 0.33850 -325 1400 14 Aluminum 10.2 E6 0.330 0.10130 -325 600 15 Copper 99.8% Cu 16.0 E6 0.355 0.32270 70 400 16 Commercial Brass 17.0 E6 0.331 0.30610 -325 1200
17 Leaded Tin Bronze 1 14.0 E6 0.330 0.31890 -325 1200
In addition
CAESAR IIsupports material types 18 or 19 for cut short and cut long
cold spring elements.
Material number 20 activates the CAESAR II Orthotropic Material Model (i.e.,
Fiber-glass reinforced plastic pipe); the default coefficient of expansion is 12.0 E-6
in./in./
°
F.
Material 21 indicates user-defined properties.
Material numbers over 100 are from the Material Database and include the
allowable stress and other piping code data.
CAESAR II Intersection Types
CAESAR II Type B31.3 Type Notes Sketch 1 Reinforced Reinforced Fabricated Tee Used to lower SIFs
Not a fitting Modified pipe
2 Unreinforced Unreinforced Fabricated Tee Routine intersection
Not a fitting Modified pipe Usually the cheapest
3 Welded Tee Welding Tee Usually size-on-size
Governed by B16.9 Usually the lowest SIF Usually expensive
4 Sweepolet Welded-in Contour Insert Sit-in" fitting
Forged fittings on a pipe
5 Weldolet Branch Welded on Fitting "Sit-on" fitting
Forged fittings on a pipe
6 Extruded Extruded Welding Tee Seldom used
Used for thick wall manifolds Extruded from straight pipe
Code Stresses
Listed below are the Code Stress equations for the actual and allowable stresses
used by
CAESARII. For the listed codes, the actual stress is defined by the left
hand side of the equation and the allowable stress is defined by the right hand side.
The
CAESARIIload case label is also listed after the equation.
Typically the load case recommendations made by
CAESARIIare sufficient for
code compliance. However,
CAESARIIdoes not recommend occasional load
cases. Occasional loads are unknown in origin and must be specified by the user.
US Codes
Longitudinal Pressure Stress - Slp
Slp = PD0/4tn code approximation
Slp = PDi2/(D02- Di2) code exact equation, CAESAR II default
Operating Stress - unless otherwise specified
S = Slp + Fax/A + Sb < NA (OPE) B31.1 Sl = Slp + 0.75 i Ma / Z < Sh (SUS) i Mc / Z < f [ 1.25 (Sc+Sh) - Sl ] (EXP) Slp + 0.75 i Ma / Z + 0.75 i Mb / Z < k Sh (OCC) B31.3 Sl = Slp + Fax/A + Sb < Sh (SUS) sqrt (Sb2+ 4 St2) < f [ 1.25 (Sc+Sh) - Sl ] (EXP) Fax/A + Sb + Slp < k Sh (OCC) Sb = [sqrt ( (iiMi)2+ (i0M0)2)]/Z
ASME SECT III CLASS 2 & 3
< 1.5 Sh (SUS)
i Mc / Z < f (1.25 Sc + 0.25 Sh) + Sh -Sl (EXP)
B31.1 (1967) and Navy Section 505
Sl = Slp + sqrt (Sb2+ 4 St2) < Sh (SUS)
sqrt ( Sb2+ 4 St2) < f (1.25Sc + 0.25Sh + (Sh-Sl)) (EXP)
Slp + sqrt (Sb2+ 4 St2) < k Sh (OCC)
B31.4
If FAC = 1.0 (fully restrained pipe)
FAC | E dT - SHOOP| + SHOOP < 0.9 (Syield) (OPE)
If FAC = 0.001 (buried, but soil restraints modeled)
Fax/A - SHOOP + Sb + SHOOP < 0.9 (Syield) (OPE)
(If Slp + Fax/A is compressive) If FAC = 0.0 (fully above ground)
Slp + Fax/A + Sb + SHOOP < 0.9 (Syield) (OPE)
(If Slp + Fax/A is compressive)
(Slp + Sb + Fax/A) (1.0 - FAC) < (0.75) (0.72) (Syield) (SUS)
sqrt ( Sb2+ 4 St2) < 0.72 (Syield) (EXP)
(Slp + Sb + Fax/A) (1.0 - FAC) < 0.8 (Syield) (OCC)
B31.4 Chapter IX
Hoop Stress: Sh F1Sy (OPE, SUS, OCC)
Longitudinal Stress: |SL| 0.8 Sy (OPE, SUS, OCC)
Equivalent Stress: Se 0.9 Sy (OPE, SUS, OCC)
Where:
Sy= specified minimum yield strength
F1= hoop stress design factor (0.60 or 0.72, see Table A402.3.5(a) of B31.4) Sh= (Pi– Pe) D / 2t
SL= Sa+ Sbor Sa- Sb, whichever results in greater stress value Se = 2[((SL- Sh)/2)2+ St2]1/2
B31.5 Sl = Slp + Fax/A + Sb < Sh (SUS) sqrt (Sb2+ 4 St2) < f [ 1.25 (Sc+Sh) - Sl ] (EXP) Fax/A + Sb + Slp < k Sh (OCC) Sb = [sqrt ( (iiMi)2+ (i0M0)2)]/Z B31.8
B31.8 For Restrained Pipe (as defined in Section 833.1):
For Straight Pipe:
Max(SL, SC) < 0.9ST (OPE)
Max(SL, SC) < 0.9ST (SUS)
SL < 0.9ST (OCC)*
and
SC < ST (OCC) *
CAESAR II prints the controlling stress of the two
SL= SP+ SX+ SB
For All Other Components
SL < 0.9ST (OPE, SUS, OCC)
B31.8 For Unrestrained Pipe (as defined in Section 833.1):
SL < 0.75ST (SUS, OCC)
SE < f[1.25(SC+ SH) – SL] (EXP)
Where:
SL = SP+ SX+ SB
SP = 0.3SHoop (for restrained pipe) = 0.5SHoop (for unrestrained pipe)
SX = R/A
SB = MB/Z (for straight pipe/bends with SIF = 1.0) = MR/Z (for other components)
SC = Max (|SHoop – SL|, sqrt[SL2– SLSHoop + SHoop2]) MR = sqrt[(0.75iiMi)2+ (0.75ioMo)2+
Mt2]
SE = ME/Z
B31.8 For Unrestrained Pipe (as defined in Section 833.1): Continued…
S = Specified Minimum Yield Stress T = Temperature Derating Factor SH = 0.33SUT
SC = 0.33SU
SU = Specified Minimum Ultimate Tensile Stress
B31.8 Chapter VIII
Hoop Stress: Sh F1S T (OPE, SUS, OCC)
Longitudinal Stress: |SL| 0.8 S (OPE, SUS, OCC)
Equivalent Stress: Se 0.9 S (OPE, SUS, OCC)
Where:
S = Specified Minimum Yield Strength
F1= Hoop Stress Design Factor (0.50 or 0.72, see Table A842.22 of the B31.8 Code) T= Temperature Derating Factor (see Table 841.116A of the B31.8 Code)
Note: The product of S and T (i.e. the yield stress at operating temperature) is required in SH of the CAESAR II Input. Sh= (Pi– Pe) D / 2t
SL= maximum longitudinal stress (positive tensile, negative compressive) Se = 2[((SL- Sh)/2)2+ Ss2]1/2
Ss= tangential shear stress
GPTC
Slp + 0.75i Ma/Z < Syield (OPE)
Sl = Slp+Sb < 0.75(Sy)Ft (SUS)
Se = sqrt(Sb2+4St2) < 0.72 (Syield) (EXP)
Note: GPTC is similar to B31.8 with noted changes.
B31.11
If FAC = 1.0 (fully restrained pipe)
FAC | E dT - SHOOP| + SHOOP < 0.9 (Syield) (OPE)
If FAC = 0.001 (buried, but soil restraints modeled)
B31.11 Continued …
(If Slp + Fax/A is compressive) If FAC = 0.0 (fully above ground)
Slp + Fax/A + Sb + SHOOP < 0.9 (Syield) (OPE)
(If Slp + Fax/A is compressive)
(Slp + Sb + Fax/A) (1.0 - FAC) < (0.75) (0.72) (Syield) (SUS)
sqrt ( Sb2+ 4 St2) < 0.72 (Syield) (EXP)
(Slp + Sb + Fax/A) (1.0 - FAC) < 0.88 (Syield) (OCC)
International Codes
Canadian Z662
If FAC = 1.0 (fully restrained pipe)
|E dT - Sh| + Sh < 0.9 S * T (OPE)
If FAC = 0.001 (buried, but soil restraints modeled)
|Fax / A - Sh| + Sb+ Sh < S * T (OPE)
(If Fax / A - Shis compressive) If FAC = 0.0 (fully above ground)
|Slp + Fax / A| + Sb+ Sh < S * T (OPE)
(If Slp + Fax / A is compressive)
Sl= 0.5Sh+ Sb < S * F * L * T (SUS, OCC)
SE= sqrt [Sb2+ 4St2] < 0.72 S * T (EXP)
RCC-M C & D
Slp + 0.75i Ma/Z < Sh (SUS)
iMc/Z < f (1.25 Sc + .25 Sh) + Sh - Sl (EXP)
Slpmax + 0.75i (Ma + Mb)/Z < 1.2 Sh (OCC)
Stoomwezen
Slp + 0.75i Ma/Z < f (SUS)
iMc/Z < fe (EXP)
CODETI
Sl = Slp + Fax/A + Sb < Sh (SUS)
sqrt (Sb2+ 4St2) < f [1.25 (Sl + Sh)] - Sl (EXP)
Slp + Fax/A + iMa/Z + iMb/Z < Ksh (OCC)
Sb = [ Sqrt ((iiMi)2+ (i0M0)2] /Z Norwegian 2 PDi .75Ma SI = 2 2 Z Eff(D0 D )1 + (SUS) iMc/Z < Sh + Sr - Sl (EXP) 2 .75i (Ma + Mb) PmaxDi + 2 2 Z Eff(D -D ) 0 i (OCC) M = sqrt (Mx2+ My2+ Mz2) Sr= Minimum of 1.25 Sc + 0.25 Sh; FrRs-F2; or Fr(1.25R1+ 0.25R2)
The latter applies to temperatures over 370°C; 425°C for Austenitic stainless steel Fr= Cyclic reduction factor
Rs= Permissible extent of stress for 7000 cycles R1= Minimum of Sc and 0.267 Rm
R2= Minimum of Sh and 0.367 Rm
Rm= Ultimate tensile strength at room temperature
FDBR
Sl = Slp + 0.75 i Ma / Z < Sh (SUS)
i Mc / Z < f [ 1.25 (Sc+Sh) - Sl ] (EXP)
BS 7159 If Sxis tensile: < Sh (OPE) 2 2 sqrt (Sx +4S )s and 2 2 sqrt (S +4S )s < Sh*EH/EA (OPE) or, if Sxis compressive: S + xSx < Sh*EH/EA (OPE) and Sx < 1.25Sh (OPE)
( )
( )
2 2 P Dm [sqrt((i M ) +(ixi i xo oM ) )] S = +x 4t Z( )
( )
2 2 P Dm [sqrt((i M ) +(ixi i xo oM ) )] Fx - - A 4t Z(If Fx/A > P(Dm)/(4t), and it is compressive)
( )
( )
MP Dm
S = 2t
for straight pipes
( )
( )
2 2 [sqrt((i M ) +(i M ) )] MP Dm i i o o + 2t Z = for bends( )
( )
2 2 MP Dm [sqrt((i M ) +(ii i o oM ) )] + 2t Z x x = for teesDmand t are always for the Run Pipe Eff = Ratio of E to Ex
UKOOA
ab(f
2/r) + PDm/ (4t) < (f1f2LTHS) / 2.0 Where:
P = design pressure Dm = pipe mean diameter t = pipe wall thickness
f1 = factor of safety for 97.5% lower confidence limit, usually 0.85 f2= system factory of safety, usually 0.67
ab = axial bending stress due to mechanical loads r = a(0:1) / a(2:1)
a(0:1) = long term axial tensile strength in absence of pressure load a(2:1) = long term axial tensile strength in under only pressure loading LTHS = long term hydrostatic strength (hoop stress allowable)
BS 806 Straight Pipe < SAOPE fc = sqrt(F2+ 4fs2) < SASUS < SAEXP fs = Mt(d + 2t) / 4I F = max (ft, fL) ft = pd/2t + 0.5p fL = pd2/[4t(d + t)] + (d + 2t)[sqrt(mi2+ mo2)] / 2I Bends < SAOPE fc = sqrt (F2+ 4 fs2) < SASUS < SAEXP fs = Mt (d + 2t) /4I F = max (ft, fL) ft = r/I * sqrt[(miFTi)2+ (m0FTo)2] fs = r/I * sqrt[(miFLi)2+ (m0FLo)2]
BS 806 Continued … Branch Junctions < SAOPE fcb = q * sqrt[fb2+ 4fsb2] < SASUS < SAEXP fb = (d + t)*p*m/(2t) + r/I*sqrt[(miFTL)2+ (moFTO)2] Fsb = Mt (d + 2t) / 4I
q = 1.0 except for operating cases = 5 or .44 bases on d2/d1ratio in operating cases
m = geometric parameter
EXP SA= min[(H*Sproof ambient + H*Sproof design); (H*Sproof ambient + F)]
OPE SA= Savg rupture at design temperature
SUS SA= min[.8*Sproof, Screep rupture]
Det Norske Veritas (DNV)
Hoop Stress: Sh nsSMYS Hoop Stress: Sh nuSMTS
Longitudinal Stress: SL n SMYS Equivalent Stress: Se n SMYS Where:
Sh = (Pi– Pe) (D – t) / 2t
ns = hoop stress yield usage factor Tables C1 and C2 of DNV
SMYS = specified minimum yield strength, at operating temperature
nu = hoop stress bursting usage factor Tables C1 and C2 of DNV
SMTS = specified minimum tensile strength, at operating temperature
SL = maximum longitudinal stress
n = equivalent stress usage factor Table C4 of
DNV
EN-13480
< Kfn (SUS)
< fn+ fh (EXP)
< Kfn (OCC)
EN-13480 Alternate Option
due to primary loads
< Kfn (SUS)
< fn+ fh (EXP)
< Kfn (OCC)
due to occasional loads
PD8010 Part 1
Hoop Stress Sh< aeSy (OPE, SUS, OCC)
Equivalent Stress Se< 0.9Sy (OPE, SUS, OCC)
Where:
Sy = specified minimum yield strength
e = weld joint factor
a = design factor
Sh
PD8010 Part 1 Continued …
Shl hoop stress using nominal dimensions
ST=
SL Based on restrained/unrestrained status
SLfor unrestrained piping SLfor restrained piping
If FAC = 1.0 (fully restrained pipe)
FAC | E dT - SHOOP| + SHOOP < 0.9 (Syield) (OPE)
If FAC = 0.001 (buried, but soil restraints modeled)
Fax/A - SHOOP + Sb + SHOOP < 0.9 (Syield) (OPE)
(If Slp + Fax/A is compressive) If FAC = 0.0 (fully above ground)
Slp + Fax/A + Sb + SHOOP < 0.9 (Syield) (OPE)
(If Slp + Fax/A is compressive)
(Slp + Sb + Fax/A) (1.0 - FAC) < (0.75) (0.72) (Syield) (SUS)
sqrt ( Sb2+ 4 St2) < 0.72 (Syield) (EXP)
(Slp + Sb + Fax/A) (1.0 - FAC) < 0.8 (Syield) (OCC)
PD8010 Part 2
Hoop Stress Sh< fdhSy (OPE, SUS, OCC)
Equivalent Stress Se< fdeSy (OPE, SUS, OCC)
Where:
Sy specified minimum yield strength
fdh hoop stress design factor (See Table 2)
fde equivalent stress design factor (See Table 2)
Sh=
Se=
Node Locations on Bends
Bends are defined by the element entering the bend and the element leaving the bend. The actual bend curvature is always physically at the TO end of the element entering the bend.
The element leaving a bend must appear immediately after the element defining (entering) the bend.
The default bend radius is 1.5 times the pipe nominal OD.
For stress and displacement output the TO node of the element entering the bend is located geometrically at the FAR point on the bend. The FAR point is at the weld line of the bend, and adjacent to the straight element leaving the bend.
The NEAR point on the bend is at the weld line of the bend, and adjacent to the straight element entering the bend.
The FROM point on the element is located at the NEAR point of the bend if the total length of the element as specified in the DX, DY and DZ fields is equal to: Radius * tan( Beta / 2 ) where “Beta” is the bend angle, and Radius is the bend radius of curvature to the bend centerline. Nodes defined in the Angle # and Node # fields are placed at the given angle on the bend curvature. The angle starts with zero degrees at the NEAR point on the bend and goes to “Beta” degrees at the FAR point of the bend.
Angles are always entered in degrees.
By default, nodes on the bend curvature cannot be specified within five (5) degrees of one another or within five degrees of the nearest end point. This and other bend settings may be changed through the Main Menu, Configure-Setup processor.
When the FROM node on the element entering the bend is not at the bend NEAR point a node may be placed at the near point of the bend by entering an Angle # on the bend spreadsheet equal to 0.0 degrees. For more information see the following figure.
When defining a bend element for the first time in the pipe spreadsheet, nodes are automatically placed at the near and mid point of the bend. The generated midpoint node number is one less than the TO node number on the element, and the generated near point node number is two less than the TO node number on the element. A near point should always be included in the model in tight, highly formed piping systems. The top-left figure below shows the points on the bend as they would be input. The top-right figure shows the actual geometric location of the points on the bend. The bottom-left figure shows the same geometry except that two nodes are defined on the bend curvature at angles of zero and forty-five degrees.
For an animated tutorial on modeling bends, select the ANIMATED TUTORIALS option on the Help
CAESAR II Quality Assurance Manual
The
CAESAR IIQuality Assurance Manual is intended to serve as a publicly
available verification document. This manual discusses (briefly) the current
industry QA standards, the
COADEQA standard, a series of benchmark jobs, and
instructions for users implementing QA procedures on their own hardware.
The benchmark jobs consist of comparisons to published data by ASME and the
NRC. Additional test jobs compare
CAESAR IIresults to other industry programs.
For additional information on the Quality Assurance Manual, please contact the
sales department at [email protected].
Mechanical Engineering News
As an aid to the users of
COADEsoftware products,
COADEpublishes Mechanical
Engineering News several times a year. This publication contains discussions on
recent developments that affect users, and technical features illustrating modeling
techniques and software applications.
This newsletter is sent to all users of
COADEsoftware at the time of publication.
Back issues can be acquired by contacting the
COADEsales staff.
Additional COADE Software Programs
CADWorx Plant
- An AutoCAD based plant design/drafting program with a
bi-directional data transfer link to
CAESAR II.
CADWorxallows models to be created
in ortho, iso, 2D or 3D modes.
CADWorxtemplate specifications, contained with
built in auto routing, auto iso, stress iso, auto dimensioning, complete libraries,
center of gravity calculations, and bill of materials, provides the most complete
plant design package to designers.
CodeCalc
- A program for the design or analysis of pressure vessel components.
CodeCalccapabilities include: analysis of tubesheets, rectangular vessels, flanges,
nozzles, Zick Analysis, and the standard internal/external thickness and pressure
computations on heads, shells, and cones. API 579 calculations are also included.
PV Elite
- A comprehensive program for the design or analysis of vertical and
horizontal vessels. Pressure Vessel Codes include ASME VIII-1 and VIII-2,
PD:5500 and EN-13445.
PVEliteincludes all of the
CodeCalcfunctionality.
TANK
- A program for the design or rerating of API-650/653 storage tanks. The
program includes API 650 Appendices A, E, F, M, P, and S, as well as API 653
Appendix B. Computations address: winds girders, conical roof design, allowed
fluid heights, and remaining corrosion allowance.
A
Additional COADE Software Programs • 26 ASME SECT III CLASS 2 & 3 • 13
B
B31.1 • 13
B31.1 (1967) and Navy Section 505 • 14 B31.11 • 16, 17 B31.3 • 13 B31.4 • 14 B31.4 Chapter IX • 14 B31.5 • 15 B31.8 • 15 B31.8 Chapter VIII • 16 Bends • 20 Branch Junctions • 21 BS 7159 • 19 BS 806 • 20, 21 C CAESAR II Interfaces • 3
CAESAR II Intersection Types • 12 CAESAR II Pipe Stress Seminars • 2
CAESAR II Quality Assurance Manual • 26 CAESAR II Quick Reference Guide Version
5.10 • 1 CAESAR II Software • 2 Canadian Z662 • 17 Code Stresses • 13 CODETI • 18 Computation Control • 6 D Database Definitions • 9
Det Norske Veritas (DNV) • 21
E EN-13480 • 22 F FDBR • 18 G Geometry Directives • 6 GPTC • 16 I International Stresses • 17 L List of Materials • 11 M
Mechanical Engineering News • 26 Miscellaneous Computations • 10
N
Node Locations on Bends • 24 Norwegian • 18 P Piping Codes • 4 Plot Colors • 8 R RCC-M C & D • 17 Restraints • 5 S
Setup File Directives List • 6 SIFS and Stresses • 7
Stoomwezen • 17 System Requirements • 3 T Troubleshooting • 3 U UKOOA • 20 US Codes • 13
12777 Jones Road Suite 480
Houston, Texas 77070
Phone: (281)890-4566
Fax: (281)890-3301
Email:
[email protected]
Web:
www.coade.com
CAESAR IIQuick Reference Guide Version 5.10