entrenamiento caesar ii - coade
TRANSCRIPT
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Table 2-1A-Nozzle Loadings (Sl Units)NoG: E&h valuc shovn b.os idd6 a @8c frcn mjus th, vlhc to Pls dld vle: fo. 6plc 710 idid rdsc frcm -l l0 to +71o.
Noio.r siz of Fld$ (NPS)t ! l
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FI
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^lz., MR
7190 3?8030 48907050 3ll044a0 6920
' 0 lcro8r0 13105E0 690
1280 910
670Jlo
930
3 l 024902050{480
710 070580 890890 r3l0
280 930
890710J80
280
1& 950270 4?0350 7206a0 1280
1420I t60?802560
1420l?80 16025@
1780t120l t @25(o
33060
t8@
249020503 l 0
1780l l l 04890
5140
(10930
5340(101450930
']1i24,4038@?50
6670
I1700
6108mo51!o
I t?m
8000610
l7@
6lm2940
E2tO
'1t20J7808900
2?80
1t208900JTEO
11780
89oO1r20J?80
2',780
6170I 20415l)8540
85066?0
t02301,'a50
E r50loo(10l4aJ0
1023084506?0
t4aJo
310lcrro890
t930
4890r?Eo3 l 06920
3tot76025gJ4710
2300l l8017603t l0
11243605420910
- loc t : = l@i NcMos: t= rcEn( inNceron111.6 : . t=uh . .SeF is r lG2-2-24 forr ia@ionofao?r . @dr(X.v .da.
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\-{or. t: Cedir. 5F1@ h! tfrn cts.i frcm API Stnd.rd 10, ?$ Fitoq s!!6r1oo ro 5O r 5ol .dnv..tio-
Table 2-1H{ozzle Loadings (U.S. Units)Nor.: Esn vlq shol; b.o* indid6 a tus fm mi6 tnd vauc to ps nt vIrc; fo..replc 60 idi@ dgr 6m-160 t +l0.
Nonint S4f n&e!(NPS)t z l 4 l6l0
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tx
fz
t @r3@2m2900
60 240!10 2M2@ 3@290 430
8507@| lm
1560
5@7@4&
t00
)2i2@4q)570
320
260570
32026/J570
9805@
D0
5&lO?@
t0t0
l2@1000tJlo22@
t2@1500lmo22gJ
t5!o1200t000'22gJ
l?ml8o2E@5@O
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t5008q)t200?gJ
l8l5@t20zffi
l9@l5o23@33{I)
MIuzUR
2&3002@130
3@240200410
7001505309JO
l@200ll0290
20)6)1302q)
340t702@
560
t0lo
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130023lO
650 l m7m
t56{'
t m850
t50
26@tl&t9m35m
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2@lmt l@2900
?3@9005m33m
r90o?3001500ll@
15@ 4?m 5,10022@ 2300 2?003{0 35m !@06tm 6300 72!4
Nr. ; f = fo@ in ro{{b: 1= mv.Ent n fd-Fudsi ^ = ll$lbt s* 8! 2-2: 2{ fo. o.icn@in of o2] lo.ds (rC y. ad .No. 2: C@rdir. 'trd d be! .ttig.n trch ^P Srd.il lO, ?rb Editior, .oov.ntd (. ISO lsof, c@adtioa
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Fioure 2-5 -Coordinaie Syslri lor the Forces and Moments in Table 2'1A (2'18)Horizontal Pumpswith End Suction and Top Discharge Nozzles
bv a combinatioo of shafl diameler' shaft sPa or ovrhag'and casing design iincluding the use ofdual voutes or dif-fisers). For one and two srage pumps- no credi shall b lkenfor fluid sdffening effcts of imPellr wea rings For mul-delaee Dumps, tluid sffening effecb shll b considered andcdc;la;ons shallbe performcd ar both one and two rimes thenominal design cleaances. The fiuid stiffness of Product tu_bricated beaings and baring bushings shll be calcutarcd atbo one d two dmes lhe nominal design clearances'
'2.5.8 whn nonconcng vibtion probes te fumished i
-- ac(omdce *irh 3 4.3 1. e lolor shaft sen\ins areas (o be ob_/ ) ,ene by rad,af vrbra(ion probes shllhe 'olcenu-ic wirh thi'
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arins ;um]s. AIl shaft sensing are$ lborh roial vibration\ sd ri oositonl shall be fre from srencil and scribe maik
' or av oer sulace discontinuity' such s a: oil hole or a key-wav- for a mininum disrance of oe pob tp diameler one side ofrhe probe. These areas shall no be mallizd'
sleved" or plaled Thc tlnal surface tinish shall b a maximumof I .0 gm (32 Fin.) Ri. Preferably obta:ned by honing or bur-nishing. These aeas shall be propeiy demagnetized to thelevels specifed in API Standrd 670. or oerwise treated sohal e combined tod electric.Iand mechanical runour doesnot xceed he foUowing:i- For a'eas to be observed by radial vibradon Probes. 25percent of the allowed Peak-to-Peak vibration amplilude or5 gm (0.25 mil). whicheYer is greater.b. For areas !o be observed by axiai Position probes. 15 Fm(0.5 mil).2.5.9 Electrical and necharical runout of lhe roto sur-facei ro b obsen'ed by vibration probes shall be derrmiredand rcorded. Th runour shall be detrmined by rollingrhe roror supponed by v-blocks posi.ioned ar the centerlineof ihe beringjoumals while measuring runout with a non-conracling vibraion Pobe ad a dial indicator simultane-
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F.1 Horizontal Pumps
F.1.1 Acceptable piping conilguraons should not cause excessve misalignment between th pump and driver-
Piping configurations thal proouce comgonent nozzle tosds lying wthin the ranges slecifed in Table 4 limit casng
disroftion to one ha' me pump """"","
.."ig;-..'1."; ("e si-g) an ensure pump shaft displacement of lessthan 250 Pm (0,010 in) '
F.1.2 Pping configurairons that prooce loads ouiside the ranges specined in.Table 4 are also acceptable
w hout consuharion wrth the pump r""oo, r i" "-t1.".
specied in F t-z.a),ftroush l-1 ? c) are.salisled-Siiii]ii" 1."1,on"
"n!,,"i ii'"t unv pu*p casins distortion ll be within the vendor's desisn critera {see
il.ij'..i, ii"iin" o'"olacement or the pump shaft wll b; less than 380 pm (0 01s in) rhis clause is a criterion ror
piping desgn only.
a) The indrviduat component torces and moments acting on eachpump nozzle flange shall not exceed the range
soecif ied in Tble 4 by a faclor o ' more lhan 2
$ '"h'fi:5;},ij.g53,.5',,:,15f,i*55,',.*,::i"ilt,:T,"#:'.r5iJ;1fl?s"" '*"^ MRD', actins on each(F.1)(F.2)
") T'^,:itl:"T#;H:3:ffiJ##i[fl:,,fi:i.:T]"'itfe!:G,q"!if",:E!i:i'fiff5i:iti4]::r#';iil:":L"m:,r{*""#:*ruil*?liJ;.iilxl,";i',,i1'"""11:.,::xi,l;;xli.'.ill"T;l'L:'ll"
(F3)(F.4)(F.5)
AP Slandard 610-Oentr l lugal PUmps ror Helroleum' reLucrrrrtr la q
Annex F(normative)
Crteria for piping design
lrrtsA/ (f ,5 x ffsra)l + IMRt^ / (t.t x MR&4')) < 2
FRD ^t (t,5 x FR,TIi+ IMRD^| (1'5 x MRDiI)
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AP Standard 610-'Cenlrifugal Pumps for Petroleum, Pet'ochemica and Natu'al Gas Indstr'es
MR)A.= IIMX: ^ )? + (wc a)2 * (Mzc^)'?)os
MXC^= MXS^+ MxD^- t{flliA) (zS) + (FrDaXzD) - (Fz&) (v0 - (rzD) (vD)l / 1 000
r[vca= Mvsa + Mm ^ + t(F.x.s) (z t +{,qDaXrD ) - (Fzs4{xs) - (rzd (D) / I 000
Mzc^ = Mzsa+ MZD ^- I(,.xsa) (r.t) + (toa) (rD) - {fl/s) (ts) - {1D ) (DI / 1 000
tn US Custoary units, the constant 1 000 shall be changed to 12 fhis constant is the conve6ion factor to change
mllimetres to melres orinches to feet
F.1.3 Pping configJrations thar produce loads grealer than those allowed n F'1'2 shall be approved by the
pLrrchaser and the venoor'
F-2 Vertical in l ine Pumps
Verticainline pumps fhat are supported only by lhe attached piping may be subiected to componenl pipng loads
ur",o," "n orHe the vatues shown n iable 4 il these loads do not cause a princpal stress greater than
, , N, ,- -2 / .r q n nsir io eirher noz e. ror callulaton ourpose". t" se"tion properi;es of the pump nozzles shall be;j=:; iil '..'."i,i; !; ;;;;;;;;f;;.i; q";i i" inat ot te pp'opate sJmp nozzre Equarion F 6'e"iri* f.i, an Equaron F-8 cn be used to evlual Principal stress' longitudnal stress' and
shear stress
respectively, in the noz|es.P = k i 2 ' ) + l d t 4 + l o F < 4 | ( F 6 )
o=11,27 x Fv / (D.2 -Di1) l+la2ooxD"@f +Mto5lt(o.o'Ol lF 7' l
r = f t 2 1 x ( F x 2 + F ) 6 1 / ( D . r - D ; ) + t 5 l o 0 x D " ( W l t r l t q . ' - D : ) ( F e )
For IJS Customary units. ihe following equations apply:
r*
P = ( o t z \ + l d t 4 + ) 6 < 5 d 5 0
o = 0,2't x F v / Q o1 - D i2 1 + 1r:2. o. 1u + ut )o5 ) t (D : - D i t
f = t1,27 x(FX2 + Ft \ 1t @.1- D3 +l6t xD.(WYtr) | @"1- D\
P s the principal stress, expressed n MPa (lbfn2); is the tongtqdanalslress. exffessed n MPa (lbf; is the snearstess, expressed in MPa { lbf / in1:FX is the applied force on lhe X axsi
FY s the applied force on the Y axisi
FZ is the appld force on the l axis;
,e s the appled moment on the X axis;
Mf rs lhe appled moment on the Y axis:
MZ s lhe appled momen on he Z axis;
Di. D" is the innerand ouler diameters ot ihe nozzles, exPressed n m (in)'
(F.s)(F.10)(F-1r)
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i ie. '=j:= _= c
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