C.C.M.A.I. - PROIECT
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Transcript of C.C.M.A.I. - PROIECT
UNIVERSITATEA POLITEHNICA BUCURESTIFACULTATEA TRANSPORTURI
INGINERIA AUTOVEHICULELOR
Calculul si constructia motoarelor cu ardere interna- PROIECT –
Coordonator: prof.dr.ing.Negurescu NiculaeStudent: VIERU CristianGrupa: 8402a
Bucuresti, 2014
1
1. Tema proiectuluiMotor cu ardere prin comprimare (MAC)Pe=160kWn = 2300 rot/minε = 15,5i = 6 cilindriλ = 1,75supraalimentatps=0,26MPa
2. Analiza performantelor unor motoare similare
pe=30 ∙ τ ∙ PeV s ∙n ∙ i
[MPa ];
PL=PeV t
;
Ps=
104 ∙ Pe
i ∙π ∙ D2
4
[ kWdm2 ];
W pm=s ∙ n30∙10−3[m /s ]
Observatii:
1. Toate motoarele alese au configuratia DOHC cu cate 4 supape pe cilindru.
2. Camera de ardere a motoarelor este de tip omega.
3. Racirea tuturor motoarelor se face cu lichid.
4. Toate motoarele sunt supraalimentate.
5. Motoarele au fost alese din gama urmatorilor producatori: IVECO, DAF, FENDT, JCB, TEREX, ITAL MOTORS.
2
Alt
e da
te
Tec
tor
E18
Tec
tor
E22
PR18
3
AW
1-IV
-38
Den
tz T
CD 2
012
EPA
201
0
N60
EN
TV
N61
EN
TV
N40
EN
TV
C78
ENT
V
Wpm
m/s
10.8
10.8
9.8
10.1
8.82
8.72
10.8
10 10.8
7.70
8
Ps
Kw
/
dm3
26.5
29
32.6
51
27.9
03
32.9
12
26.7
03
24.8
15
32.6
51
37.7
52
27.3
45
28.8
97
pe
MPa 0.9
1.2
1.1
1.2
1.2
1.1
1.2
1.5 1 1.5
Pei
kW/c
il
26.6
6
26.6
6
30.5
31.8
3
21.3
8
26.6
6
26.6
6
30.8
3
22.3
3
30
i - 6 6 6 6 6 6 6 6 6 6
Vt
l;
cm3
5880
.3
5880
.3
9181
.4
8414
.6
6053
.8
7672
.5
5880
.3
5880
.3
5880
.3
7786
.2
Vs
l;
cm3
980.
05
980.
05
1530
.2
1402
.4
1008
.9
1278
.7
980.
05
980.
05
980.
05
1297
.7
Ψ -
1,17
6
1,17
6
1,18
6
1,30
6
1,24
7
1,01
7
1,17
6
1,17
6
1,17
6
1,08
6
ε -
15.3
15.3
17.4
16.2
14.1
16.5
17 17 17 16.5
sm
m
120
120
140
145
126
119
120
120
120
25
D mm
102
102
118
111
101
117
102
102
102
115
nrp
m
2700
2700
2100
2100
2100
2200
2700
2500
2700
1850
Pe
kW 160
160
183
191
128.
3
160
160
185
134
180
Nr.
cr
t. 1 2 3 4 5 6 7 8 9 10
3. Calculul ciclului motor
3.1. Calculul admisiei
Observatii:
1. Datorita faptului ca motorul este supraalimentat vom inlocui T 0cu T s=T 0 ∙( psp0 )m−1m −∆T racire si T 0
' cu
T s'=T s+∆T . Astfel valorile lor sunt: T s=336,41K si T s
'=344,41K .
2. Pentru ΔT am ales 8K.
3. Pentru rapoartele pgps
si paps
am ales 0.8, respectiv 0.94.
4. Pentru T g am ales valoare de 800 K.
5. Pentru m am ales valoare de 1,6 .6. Se neglijeaza avansul la deschiderea si intarzierea la inchiderea supapelor.7. Amestecul este unul de gaze ideale.8. Transformarile de comprimare si destindere sunt politropice cu coeficienti constanti.9. Incarcatura proaspata se incalzeste cu ΔT.10. La inceputul admisiei se gasesc gaze arse reziduale.11. Admisia se face la presiune constanta.12. Calculul este pentru ciclul ipotetic.13. Doza de combustibil este de 1 kg.14. Valorile variabilelor au fost alese din urmatoarele tabele:
Tabel 1. Valoarea ΔTTipul motorului ΔT [grade]MAC Supraalimentat 5..10
Tabel 2. Valoarea pgTipul motorului pgSupraalimentat Turbosuflanta (0,70..0,90)ps
Tabel 3. Valoarea T gTipul motorului T g [K]MAC 600..900
Tabel 4. Valoarea paTipul motorului paSupraalimentat Turbosuflanta (0,91..0,985)pg
3.1.1. Coeficientul de umplere ηV si presiunea la sfarsitul admisiei Pa (k=1,4, P0=0 ,1MPa, T 0=298K ¿ :
(1)
ηV=pa ∙ [ε+ (k−1 ) ∙ (ε−1 ) ]−pg
ps ∙(ε−1)∙ k ∙T ' sT s
=pa ∙ [ ε+ (k−1 ) ∙ (ε−1 ) ]
ps ∙(ε−1)∙ k ∙T ' sT s
−pg
ps ∙ (ε−1 ) ∙ k ∙T ' sT s
=0,94 ∙15,5+(1,4−1 ) ∙ (15,5−1 )
(15,5−1 ) ∙1,4 ∙ 344.41336.41
− 0,8
(15,5−1 ) ∙1,4 ∙ 344.41336.41
=0.925
3
3.1.2. Coeficientul de gaze de ardere reziduale γ :
(2) γ=pgps∙1ηv∙1ε−1
∙T sT g
=0.94 ∙ 10,925
∙1
15,5−1∙336.41780
=0,0302
3.1.3. Temperatura la sfarsitul admisiei T a:
(3) T a=paps∙1ηv∙εε−1
∙1γ+1
∙ T s=0,94 ∙1
0,925∙15,515,5−1
∙1
0,03+1∙336.41=354,79K
3.2. Calculul comprimarii
3.2.1. Presiunea la sfarsitul comprimarii
(4) paV amc= pcV c
mc => pc=¿ pa ∙ εmc=0,239∙15,51,35=¿ 9,67 MPa
3.2.2. Temperatura la sfarsitul comprimarii
(5) T aV amc−1= T cV c
mc−1=> T c=T a ∙ εm c−1=354.79∙15,50,35=925.94K
Observatie: Conform rezultatului presiunii de la sfarsitul confirmarii constatam ca discutam despre un MAC rapid.
3.3. Calculul arderiiDate initiale:- Compozitia chimica a combustibilului 1kg = c + h + o
tip combustibil c[%] h[%] o[%] Hi [kj/kg]MAC Motorina 85,7 13,3 1 41855
H i - puterea calorifica inferioara
Observatie: Datorita valorii coeficientului de exces de aer λ = 1,75 rezulta ca discutam despre MAC rapid cu injectie directa in volum.
Coeficientul de utilizare a caldurii ξ z=0,7. .0.88→MACrapid cu injectiedirecta (ID).
3.3.1. Compozitia gazelor de ardereLa arderea unui kg de combustibil rezulta [kmol/kg]:- cantitatea teoretica de aer:
(6) Laert=10,21
∙( c12+ h4− o32 )= 1
0,21∙( 0,85712 +0,133
4−0,01032 )=0,496[kmol/kg]
- cantitatea reala de aer:
(7) L=λ ∙ Lt=0,868 [kmol/kg]
- cantitatile de gaze de ardere:
(8) NCO2= c12
=0,85712
=0,071[kmol/kg]
(9) N H 2O=h2=0,133
2=0,0665 [kmol/kg]
(10) NO2=0,21∙ ( λ−1 ) ∙ Lt=0,078 [kmol/kg]
(11) N N2=0,79 ∙ L=0,685 [kmol/kg]
- cantitatea totala de gaze de ardere
(12) N f=∑j
N j=NCO2+NH 2O
+NO 2+N N 2
=0,071+0,011+0,078+0,685=0,845 [kmol/kg]
- participatiile molare (volumice) ale gazelor de ardere
4
(13) nCO2=NCO2
N f
=0,0710,845
=0,084 kmol/kg
(14) nH 2O=NH 2O
N f
=0,06650,845
=0,013 kmol/kg
(15) nO 2=N O2
N f
=0,0780,845
=0,092 kmol/kg
(16) nN2=N N2
N f
=0,6850,845
=0,81kmol/kg
(17) n f=nCO2+nH 2O+nO 2
+nN 2=0,084+0,013+0,092+0,81=0,999kmol /kg
(18)rCO2=nCO2
nf=0,0840,999
=¿ 0,084
(19)rH 2O=nH2On f
=0,0130,999
=¿ 0,013
(20)rO2=nO2n f
=0,0920,999
=¿ 0,092
(21)rN2=nN2n f
= 0,810,999
=¿ 0,81
- coeficientul chimic (teoretic) de variatie molara:
(22) μc h=N f
N0=¿ 1,02 > 1 (23) N0=L=0,868kmol /kg
- coeficientul total (real) de variatie molara:
(24) N g=γ ∙ N0=0,026 kmoli
(25) μ=N f+N g
N0+N g
=γ+μc1+γ
=1,019<μc
(26) U g¿TC=∑ r i ∙U i ¿TC(27) U aer ¿TC
1=1000=22047<U aer ¿TC=1027,65=?<U aer ¿T C
2=1100=24562kJ /kmol
(28) U aer ¿TC=1027,65=U aer ¿T C1
+(U aer ¿TC2
−U aer ¿T C1
) ∙T C−T C1TC2−TC1
(29) U aer ¿TC=1027,65=22047+(24562−22047 ) ∙ 1027,65−10001100−1000
=22742,39kJ /kmol
(30) UCO2¿TC=1027,65=UCO2
¿TC1
+(U CO2¿TC
2
−UCO2¿T C
1
) ∙T C−T C1T C2−TC1
(31) UCO2¿TC=1027,65=34443+(39100−34443 ) ∙ 1027,65−1000
1100−1000=35730,66 kJ /kmol
(32) U H 2O¿TC=1027,65=U H2O
¿T C1
+(U H 2O¿TC
2
−U H 2O¿TC
1
)∙T C−T C1TC2−TC1
(33) U H 2O¿TC=1027,65=27696+(31036−27696 ) ∙ 1027,65−1000
1100−1000=28619,51kJ /kmol
(34) UO2¿T C=1027,65
=U O2¿TC
1
+(UO2¿TC
2
−U O2¿TC
1
)∙TC−TC1T C2−T C1
5
(35) UO2¿T C=1027,65
=23013+(25696−23013 ) ∙ 1027,65−10001100−1000
=23754,84 kJ /kmol
(36) U N2¿TC=1027,65=U N2
¿TC1
+(U N2¿TC
2
−U N 2¿T C
1
) ∙T C−T C1T C2−T C1
(37) U N2¿TC=1027,65=21791+(24265−21791 ) ∙ 1027,65−1000
1100−1000=22475,061kJ /kmol
Conform (26) => U g¿TC=rCO2 ∙U CO2¿T C
+rH2O ∙UH 2O¿T C
+rO2 ∙UO 2¿TC+rN2 ∙U N2
¿T C
¿0,084 ∙35730,66+0,013 ∙28619,51+0,092 ∙23754,84+0,81 ∙22475,061¿23763,67kJ /kmol
(38)
I z=ξ z ∙H i
μn0 ∙(1+γ )+U aer ¿T C
+γ ∙U g ¿TCμ ∙(1+γ )
+R ∙ λp ∙ Tc
μ= 0,78 ∙418551,019∙0,868 ∙1,03
+ 22742,39+0,03 ∙23763,671,019∙1,03
+ 8,315 ∙1,6 ∙1027,651,019
=67924,33
Din tabelul urmator voi alege T z1 si T z2
Tipul motorului T z [K]MAC ID 1800 - 2800
Aleg T z1 =1900 K si T z2=2000K
(40) I z1=∑ ri ∙ I i¿I z1
=rCO2∙ ICO2
¿I z1
+rH 2O∙ IH 2O
¿I z1
+rO2 ∙ IO2¿I z1
+rN2 ∙ IN 2¿I z
1
¿0,084 ∙94866+0,013∙77753+0,092 ∙64014+0,81∙61206¿64445,68
(41) I z2=∑ ri ∙ I i¿I z2
=rCO2∙ ICO2
¿I z2
+rH 2O∙ IH 2O
¿I z2
+rO2 ∙ IO2¿I z2
+rN2 ∙ IN 2¿I z
2
¿0,084 ∙100904+0,013∙82846+0,092∙64796+0,81∙67776¿70412,72
(42) I z=¿ 67924,33 ϵ [ I z1 , I z2 ]=[64445,68 ;70412,72]
(43) T z=1900+100 ∙67924,33−64445,6870412,72−64445,68
=1958,29K ϵ [T z1 , T z2 ]
(44) pzV z=(ng+n f) ∙R ∙T z(45) pcV c=(n0+ng) ∙R ∙Tc (:)
(46) pzpc∙V z
V c
=μ∙T zTc
=¿ λ pρ=μ∙T zTc
=¿ ρ=μT zλ pT c
=1,019 ∙1958,291,6 ∙1027,65
=1,2136
3.4. Calculul destinderii(47) pb ∙V a
md=pz ∙V zm d
(48) λ p=pzpc
=¿ pz= λp ∙ pc=1,6 ∙9,67=15,482MPa
(50) pb=15,482∙( 1,21315,5 )1,25
=0,727 MPa
6
3.5. Trasarea diagramei ciclului de referinta
3.5.1. Diagrama ciclului real
(51) ηd=LiL' i
=0,94
(52) Δp=pg−pa=0.8−0.94=−0.14
(53)p'i=pa ∙ ε
mc
ε−1∙{λ p ( ρ−1 )+
ρ ∙ λpmd−1
∙[1−( ρε )md−1]− 1
mc−1∙(1− 1
εmc−1)}− ρp ∙ Δp
¿ 0.8 ∙15.51.35
15.5−1∙ {15.482 (1.21−1 )+ 1.21 ∙15.482
1.25−1∙ [1−( 1.2115.482 )
1.25−1]− 11.35−1
∙(1− 115.51.35−1 )}+0.3 ∙0.14
p' i=1,611MPa
3.5.2. Calculul marimilor caracteristice ale ciclului real
(54) pi=LiV s
=ηd ∙ p 'i=0,94 ∙1,611=1,514MPa
(55) ηi=LiH i
=p i ∙V s
H i
=p iH i
∙V 0ηv
= 1,03141855
∙5770,920,92
=0,41
(56) V 0=n0RT sps
=0,4747∙8,314 ∙380,180,26
=5770,92cm3
(57) c i=3600ηi ∙H i
= 36000,15 ∙41855
=209,783 g/kwh
3.5.3. Calculul marimilor caracteristice efective(58) pe=ηm∙ p i; ηm=0,8(59) pe=0,8 ∙1,514=1.02MPa(60) ηe=ηmηi=0,8 ∙0,41=0,328
(61) cc=3600ηe ∙ H i
= 36000,328∙ 41855
=262,2g /kwh
3.5.4. Calculul dimensiunilor de baza ale motorului
(62 )ψ= SD→ψ=1,176
(63) Pe=pe ∙ i ∙ n
30 ∙ τ∙π D3
4∙ψ=160kW
(64) D=102∙ 3√ 4 ∙30 ∙ τ ∙Peπ ∙ψ ∙ pe ∙i ∙n=102 ∙ 3√ 4 ∙30∙3 ∙160
π ∙1,176 ∙1.02∙6 ∙2300=103.6mm=104mm
(65) S=ψ∙ D=1,176 ∙104=122mm
(66) V s=π D2
4∙ S=π D
3
4∙ψ=1038.4 cm3
(67) V t=1038.4 ∙6=6230.4cm3
(68) PL=PeV t
= 16010,0578
=15,9kW /L
7
(69) Ps=
104 ∙Pe
i ∙π D 2
4
=22,82kW /cm2
(70) W pm=S ∙n30
∙10−3=144 ∙230030
∙10−3=11,04m / s
(71) ηd=LiL' i
=¿Li=0,94 ∙1838,57=1728,25kJ /ciclu
(72) V c=V S
ε−1=167614,5
=115,58cm3
0 20 40 60 80 100 120 140 1600
0.51
1.52
2.53
3.54
4.55
5.56
6.57
7.58
8.59
9.510
10.511
11.512
12.513
13.514
14.515
15.516
pxc [MPa]pxd [MPa]ps [MPa]Series8pi [MPa]
PMI PME
8
4. Calculul dinamic
4.1. Estimarea maselor in miscare de rotatie
(73) K= Fcosβ
−fortadin biela
(74) N=F ∙tgβ
(75) T=F ∙sin (α+β)cosβ
(76) z=T ∙cos (α+ β)cosβ
(77) M=T ∙ R(78) sinβ= λ ∙ sinα
(79) λ=RL
=15
(80) J p=R ∙ω2 ∙ (cosα+ λ ∙cos2α )[ms2 ]
(81) ω=π ∙n30 [ rads ]=240,85[ rads ]
(82) F=Fg+F t
(83) Fg=π ∙D2
4∙ ( pg−pcarter )
(84) F t=−mt ∙ J p−fortade inertie∈translatie(85) m p=2,43kg(86) ms=1,5g(87) mb=0,94kg(88) mL=3,7 kg(89) mgp=mp+mb+ms=2430+1,5+940=3371,5 g=3,371kg(90) mt=mgp+0,275 ∙mL=3,371+0,275 ∙3,7=4,3885 kg
9
5. Pistonul5.1. Solutia constructiva si alegerea materialului
5.2. Dimensionarea si calculul de verificare
(91) D = 104 mm
Capul pistonului
(92) Δp=D [1+α c (t c−t 0 ) ]−∆ 'c
1+α p(t p−t 0)(93) α c=(11…12 ) ∙10−6K−1. Aleg α c=11 ∙10
−6K−1
(94) α p=(17…24 ) ∙10−6K−1 . Aleg α p=20 ∙10−6K−1
(95) t c=110…120 °C . Alegt c=115° C(96) t p=300 °C(97) t 0=25 °C(8 ∆ 'c=(0,002…0,003 ) ∙ D=¿∆'c=0,002 ∙104=0,208(99) ∆c=(0,003…0,005 ) ∙D=¿∆c=0,004 ∙104=0.416
∆ p=104 ∙ [1+11 ∙10−6 (115−25 ) ]−0,244
1+20 ∙10−6(300−25)=103.29mm
Manta
(100) ∆m' =(0,0003…0,0013 ) ∙ D=¿ ∆m
' =0,0008∙104=0,0832(101) ∆m
❑=(0,001…0,002 ) ∙D=¿∆m=0,0015 ∙104=0,156(102) tm=200 ° C
(103) ∆ pm=D [1+αc (tc−t0 ) ]−∆ 'm
1+α p (tm−t 0 )=104 ∙ [1+11 ∙10−6 (115−25 ) ]−0,0976
1+20 ∙10−6 (200−25 )=103.64
Verificarea capului pistonului
(104) σ r=34pmax ( ∆ i2δ )
2
<30…60N /mm2
Se aleg {∆i=60mmδ=15mm
(105)σ r=34∙17 ∙( 602 ∙15 )
2
=51 Nmm2
<60N /mm2
Regiune port segmentiVerificarea la compresiune
(106) σ c=FgmaxASU
<30… 40N /mm2
(107) Fgmax=Fg370°=132519,92N
10
(108) ASU=π4
(∆SU2 −∆ i2)−z ∙ d0 ∙
∆SU−∆i2
(109) aSU=5,1mm(110) ∆SU=∆p−2 ∙ a=103−2 ∙5,1=92.8mm(111) z = 8 gauri(112) d0=3mm
ASU=π4
(95,112−602 )−8 ∙2∙ 95,11−602
=8855,88 (107)
(113) σ c=1491383855,88
=38,67<40conditie verificata
Verificare la intindere
(114) σ i=1ASU
∙mps ∙R ∙ω2 ∙ (1+ λ )<4MPa
(115) m ps=13∙m p=
13∙1,28=0,424 kg
(116) R = 63 mm(117) ω=272 ,271rps(118) λ=1,75
(119) => σ i=1ASU
∙mps ∙R ∙ω2 (1+λ )= 1
3855,88∙0,424 ∙0,061∙272,2712 (1+0,25 )=0,621MPa<4MPa
Presiunea maxima pe manta
(120) Pmax=Nmax
D ∙ Lm−Acv<1,5MPa
(121) Nmax=9802N(122) Lm=100mm
(123) Acv=102mm2
(124) => Pmax=9802
106 ∙100−102=0,93MPa<1,5MPa
Verificarea la forfecare
(125) τ=0,5 ∙F gmax
π4
(du2−d2 )<40 N
mm2
(126) Fgmax=149138N(127) du=61mm(128) d=36mm
(129) => τ= 0,5 ∙149138
π4
(612−362 )=39,15 N
mm2<40 N
mm2
11
6. Axul pistonului (boltul)
(130) l = 2l p+2 j+lb
(131) ∝=d id
(132) j = 1 … 2 mm
(133) F=Fgmax−m p ∙ R ∙ω2 (1+ λ )
(134) F=141665 ,5N
(135) Pp=F
2 l p ∙ d
(136) l p=25mm(137) lb=36mm=¿ l=2 ∙25+2 ∙1,5+36=89mm(138) j = 1,5 mm(139) d i=22mm
(140) ∝=2236
=0,61=¿P p=149665,52 ∙25 ∙36
=78,7 N
mm2<90 N
mm2
(141) Pb=Pl p ∙ d
=141665,536 ∙36
=109,31 N
mm2<180 N
mm2
(142) M i=F2 ( 12−23 l p 14 lb)=1334017Nmm
(143)σ imax=F ¿¿
Bolt flotant
(144) cσ=
σ−1
βσεσ ∙ γ
∙ σv
∈1…2
(145) σ V=σ imax=332,26N
mm2
(146) βσ=1(147) ε σ=0,85γ=1,1…1,5 (cementare ) = 1,5 … 2,9 (nitrurare)(148) γ=2
(149) σ−1=280…320N
mm2(OLC 45 )→σ−1=300
N
mm2
(1)50 cσ=
3001
0,85 ∙2∙ ∙342,26
=1,41∈(1 ;2,2)
Verificare la forfecare
τ=0,85∙ F ∙(1+∝+∝2)
d2∙(1−∝4)=0,85 ∙141665,5 ∙(1+0,61+0,612)
362 ∙(1−0,614)=214,27∈150…220 N
mm2
Verificare la ovalizare
12
σ i=−F ∙Kl∙d [0,19 ∙ (1+2∝ ) (1+∝ )
(1−∝2 ) ∙∝+11−∝ ]∈250…350MPa
k=1,5−15 (∝−0,4 )3=1,36
¿>σ i=−141665,5 ∙1,36
89 ∙36 [0,19 ∙ (1+2 ∙0,61 ) (1+0,61 )(1−0,612 ) ∙0,61
+1
1−0,61 ]=272,243∈250…350MPaVerificare la deformare
∆ '=(0,001…0,005 ) ∙ d=0,0036…0,18∆ '2
=0,018…0,09
f b=0,09 ∙F ∙ KE ∙l ( 1+∝1−∝ )
3
<0,5∆ '
f b=0,09 ∙141665,5 ∙1,36
210000∙89 ( 1+0,611−0,61 )3
=0,78
∆ '=0,004 ∙ d=0,156
∆=∆'+d [∝b (tb−t 0)−∝p ( t p−t0 ) ]
1+∝p ( t p−t0 )=0,144+36 ∙ [11 ∙10−6 (425−298 )−20 ∙10−6 (450−298 ) ]
1+20∙10−6 (450−298 )=0,09
7. Segmentii
Segment de compresiea=4mm,h=3mmk=1,77c=0,209m=0,5
R=D2
=1042
=52mm
r=D−a2
=104−42
=50mm
i=h ∙a3
12=16mm4
E=(8,5…17 ) ∙104 N
mm4=100000 N
mm4
pE=0,12MPa
σ emax=pE ∙ k
2 [3∙(Dn −1)2
−1]=0,12 ∙1,3792 [3 ∙( 1224 )2
−1]=224,767 Nmm2
∈220…260 Nmm2
s0=(3−c)π ∙R ∙h ∙ r3∙ pe
E ∙ i=13,87mm
13
σ dmax=2 ∙m∙ E
(Da −1)2 ∙[1− so
(3−c ) ∙ π ∙ a ]=92,97<260MPa
Rostul in stare libera
s0=(3−c)π ∙R ∙h ∙ r3∙ pe
E ∙ i=
(3−0,209) π ∙52 ∙3 ∙593 ∙0,12105 ∙16
=13,87∈12,8…16
Rostul la montaj
sm=s'+πD∙ [∝s (T s−T 0 )−∝c (T c−T0 ) ]
1+∝s (T s−T 0 )=0,2+π ∙122∙ [11 ∙10−6 (520−298 )−11 ∙10−6 (388−298 ) ]
1+10 ∙10−6 (520−298 )¿>sm=0,68mm
Segment de ungerepe=0,21a=5mmh=6mm
r=D−a2
=104−52
=49,5mm
i=h ∙a3
12=62,5mm4
σ emax=pE ∙ k
2 [3∙(Dn −1)2
−1]=0,21 ∙1,7792 [3 ∙( 1224 )2
−1]=259,67 Nmm2
<260 Nmm2
s0=(3−c)π ∙R ∙h ∙ r3∙ pe
E ∙ i=
(3−0,209) π ∙61 ∙3 ∙593 ∙0,12105 ∙16
=12,06∈12,8…16
σ dmax=2 ∙m∙ E
(Da −1)2 ∙[1− so
(3−c ) ∙ π ∙ a ]=177,62<260MPa
sm=s'+πD∙ [∝s (T s−T 0 )−∝c (T c−T0 ) ]
1+∝s (T s−T 0 )=0,2+π ∙122∙ [11 ∙10−6 (520−298 )−11 ∙10−6 (388−298 ) ]
1+10 ∙10−6 (520−298 )¿>sm=0,68mm
14
8. Bielahb=2,9mmhcuz=2mmlM=38mmdM=69mmlc=88mmdci=73mmlb=36mmd s=12mmL=250mmmg p=2,1kgR=63mmω=272,271λ=0,25Fgmax=149138N
H p=42mmH c=50mmH=46mmB=34,5mmH i=Bi=7,68mmh=30,63mmhp=9,1mmdc=60mmd i=41,8mmd=36mm
F i=mg p ∙R ∙ω2 ∙ (1+ λ )=12259,5N
F i=Fgmax−mg p ∙R ∙ω2 ∙ (1+λ )=136879,5N
Intindere
M A=10−4 ∙ Fi ∙r ∙ (3,3φ°−297 )=10−4 ∙12259,5 ∙25,45 ∙ (3,3 ∙120−297 )=3088,841Nmm
N A=10−4∙ F i ∙ r ∙ (5720−8 ∙φ ° )=10−4 ∙12259,5∙25,45 ∙ (5720−8 ∙120 )=5835,52Nmm
Mψ=M A+N A ∙ r (1−cosφ )−Fi ∙ r
2(sinφ−cosφ )=12757,01Nmm
Nψ=N A ∙ cosφ+F i ∙ r
2( sinφ−cosφ )=5455,63Nmm
KM=1
Eb=0,115 ∙106N /mm2
E=0,21∙106 N /mm2
hb=de−d i2
=9,1mm
K N=1
1+Eb ∙hbE+hp
=0,851mm
M p=KM ∙ Mψ=12757NmmN p=K N ∙ Nψ=4645Nmm
σ e=[2 ∙M p ∙6 r+hp
hp (2 r+hp )+N p] ∙ 1lb ∙ hb=116,91MPa
σ i=[−2 ∙M p ∙6 r−hp
hp (2 r−hp )+N p] ∙ 1lb ∙ hb=−15,228MPa
15
Compresiune
N 'A
Fc=0,003 pt φ=120°=¿N '
A=0,003 ∙ Fc=410,638Nmm
M 'A
r ∙ Fc=−0,0011 pt φ=120 °=¿M '
A=−0,0011 ∙ r ∙Fc=−3831,94Nmm
M 'ψ=M ' A+N 'A ∙ r (1−cosφ )−Fi ∙ rH [( π2−φ) ∙ sinφ−cosφ]=−39773,4Nmm
N 'ψ=N 'A ∙ cosφ+F i ∙ rH [( π2−φ) ∙ sinφ−cosφ ]=1822,876Nmm
M 'p=1 ∙ (−39773,4 )=−39773,4Nmm
N ' p=0,851∙1822,876=1552,023Nmmσ ' e=−210,926MPaσ ' i=96,405MPa
Calcul la fretaj
pf=∆m+∆ t
[ de2+di
2
de2−d i
2+μ
E+
d i2+d❑
2
d i2−d❑
2 −μ
Eb] ∙ d
μ=0,3∆ m=stran gereamecanica=0,006mm∆t=(∝b−∝OL) ∙ di ∙ ( t p−t0 )∝OL=10 ∙10
−6 K−1
∝b=18 ∙10−6 K−1
t p=125 °Ct 0=20 °C
Eb=11,5 ∙104 N /mm2
E=21∙104 N /mm2
∆ t=0,035° C
pf=0,006+0,035
[ 602+41,82
602−41,82+0,3
21 ∙104 +
41,82+362
41,82−362
11,5 ∙104 ] ∙36
=16,04MPa
σ fe=p f ∙2d i
2
de2−di
2=16,04 ∙2 ∙41,82
602−41,82=30,25MPa
σ fi=pf ∙de2−d i
2
de2−d i
2=16,04 ∙362−41,82
602−41,82=3,91MPa
σ max=σe+σ fe=116,92+30,25=147,16MPa
16
σ min=σ 'e+σ fe=−210,926+30,25=−180,678MPa
σ m=σmin+σmax
2=−16,76MPa
ψσ=0,16ε σ=0,8βσ=0,8γ=0,8σ−1 t=360MPa (otel aliat )
σ V=σmax−σ min
2=163,92MPa
cσ=σ−1 t
βσεσ ∙ γ
∙ σV+φσ ∙ σm
= 3601
0,8 ∙0,8∙163,92+0,16 ∙ (−16,76 )
=1,4∈(2,5…5)
Deformatia
f p=9,6 ∙ Fi ∙r
3
105∙ E ∙l b (2 r−d i )3 ∙¿
f p=9,6 ∙12259,5∙25,453
105∙21 ∙104 ∙36 (2 ∙25,45−41,8 )3∙¿
Corpul bieleiSectiunea mica
Fℑ=−mgp ∙R ∙ω2 (1+λ )=−2,1 ∙ 63
1000∙272,2712 (1+0,25 )=−12259,5N
Fℑ=Fgmax−mg∙ R ∙ω2 (1+ λ )=136879,5N
Sm=H i ∙B ∙2+(H p−2H i ) ∙BiSm=34,5∙7,68 ∙2+26,636 ∙7,68=734,67mm
2
σ min=Fℑ
Sm=−12259,5734,67
=−16,69N /mm2
σ max=FcmSm
=136879,5734,67
=186,31N /mm2
Sectiunea mare
Fℑ=−mt ∙R ∙ω2 (1+λ )=−2,6 ∙ 63
1000∙272,2712 (1+0,25 )=−15178,42N
Fℑ=Fgmax−Fℑ=133960,6N
SM=H i ∙B ∙2+(H p−2H i )∙ Bi=765,4mm2
l0=L=250mmσeπ 2E
=0,0002
I z=B H3−
(B−Bi ) (H−2H i )3
12=3293832mm4
17
I y=2H i ∙B
3+(H−2H i) (Bi )3
12=823458mm4
σ max(0) =(1+ σe
π 2E∙l02 ∙ SMI z )∙ Fc mSM =175,53N /mm2
σ max(1) =(1+ σe
π 2E∙li2 ∙ SMI y ) ∙ Fc mSM =179,96N /mm2
σ min=F imSM
=−19,83N /mm2
βσ=1ε σ=0,9ψσ=0,15γ=1,15σ−1 t=360MPa (otel aliat )
cσ(0 )=
σ−1t
βσεσ ∙ γ
∙ σV(0 )+φσ ∙ σ m
(0)= 360
10,9 ∙1,15
∙97,68+0,13 ∙77,85=3,44
cσ(0 )=
σ−1 t
βσεσ ∙ γ
∙ σV(1)+φσ ∙ σm
(1)= 360
10,9 ∙1,15
∙99,9+2,13 ∙80,06=3,36
cσ(0 )−cσ
(1 )=3,44−3,36=0,08≤0,2
Capul bieleiφc=120 °
F i=[mt (1+λ )+mLM−mLC ] ∙ R ∙ωmax2
mt=2,6kgmLM=1,6kg
mLC=13∙mLM=0,6kg
nmax=1,05 ∙2600=2730 rpm
ωmax=π ∙nmax30
=285,885 s−1
¿>F i=[2,6 ∙ (1+0,25 )+1,8−0,6 ] ∙0,063∙285,8852=22913N
M 0=103 ∙F i ∙ lc2∙ (0,83∙ φc−62 )=103 ∙ 22913 ∙88
2∙ (0,83 ∙120−62 )=37907,37Nm
N0=103 ∙ Fi ∙ (792−3 ∙ φc )=103∙22913,06 ∙ (792−3∙120 )=9898,442N
KM=ic
ic−icuz= 3162,53162,5+25,3
=0,992
Sc=hc ∙ lM=10 ∙37,95=379,5mm2
Scuz=hcuz ∙ lM=2 ∙37,95=75,9mm2
18
K N=Sc
Sc−Scuz=0,83
σ ic=KM ∙ M 0
ωc
+KN ∙ N0Sc
=81,19MPa<300MPa
σ c=1,5 ∙F i ∙ lc
3
106 ∙ E (ic+icuz )∙ (φc−90 )2=
1,5∙22913 ∙ (120−90 )2
106 ∙105 ∙2,1∙ (3162,5+25,3 )=0,03≤0,207
9. Arborele cotitD=104mml=130mmd L=190mmd Li=70mm
lL={50mm70mmdM=69mmlM=40mmdM i
=35mmh=30mmb=100mmρ=4mm
Verificarea fusului maneton la presiune si la incalzire
PMmax=RMmaxdM ∙ l 'm
l'm=lm−2 ( ρ+∆ )=40−2∙ (4+0,2 )=31,6mm∆=0,2RMmax=68573,9NRMmin=12263,04N
PMmax=RMmaxdM ∙ l
'm
=68573,969 ∙31,6
=31,45 Nmm2
19
PMmin=12263,0469 ∙31,6
=5,62 N
mm2
K f=¿
W f=10−3 ∙ ζ ∙
π ∙ dM ∙M
60=10−3 ∙1,05 ∙
π ∙69∙260060
=9,86
K f=¿
Verificarea la obosealaFLr=−6094,72N
FMr=−mM ∙R ∙ω2=−2,985 ∙0,063 ∙272,2712=−13940,8N
FBr=−mB ∙ ρB∙ω2=−2,164 ∙77 ∙272,2712=−12352,8N
Fg=0
Zk=12
( z+FMr+FLr )+Fbr+F g
T K=12∙T
MK +1=M K+T (K) ∙R
Verificarea bratuluiM z=zK ∙ a; a=25mmzB=zK−Fg=zKM τ=T K ∙ a
σ=M z
bh2
6
+zBb ∙h
zK max=43266,23N=zB maxzK min=−29518,18N=zBminM z max=1081,656NmM z min=−737,954 Nm
σ max=1081656
100 ∙302
6
+ 43266,23100 ∙30
=86,53 N
mm2
σ max=−737,954100 ∙302
6
+−29518,18100 ∙30
=−59,04 N
mm2
σ m=σmax+σmin
2=86,53−59,04
2=13,74 N
mm2
σ V=σmax−σ min
2=86,53+59,04
2=72,78 N
mm2
cσ=σ−1 t
βσεσ ∙ γ
∙ σV+φσ ∙ σm
= 3502
0,8 ∙0,8∙72,78+0,09∙13,74
=1,53
T K max=30100N
20
T K min=−9764NM τ max=5372,6NmmM τ min=−819Nmm
¿>τmax=603472,6
0,3 ∙100 ∙302=22,35 N
mm2
τ min=−1512230,3 ∙100∙302
=−0,22 N
mm2
τ m=τmax+τmin2
=22,35−0,222
=11,06MPa
τV=τmax−τ min
2=22,35+0,22
2=11,28MPa
cσ=τ−1 t
β τετ ∙ γ
∙ τV+ψσ ∙ τm
= 2202
0,8∙0,8∙11,28+0,09 ∙11,06
=6,06
c Σ=cσ ∙ cτ
√cσ2+cτ2= 1,53 ∙8,01
√1,532+8,012=1,48∈ (1,2…1,5 )
Verificarea fusurilor paliere
τ max=MK max
W p
τ min=MK min
W p
W p=π ∙dL
3
16 [1−( dL idL )4]=π ∙100316 [1−( 70190 )
4]=90757cτ=
τ−1βτε τ ∙ γ
∙ τV +ψσ ∙ τm
∝ (K )=∝1+(720−z ∙ 7206 )Ordinea de aprindere 1-5-3-6-2-4∝(1)=0
∝ (2 )=∝ (1 )+720−4 ∙ 7206
=240
∝ (3 )=∝ (1 )+720−2 ∙ 7206
=480
∝ (4 )=∝ (1 )+720−5 ∙ 7206
=120
∝ (5 )=∝ (1 )+720−1 ∙ 7206
=600
∝ (6 )=∝ (1 )+720−3 ∙ 7206
=360
MK max=3475Nm;M Kmin=−1044,41Nm
21
τ max=347500090757
=38,29MPa
τ min=104441090757
=−11,5MPa
τ m=τmax+τmin2
=38,29−11,52
=13,39MPa
τV=τmax−τ min
2=38,29+11,5
2=24,9MPa
cτ=180
2,51,1∙24,9+0,1 ∙13,39
=3,1
Verificarea fusului manetonM z=0,5 ∙ ZK ∙ l+(FBr−Fg)(0,5 ∙l−a)M T=0,5 ∙T K ∙ lM τ=MK+T K ∙ R
M u=M z ∙cos φu−M T ∙ sinφu
σ max=M umax
W M
σ min=M umin
W M
cσ=τ−1 t
β τετ ∙ γ
∙ τV+ψσ ∙ τm
MUmax=1171000NmmMUmin=−1193000Nmmσ max=16,32MPaσ min=−26,93MPa
τ m=τmax+τmin2
=16,32−26,932
=−5,3MPa
τV=τmax−τ min
2=16,32+26,92
2=21,62MPa
cσ=350
1,90,8 ∙1,4
∙21,62+0,1 ∙(−5,3)=9,68
cτ=τ−1
β τε τ ∙ γ
∙ τV +ψσ ∙ τm
=1,74
c Σ=cσ ∙ cτ
√cσ2+cτ2= 9,68 ∙1,74
√9,682+1,742=1,71∈(1,7 ;3)
22