:536.24(075.8) , ANSYS FLUENT STAR CCM+ , , ISBN
|
|
- Joy Potter
- 5 years ago
- Views:
Transcription
1
2 .. КИК ЧЕЕ ИЕ 07
3 5.56:56.4(075.8) 66 :,,..,,.... :. /....:., ,,,,.,,. ANSYS FLUENT STAR CCM+ ().,.0.0,.0.0,.04.0,.04.0И ISBN , 07, 07
4 ,,,. ( ),.,,.,,, ,, ().
5 .,.,. ( ). TW,.. ( ) w,.,. ( ). Ч (). ( ) (Conjugate eat Transfer CT) []., 4
6 . ().,, Д4].,,., Д 8Ж. []. ANSYS FLUENT STAR CCM+ [5,6].,,,,., 5
7 ( 5, %)., Д4],, :?,., (error, residual),.,.,, (,, ). (...,......,...),.....,.....,
8 .,.... (), w( x, ) T T. w w x x, T T, w (.) (, ),.,.,,, ( ) s.,. (,,, )., () 7
9 ., T T u x, y,, (,).. () (),, (,). T w / x<0,,,.. 8
10 ,,, T w / x>0,..,. ( ): w T, w x, x, T T Nu T T, (.) y w w w L Nu,, L.,,,,.,,,., T w / x=0,..,., T w > T.,,, Nu., Tw < T,,, (.), Nu>0. 9
11 ,,, (.)..,,, s,,.,,,. (.). (.. ) [], 0
12 ,.,.,,,.,,,. :, ;, ; ; ;..., : (, ); (, ); (, ).,,, ( );
13 ,. (, ). (,, ).,.,,. ( ), ( ). (). ( )., [0], ; ;....,,
14 , []: 0 τ ρ j j j j (.) k j k j j jj jk k j j k j j k k j k j k j k j j j k j j k (.4) e j k k j k j k jj k j k j j jk j k j jk j T j j j j j j j e e ρ (.5) : ;,, j ; k ; j
15 ;,, j, jk ; T j ; e.,. (.) (.5) T,,. S, : j j S k jj ( j,, ) (.6) j j k j k k S jk j k k j j k j j k k ( j, k,,; j k) (.7) : 4
16 5 4 p (.8) 4 p (.9) 4 p (.0) (.)
17 6 (.) (.) T ( j e ) j j T j e j T (.4)... : z, r,, (.5) z. : r,,. z, r, u,, w. 0.
18 7 []: 0 r r ur z (.6) ; r r z z p r u z u u zr zr zz (.7) z; rr zr rr r z r r p r z u (.8) r; r z r r r z r w r w z w u (.9) φ;
19 8 r r z u zz 4 (.0) r z u r rr 4 (.) r z u r 4 (.) z r u zr (.) r w r w r r (.4) z w z z (.5) : r r z u p r T r r T r z T z r T z T u c V (.6)
20 9 : r r z u z r u r r z u (.7).4.. :,. 0 y x u (.8) y u x p y u x u u u (.9) y u y T y y T x T u T p c (.0)
21 T T T s s s s c s (.) y s y x s x V y 0, u 0; y, u U, T T ; (.) y 0, T T ; s w T T s. (.) s y y y 0 y 0,, : z 0, u 0, w r z,, w 0 T T,(.4) z=0.,., << L /s /. Bi / s,, 0
22 . (.),.,. : a s T s t T s x w w s V s 0 (.5), w ; V w..5. (.6) T T w w w. (.6),., [,]: w k k d * g x w, k k w w x d w k g w k dx k * k k,(.6) dx k w w
23 * w, g k. * / * w w w (error, residual),. * dp / dx /, W dp / dx ( * ; W ).. g
24 ,,.. * Re u * / ( ). g.. g : = 0,; 0,0;,0; 4 0,0 ( Re * =0, 0 4, 0 5 )
25 w x g x w g w g x w 0 x 0 u t 0 x x g g w 0 u u xt w x (.7) 4 u / x, Д]. g ki 4. g ki u / x : Pr=.0; g ; 0 g ; g ; 4 0 g 0 4
26 ,,,,.,,,.,,..., (.6) (.7),. (.6,.7),. [,4,8], ( ).,,,.,. []. 5
27 ,,.,., (.6), : d T w s g x Bi y w, (.8) dx / y 0. (.8), Bi Bi 0,, ( ).,, d (.8), w. dx, ( ),,. 6
28 ( Bi 0) :,, ( ),.,,.,,,,..,.. ДЖ / Br Pr Re, [8Ж x s Br s / Pe.6..,, :. a s T T s s x * s w g 0 x u w 0, (.9), w. V 7
29 , w T s. a s T s * x >> g 0 u s w T s >> x g 0 Nu * Pe c p c s s w, (.40) (.40), Nu * Pe cp / s c s, [Ж.. Lu c p / s c s. (.40) T s >> L g 0 Nu * Pe Lu w, (.4),. 8
30 ,, (.4),,. L /,.,,, ( ).. (Ni 90%, Cr 0%) =,7/( ), =0,004 L / =00 (Pr=0,7) (Pr=0,0074). t 00 o C u,0 /. t 00 o C u 0, /., 5. L Nu *. g Lu 0 Pe, 4,,0 04 0, 64.,.. 5,8 0,0Re Pr 0, 8 Nu * 0, Re 0,5 Pr 0, Nu * Д4]. 9
31 y y t a t dy y u t t x (.) a c p /, p c,,. : / y y u u y d y c y b a w T T (.) (.) (.), : y T w y T w w y w w s (.)
32 z 0, w z z, (.4) s T 0.,, y, : d 4 a z u, / (.5) 0 dx ( z) z 4z 4 z T,, z 0 (.5) : d dx 0a T (.6) z z 4 Pr (.6) [,]: Br x Pr m Re n x s
33 Nu x Nu x * 0,Br x Br <,5; x Nu x Nu x * 0,4,66 Br, 5(.7) Nu x x * Nu 0, Re 0,5 Pr / x * x... d T dt r r T T dy ar, (.8) dr 0 dy y0 5. r Д]
34 49 y y r r, 60, 5 (.9) w w y y, w y w, (.0) T w T T T b, b, T b b const. (.0) : y T, T Tb, 0; (.) y y 0, s, y y, (.) w y, 0, (.), z, w, T z z / s / T.
35 (.9) (.0) (.8), k T / []: d k a Br k r r dr k Br 49 0 (.4) Br 0 S. / / (.4) : k 0,908 Pr /, Br 0 0. Nu 0,47Re / Pr / r, r, (Pr=0,7) Д7] ( 6%). Nur r /, Re r /, r. (.4) Br 0 k / 0,908 Pr / z, (.5) 4
36 Nu 0.47Re / Pr / / r, r z (.6) (.6),., T T w T T b z ( z). T ДЖ..., T c c. u. u a,, (.7) x y 5
37 T T 0, T 0, T c. 0, x >0, y >0 c T c T 0 (.8) x 0, >0, y >0, =0 (.9) ( T s ) (.5) (.7) y=0,τ>0, x>0, r s ( ), (.0) y r c /. s s (step) [5]: 6
38 T T W c T T 0 c step u exp erf [ ] erf, (.) 0, u., u x / au / r ; x []; c ax/u erf t ) dt [7]. 0 ; exp( Q w step w ( T c T0 ) u /( ax) : 0,, Q (.) w step exp erf, exp erf (ramp) 7
39 T T W c T T 0 c ramp, exp( ) erfc[ ] i erfc[ ] i erfc[ ], (.) T T exp( ) erfc[ ] i erfc[ ] W c, (.4) T T 0 c ramp i erfc[ ]. ;, erfc[ ] erf [ ] i erfc[ ] erfc( t) dt, : erfc( t) dt exp( ) erfc[ ]. exp Q w ramp T W T c T 0 T c step T W T c ramp, (.5) T 0 T c. 8
40 Q w ramp exp erf erf T T W c T T 0 ramp c ( ), (.6). (Quasi steady Q.s.) (.) (.) : Q. s. T T W c T T 0 c step exp( ) erf erf (.7) Q Q. s. exp exp erf erf w step (.8) 9
41 ,. Ж.,.., ( ): w T T w T T w ( T T ) Bi / Bi, (.) Bi T w, T, T ;, ; Bi / s, Bi / s ; ; s. Nux 0, Pr / Re /, x Nux 0,095 Pr 0.4 Re 0.8 (.) x 40
42 ., Bi D x n, Bi D x m. dbi Bi dbi ( / Bi ) dx n n m Bi dx Bi g x g Bi Bi / Bi (.) Bi Bi gn n x D D D / D m x g n m n x D / D D m x D / D x m (.4) (.4), x 0 max n, m 0; g n m 0, m 0 g n max max n (.5), n 0, m 0, 4
43 , n, m 0. max max g / max g /5. Pr>0.5 g 0,6 ( ). max 0%. g =0, ( ) max =4%., Pr=0,0 g =0,5 max =0%.,, ( Pr>0.5).,, 0 5%; 7% []. Д],,.,, max.. (Ni 90%, Cr 0%) =,7/( ), s =0,04 L =0,4.. 4
44 t 0 o C u 0, 5/,, ; t 50 o C u 0, /.,,, x=0,.. 0,5 u D 0, Pr 0, n m 0, 5. s D =0,67( 0,5 ), D =0,0( 0,5 ), =,%.. t 00 o C u 0 / ;,, t 00 o C u 50 /.,,. D =0,046( 0,5 ), x=0, =%. D =0,0( 0,5 ). 4.,.. =56,8% x=0,. 5.,.. x=0, =4,7%. 4
45 ..,, ( x 0) ( 0), w ( x L) T w. T T x w w ch( Bi ) T (.6) T w ( L) ch( Bi) L (.6) : x d x x g w g Bi th Bi, (.7) w dx L L ( g =0.6, Re ) x L Bi =.64, (.7) max =00%.,,, 00%. 44
46 .. w, (.8) w / / w. F / F ;.. F F c ze ;. F F... z ; F.. F zfp ; F p ; F ; c ;, E. : Bi ; s Bi c c s. Bi ; : Bi c D x k 4, Bi, c Bi. s Bi. F Bi c D x k D,. F
47 F F Ez p Bi D.,,..... Bi Bi F c F Bi Bi k n Bi n g (.9) (.9), k x D F c F D k x D D n x nd g 5.. / 4 / + + / D n x k x F c F D D F c F D k x D F F D k n g (.0)
48 , n, k 0,... g n x 0. max n 0; k 0,,, max,.. g n x 0. max 6. Д.5, 4].. (.9) g n Bi. Bi n k Bi. Bi Bi. F c F.. 0,6,55 0,5 5,5 0,5 0,479 6,6 085, =6,7%.. 0, 0,5 0,5 0, Pr,5 L Re Pr Re Pr Nu L L, w u u L Re, Re L, L 47
49 . 0 <Re L <, , (.) w T T, w, () T T,, ; T T,., T T,,,. T.,,, d x w w dx d x x d dx g g (.) dx w w 6, 48
50 M=0,5 M=0,68. M ( u ) /( u ) ( ) ( ). M=0,5 0,68 DR = ρ/ρ = 0,95 ( R / d =47, R, d ), ( R / d = 44,5), []. =0 ( ) P/d=. 6., M=0,6.,,.,, 49
51 . M=.0, ( 7). 7.,. ( 8 9). 8., 50
52 =0, ( 9). 9., ( 8 9),. M =, M =,7 x x / d = 6 5. D x l 6, l >0 ( 6 7) l <0 ( 8 9). l M x / d. (.), : Bi D x n D x l 6 5
53 5 w nbi w dx dbi x dx w d x ; l dx d x, w w w l w nbi g w w dx w d x w dx d x g (.), / Bi Bi, (.) n x D l x D n x D l x D l x D n x D l n x D l x D n x nd g = = D n x n x D D n x n l x D D D n x n x l D n x n x D n l x nd g (.4)
54 x 0 n >0 l g l max n >0; g n max n >0 l n <0 (.5) 7., ( 0). L 5 h =,0,5 Д6Ж. d =0,8,, P / d =,5,0. L.5,0. 0. ( ) 5
55 =0 0 P / d =. ( g =0,; n=0,).. (.). l, 7, M=,05 DR=,0: l ln ln ln x lnx =0,. 5 0,8. L / d =8,7. : =0, =0,5. w Bi = 5,0 [6].,, x = 8,7: l w nbi g w w w =5,8%. 0, 5,0 0,5 0,78 0, 0,5 0, 0, 0, 0,5 0,5 0, ,5. x / d =40. : =0, =0,. w Bi =,0 [0]. 54
56 . l, 8, M=, DR=,0: 0,5. l w nbi g w w w =,% l ln ln ln x lnx 0,,0 0, 0,88 0,5 0,7 0, 0, 0, 0, 0, 0, =.5.,, : g x w 0 u w (.6) g 0 ( 4), u. d i erfc x / dx erfc x :, 55
57 erfc erfc i erfc i erfc ramp g 0 erfc (.7) ramp g 0 erfc erfc erfc i erfc i erfc[, (.8) ]. Q.s. step Q. s. step g 0 erf erf exp (.9) (.9),. 9. Q.s.. step 50% Ni 50% Fe,75, L =76,, =0,. 56
58 (,9,5). 0 5,6, Pr,. : Re,0 5 ( ) L ( ).. : Re L Re L,45 0 6,0 5. 0, 8 4 g =,. Д4] : 0 995,9 /, 0, 687 /(), 450 /(), p,5 0 7 /, a, /. 50% Ni 50% Fe : 8900 / s, 40 /(). s Nu L / 0,664Re 0,5 Pr 0, 4, 6; L c L Lu c p /( s c s ),09 ; Nu L / =0,09. Pe L =0,66, erf(0,7)=0,695 erf(0,66)=0,67 (. 7). Q.s. (.9): step Q. s. step g 0 exp, 0,09 erf erf 068 0,597 0, = 6%, 5 Q.s. =6,%. step 57
59 0. : Re L, , 8. Nu L / 0,07 Re 0,8 Pr 0,4 48; L c L Nu L / Pe L =,54 =0,0. erf(,564)=0,97 erf(,54)=0,967 (. 7). Q.s. (.9): step Q. s. step g 0 exp, 0,09 erf erf 004 0,009 0, =,6% Q.s., step Д8] 0, 8.. ramp,., >, 9, : =0,66 =0,09. =0,8 =,0. 0, <. (.7) =0, : 58
60 erfc(0,66)= erf(0,66)=0,7; erfc(0,6578)= erf(0,6578)=0,55; i erfc(0,66) =0,94; i erfc(0,6578) =0,6; erfc 0,66 =0,008. 0,7 0,55, 0,09 ramp 0,008 0, 0068 =7%. erfc :.,. =5 (.8), >. =0,8. 4,.. : erfc ( ) = erfc(,098); erfc(,007)= 0,57; i erfc(,098) =0,06; i erfc(,007) =0,0506; erfc 0,66 =0,707. 0,57 0,,4 0,09 ramp 0,707 0,06 0, 0506 =5,7%. erfc : 59
61 : ;, [4,7].,.,,...,. : ()., ( ).,. 60
62 . s, : T W T s Y Y T s s / s, (4.) Y Y s W, ; Y Y, s. (4.)..,..,. ; (),.,.,,,.,, 6
63 ,,,... Д7]:, ;,,.,,,,,. 4.. STAR CCM+ STAR CCM+ [6],. STAR CCM+, (),. ABAQUS STAR CCM+. 6
64 STAR CCM+ ABAQUS. ABAQUS STAR +...,.. [6].,.. (); (),, 00. 6
65 In place interface,,. Air interface Solid interface Type contact interface Interface. STAR CCM+ (.,),,.,.. STAR CCM+ 64
66 ,..,. 4.. ANSYS FLUENT. ANSYS FLUENT [5] ( 4,).,, (mixed). ( STAR CCM+) (Fluid Solid) GAMBIT.4.6, 65
67 , (wall), (wall shadow) ( 4,)., Coupled. 4. (); () 4.. 0,5 0,0 0 / ,. Ч. 900 GAMBIT.4.6. y yu / *, u / * w. 5, y = 0,46. 66
68 5. (); : Д Ж,, () : Velocity inlet=0 /, Gauge pressure outlet=0. Second Order Upwind. Coupled. k RNG. 5, ( ), ( ).,, 5,. ( 6),. ДЖ,,,. (). 6, 67
69 () x > 0, ДЖ 6,. 68
70 4.4.,.,, ( 5) 0 4 ( ), ( 0 ).,,. Д]: u Y a 00, s s 0. 5, (4.) ( Y ) s, s,., Y = Y s =0,00.,, 00/, s / 00., 69
71 ,.,,.,. STAR CCM+ Simulation, ( 7). Implicit Unsteady model,, T T 00 0 ( 8). c Field Functions Tools C *$ Time 00 0*$Time. Restart,., s Implicit Unsteady model. 7 C++ : ($Time > = 0.0)? 000: *$Time. =0,
72 , >0, , ( 8)., / ( 9,)
73 ;. 0,4 0,04. 50% Ni 50% Fe : 8900 / s, 40 /(). s , Y + =0,6.. =0, =0, s 8. 9., 7
74 5, (); (),. (.7), 0 : ramp g 0 exp, ramp %. 7
75 5. 5..,,,,..,. Д9,0Ж,,,,...,,,., ,88 0,99,4,6 0,6 74
76 , 664 Q = ): d. =50 (, Q ,8( /. ) F.. 0,99,. Q 000 4, ( / ) ( / 4), d., [Ж 664 ( 0) 9/0 SEMIKRON
77 ё ё (, ). GAMBIT ё. Z Y X ё / ) (. 664: ( ); ( ) Д9Ж,, ANSYS FLUENT. (, ), 76
78 ( ). ( 40 ).,, , /. 77
79 0 (. ),,.. ё 664 u (/) R / T RNGKE 0, 0,87 RNGKE P 0, 0,8 RNGKE DO 0, RNGKE,0 0,8 5 SKE,0 0,097 6 RNGKE P,0 0,096 7 RNGKE DO,0 0,8 8 RNGKE P,5 0,079 9 SKE 5,0 0,058 0 RNGKE 5,0 0,065 RNGKE k ε RNG, SKE k ε. P DO Д5]. R T T Q T max /, 78
80 () Q., ё k ε RNG DO ( ).. ё 664 9/0 SEMIKRON ( 000 ).,,, ( ). 79
81 5.., ( ),,.,.,, Д0Ж,. ( ) Д0], d=0,4, P ( 4, ). P/d=,,5, : 4,7 7,
82 ( 70) () (), P/h=0. h 0.4, 0...,,., d =,,. d =. 8
83 ,, , d, 0,4 0,4 0,4 0,4 0,4 0,4 0,4 0,4, t/d,5 4,67 4,67,, 4,67 4,67,8,66,84,87,87,87,87,86,8, DR, M,,8,,95,0,98,0,4 0,88, 64C, 0%, 0,68. I V 0,5; 0,09; 0,0; 0,; 0,80 (90,, 5, 99, 54)C, 0%. (D),.,,. (, ANSYS FLUENT, STAR CCM+) D ( 8
84 ),,,.. Unigraphics NX. 5. Cyclic. 0,8,8. Stagnation ( P* = 0,88, T* = 887, 47, Tu=0%, L= ). Mass Flow Inlet ( 64,6%, 0,5%, 6,9%, 8%, T* = 45, Tu=%, Turbulent Viscosity Ratio ( t / 0). Pressure Outlet ( P = 0,68 )., (In Place). ( Д0]). 8
85 ( ). 5. : (); () STAR CCM+. (. 4).,,. 4 84
86 Y +,0 ( 6). 4.,. Y + Coarse mesh,8,4, Fine mesh 9,5 5,0 4, Finer mesh 8,6,9 6, Finer mesh,5 5, 8, (),, Cp=Cp(T) ( ),, Д6]. 85
87 8760 /, 90 /(),. 6. 4: (); () 86
88 ,. Д9]. : VF ally +, SST ally +, RKE ally +, SST swf, KE swf. (standard wall function swf), «ally +», Y +.,..., Y +,. Segregated,..,.. 9,5. 8,5.,..,,7 48, ,5,5,..,, ,5. 87
89 4 4 ( 7 ). : ( 0 5 ),, ( );, ;,. ( 5). 5., Y+ [ ]. k SST all Y+,8 00 9,5 0 8,5 5,5 4 4 RKE all Y+, , , ,5 8 8 VF,5 9 9 k SST swf, KE swf,8 00 k SST LowRe Re,5 0 88
90 .,8.,,5. ( 4). (,5 ), 6.,,5.,% ( ) ( T * * * T ) /( T T ).,. 7,,% T,,,. 7,,,%,. 5%,, T.,,, RKE.,8. Y + = 00. (SST, VF) 5%, (0 5)%. 89
91 7. : (), (), (), (): SST all Y + (, ), RKE all Y + (, ), VF (, ), SSTsWF ( ), KWsWF ( ), SST LowRe γ Re ( ). ( 8,). 8,, 50., ( 8,). 90
92 8. (); (); () 9., ( 4).,,, D,. ( ),, D. 9
93 T, C Экеие L :, D, D, 4 D 0,, ,. 0 40,
94 0. : (,); RKE (realizable k ),,5.. 9
95 5.., ( Д9Ж ),..,..,. () 94
96 . ( ). ANSYS FLUENT, (). (),, Д9].. ( ; ; ; 4 ; 5 ) (); () 95
97 (,): (),,, (5). (,). ( ).,,,,.,,., ( A, ) (,,)., elocity inlet (,), [7]. (,), S/h 0,4, S, h. 96
98 . (); () (,, ), 0 0.,, ( 4).,.,,.,, 97
99 .,. ( ). ANSYS FLUENT 4.0 [5]. ( ). 4. (); ( ) ();,, ANSYS Gambit.4.6. STEAM, ANSYS FLUENT 4.0 UDF (user defined function),. SST k ( ). 98
100 , Re, r r / i, G =.9 07, D c Re =. 0 4, r,,. D c G ( ) Re G D =.0 0 4,, i, D G,, t , Re i, ( 4). (D ).,. M =0, ( 4,). []. 99
101 ,, ( 4,).., n=000/.,, 5 ( 5,). 5. (): (,, ); ():, 00
102 ,. 5,., 0 0. Д9Ж,, ( 4,).,,. 6, ( % %) ANSYS FLUENT t, 0 C
103 6. ( leel or effect of conjugation ),,.,.,, : ( ).,,,. ( ) ;,. Bi Bi 0,, ( ).,,.,, : 0
104 ()., ; :, ( ); : ( ), ; :, ; :,.,. ( ),,. (Computational Fluid Dynamics CFD). () 0
105 ,.,. ( ) ( 4).,,, ( 5),., ( 5, %). 04
106 7.. Conjugate Problems in Conectie eat Transfer/Dorfman A. Sh. Taylor & Francis Group, LLC. London New York p..,.. /..,..,... :., c..,.. /.....:, ,.. /.. :, ,.. /..,... :, ,.. /....: c. 7.. /..,..,...;.....: :..:, ,..,....: ,.. :....,..: : :. 06. c. 05
107 ..., :.. (.)..:...IV 9/..,..,...: ,..... /....: User Guide ANSYS FLUENT ersion 4.0. USA STAR CCM+ Documentation. CD adapco. Version pp. 7.,..,....: /..,..,..,...: ,....: :.., , ;., ,..,
108 ..., :.. /..: Sucec J. Unsteady heat transfer between a fluid with time arying temperature and a plate: an exact solution//international Journal eat Mass Transfer. Vol pp /..,..,..,..... : ,...:. (... ) /..: ,.... (9) ,..,
109 8. 7 [7]. Итр x x t e dt 0 x (x) x (x) x (x) x (x) x (x) x (x) 0, 0, 0, 0, 0, 0, 0, , ,0 86 0, , , , ,0 70 0, , , , ,0 46 0,5 76 0, , , , , ,0 86 0, , , ,
110 7. р x (x) x (x) x (x) x (x) x (x) x (x) 0, 0, 0, 0,9 0,9 0,9 0,9 8088, 885, 9606,5 678,7 844, , ,5 896,5 9476,55 76, , , ,0 90,40 959,60 765, , , ,5 990, ,65 808,85 9, ,0 880,0 940,50 966,70 879,90 979,
111 7. р x (x) x (x) x (x) x (x) x (x) x (x) 0,99 0,99 0,99 0,99 0,99, 755,6 8607,4 946, ,7 987, ,5 769,0 8857, , , , ,0 87,5 9,50 959,65 98,80 995, ,5 857,40 9, , , , ,99 0,99 0,99 0,99 0,99 0,99 0
112 ,
113 ,4,5 4.., , STAR CCM ANSYS FLUENT
114
115 Крт 005 9,.; / , Л.,,. 955,,., 9..: (8) ;
CHAPTER 7 NUMERICAL MODELLING OF A SPIRAL HEAT EXCHANGER USING CFD TECHNIQUE
CHAPTER 7 NUMERICAL MODELLING OF A SPIRAL HEAT EXCHANGER USING CFD TECHNIQUE In this chapter, the governing equations for the proposed numerical model with discretisation methods are presented. Spiral
More informationCFD in Heat Transfer Equipment Professor Bengt Sunden Division of Heat Transfer Department of Energy Sciences Lund University
CFD in Heat Transfer Equipment Professor Bengt Sunden Division of Heat Transfer Department of Energy Sciences Lund University email: bengt.sunden@energy.lth.se CFD? CFD = Computational Fluid Dynamics;
More informationComputational fluid dynamics study of flow depth in an open Venturi channel for Newtonian fluid
Computational fluid dynamics study of flow depth in an open Venturi channel for Newtonian fluid Prasanna Welahettige 1, Bernt Lie 1, Knut Vaagsaether 1 1 Department of Process, Energy and Environmental
More informationInvestigation of reattachment length for a turbulent flow over a backward facing step for different step angle
MultiCraft International Journal of Engineering, Science and Technology Vol. 3, No. 2, 2011, pp. 84-88 INTERNATIONAL JOURNAL OF ENGINEERING, SCIENCE AND TECHNOLOGY www.ijest-ng.com 2011 MultiCraft Limited.
More informationParallel Plate Heat Exchanger
Parallel Plate Heat Exchanger Parallel Plate Heat Exchangers are use in a number of thermal processing applications. The characteristics are that the fluids flow in the narrow gap, between two parallel
More informationCalculations on a heated cylinder case
Calculations on a heated cylinder case J. C. Uribe and D. Laurence 1 Introduction In order to evaluate the wall functions in version 1.3 of Code Saturne, a heated cylinder case has been chosen. The case
More informationNumerical Modelling of Twin-screw Pumps Based on Computational Fluid Dynamics
Numerical Modelling of Twin-screw Pumps Based on Computational Fluid Dynamics 6-8 th March 2017 Dr Sham Rane, Professor Ahmed Kovačević, Dr Di Yan, Professor Qian Tang, Centre for Compressor Technology,
More informationThe Meaning and Significance of Heat Transfer Coefficient. Alan Mueller, Chief Technology Officer
The Meaning and Significance of Heat Transfer Coefficient Alan Mueller, Chief Technology Officer The Meaning of Heat Transfer Coefficient I kno the meaning of HTC! Why should I aste my time listening to
More information5. FVM discretization and Solution Procedure
5. FVM discretization and Solution Procedure 1. The fluid domain is divided into a finite number of control volumes (cells of a computational grid). 2. Integral form of the conservation equations are discretized
More informationHEAT TRANSFER BY CONVECTION AND CONDUCTION FROM THE FLUID MOVING AT SOLID WALLS
HEAT TRANSFER BY CONVECTION AND CONDUCTION FROM THE FLUID MOVING AT SOLID WALLS Associate Professor Ph.D. Amado George STEFAN, Lt.Eng., doctoral student Constantin NISTOR MILITARY TECHNICAL ACADEMY Abstract.
More informationDEVELOPED LAMINAR FLOW IN PIPE USING COMPUTATIONAL FLUID DYNAMICS M.
DEVELOPED LAMINAR FLOW IN PIPE USING COMPUTATIONAL FLUID DYNAMICS M. Sahu 1, Kishanjit Kumar Khatua and Kanhu Charan Patra 3, T. Naik 4 1, &3 Department of Civil Engineering, National Institute of technology,
More informationLaminar Flow. Chapter ZERO PRESSURE GRADIENT
Chapter 2 Laminar Flow 2.1 ZERO PRESSRE GRADIENT Problem 2.1.1 Consider a uniform flow of velocity over a flat plate of length L of a fluid of kinematic viscosity ν. Assume that the fluid is incompressible
More informationDischarge Coefficient Prediction for Multi hole Orifice Plate in a Turbulent Flow through Pipe: Experimental and Numerical Investigation
Discharge Coefficient Prediction for Multi hole Orifice Plate in a Turbulent Flow through Pipe: Experimental and Numerical Investigation [] Mahendra Babu.K.J, [2] Dr. Gangadhara Gowda C.J, [3] Ranjith
More informationApplied CFD Project 1. Christopher Light MAE 598
Applied CFD Project 1 Christopher Light MAE 598 October 5, 2017 Task 1 The hot water tank shown in Fig 1 is used for analysis of cool water flow with the heat from a hot plate at the bottom. For all tasks,
More informationEffect of radius ratio on pressure drop across a 90 bend for high concentration coal ash slurries
This paper is part of the Proceedings of the 11 International Conference th on Engineering Sciences (AFM 2016) www.witconferences.com Effect of radius ratio on pressure drop across a 90 bend for high concentration
More informationTutorial for the supercritical pressure pipe with STAR-CCM+
Tutorial for the supercritical pressure pipe with STAR-CCM+ For performing this tutorial, it is necessary to have already studied the tutorial on the upward bend. In fact, after getting abilities with
More informationConjugate Heat Transfer Simulation of Internally Cooled Gas Turbine Vane
Conjugate Heat Transfer Simulation of Internally Cooled Gas Turbine Vane V. Esfahanian 1, A. Shahbazi 1 and G. Ahmadi 2 1 Department of Mechanical Engineering, University of Tehran, Tehran, Iran 2 Department
More informationOPTIMAL DESIGN OF CLUTCH PLATE BASED ON HEAT AND STRUCTURAL PARAMETERS USING CFD AND FEA
International Journal of Mechanical Engineering and Technology (IJMET) Volume 9, Issue 5, May 2018, pp. 717 724, Article ID: IJMET_09_05_079 Available online at http://www.iaeme.com/ijmet/issues.asp?jtype=ijmet&vtype=9&itype=5
More informationStudies on flow through and around a porous permeable sphere: II. Heat Transfer
Studies on flow through and around a porous permeable sphere: II. Heat Transfer A. K. Jain and S. Basu 1 Department of Chemical Engineering Indian Institute of Technology Delhi New Delhi 110016, India
More informationRANS-LES inlet boundary condition for aerodynamic and aero-acoustic. acoustic applications. Fabrice Mathey Davor Cokljat Fluent Inc.
RANS-LES inlet boundary condition for aerodynamic and aero-acoustic acoustic applications Fabrice Mathey Davor Cokljat Fluent Inc. Presented by Fredrik Carlsson Fluent Sweden ZONAL MULTI-DOMAIN RANS/LES
More informationPERIODICALLY FULLY DEVELOPED LAMINAR FLOW AND HEAT TRANSFER IN A 2-D HORIZONTAL CHANNEL WITH STAGGERED FINS
THERMAL SCIENCE: Year 2017, Vol. 21, No. 6A, pp. 2443-2455 2443 PERIODICALLY FULLY DEVELOPED LAMINAR FLOW AND HEAT TRANSFER IN A 2-D HORIZONTAL CHANNEL WITH STAGGERED FINS by Oguz TURGUT a* and Kamil ARSLAN
More informationIntroduction to Heat and Mass Transfer. Week 8
Introduction to Heat and Mass Transfer Week 8 Next Topic Transient Conduction» Analytical Method Plane Wall Radial Systems Semi-infinite Solid Multidimensional Effects Analytical Method Lumped system analysis
More informationTABLE OF CONTENTS CHAPTER TITLE PAGE
v TABLE OF CONTENTS CHAPTER TITLE PAGE TABLE OF CONTENTS LIST OF TABLES LIST OF FIGURES LIST OF SYMBOLS LIST OF APPENDICES v viii ix xii xiv CHAPTER 1 INTRODUCTION 1.1 Introduction 1 1.2 Literature Review
More informationFLOW SIMULATION AND HEAT TRANSFER ANALYSIS USING COMPUTATIONAL FLUID DYNAMICS (CFD)
PERIODIC FLOW SIMULATION AND HEAT TRANSFER ANALYSIS USING COMPUTATIONAL FLUID DYNAMICS (CFD) *M.SNEHA PRIYA, **G. JAMUNA RANI * (Department of Mechanical Engineering, koneru lakshmai University, Guntur)
More informationCOMPUTATIONAL FLUID DYNAMICS ANALYSIS OF A V-RIB WITH GAP ROUGHENED SOLAR AIR HEATER
THERMAL SCIENCE: Year 2018, Vol. 22, No. 2, pp. 963-972 963 COMPUTATIONAL FLUID DYNAMICS ANALYSIS OF A V-RIB WITH GAP ROUGHENED SOLAR AIR HEATER by Jitesh RANA, Anshuman SILORI, Rajesh MAITHANI *, and
More informationHeat Transfer Modeling
Heat Transfer Modeling Introductory FLUENT Training 2006 ANSYS, Inc. All rights reserved. 2006 ANSYS, Inc. All rights reserved. 7-2 Outline Energy Equation Wall Boundary Conditions Conjugate Heat Transfer
More informationreport: Computational Fluid Dynamics Modelling of the Vortex Ventilator MK4 Rev 2 Ventrite International
report: Computational Fluid Dynamics Modelling of the Vortex Ventilator MK4 Rev 2 PrePAreD for: Ventrite International D O C U men t C O N trol Any questions regarding this document should be directed
More informationComparison of Flow and Sedimentation Pattern for three Designs of Storm Water Tanks by Numerical Modelling
Comparison of Flow and Sedimentation Pattern for three Designs of Storm Water Tanks by Numerical Modelling 9th International Conference on Urban Drainage Modelling, Belgrad 2012 Simon Ebbert Nina Vosswinkel
More informationTurbulence Modeling of Air Flow in the Heat Accumulator Layer
PIERS ONLINE, VOL. 2, NO. 6, 2006 662 Turbulence Modeling of Air Flow in the Heat Accumulator Layer I. Behunek and P. Fiala Department of Theoretical and Experimental Electrical Engineering Faculty of
More informationEFFECT OF ROTOR S ANGULAR SPEED AND ASPECT RATIO ON ENTROPY GENERATION IN A ROTOR-CASING ASSEMBLY
Third International Conference on CFD in the Minerals and Process Industries CSIRO, Melbourne, Australia 1-1 December 3 EFFECT OF ROTOR S ANGUL SPEED AND ASPECT RATIO ON ENTROPY GENERATION IN A ROTOR-CASING
More informationNumerical simulation of fluid flow in a monolithic exchanger related to high temperature and high pressure operating conditions
Advanced Computational Methods in Heat Transfer X 25 Numerical simulation of fluid flow in a monolithic exchanger related to high temperature and high pressure operating conditions F. Selimovic & B. Sundén
More informationLast 4 Digits of USC ID:
Chemistry 05 B Practice Exam Dr. Jessica Parr First Letter of last Name PLEASE PRINT YOUR NAME IN BLOCK LETTERS Name: Last 4 Digits of USC ID: Lab TA s Name: Question Points Score Grader 8 2 4 3 9 4 0
More informationCFD Analysis of Forced Convection Flow and Heat Transfer in Semi-Circular Cross-Sectioned Micro-Channel
CFD Analysis of Forced Convection Flow and Heat Transfer in Semi-Circular Cross-Sectioned Micro-Channel *1 Hüseyin Kaya, 2 Kamil Arslan 1 Bartın University, Mechanical Engineering Department, Bartın, Turkey
More informationCFD Analysis for Thermal Behavior of Turbulent Channel Flow of Different Geometry of Bottom Plate
International Journal Of Engineering Research And Development e-issn: 2278-067X, p-issn: 2278-800X, www.ijerd.com Volume 13, Issue 9 (September 2017), PP.12-19 CFD Analysis for Thermal Behavior of Turbulent
More informationExternal Forced Convection :
External Forced Convection : Flow over Bluff Objects (Cylinders, Spheres, Packed Beds) and Impinging Jets Chapter 7 Sections 7.4 through 7.8 7.4 The Cylinder in Cross Flow Conditions depend on special
More informationHeat Transfer Modeling using ANSYS FLUENT
Lecture 2 - Conduction Heat Transfer 14.5 Release Heat Transfer Modeling using ANSYS FLUENT 2013 ANSYS, Inc. March 28, 2013 1 Release 14.5 Agenda Introduction Energy equation in solids Equation solved
More information6.2 Governing Equations for Natural Convection
6. Governing Equations for Natural Convection 6..1 Generalized Governing Equations The governing equations for natural convection are special cases of the generalized governing equations that were discussed
More informationA concept for the integrated 3D flow, heat transfer and structural calculation of compact heat exchangers
Advanced Computational Methods and Experiments in Heat Transfer XIII 133 A concept for the integrated 3D flow, heat transfer and structural calculation of compact heat exchangers F. Yang, K. Mohrlok, U.
More informationJ.P. Holman: 3.09) T sur := Use table 3-1 to determine the shape factor for this problem. 4π r S := T sphere := 30K r 1. S = m k := 1.
.P. Holman:.09) T ur : 0 Ue table - to determine the hape factor for thi problem. D :.m r : 0.5m π r S : T phere : 0 r D S 7.0 m :.7 m Ue eq. - to calculate the heat lo. q : S T phere T ur q 57.70 .P.
More informationTutorial for the heated pipe with constant fluid properties in STAR-CCM+
Tutorial for the heated pipe with constant fluid properties in STAR-CCM+ For performing this tutorial, it is necessary to have already studied the tutorial on the upward bend. In fact, after getting abilities
More informationLaminar flow heat transfer studies in a twisted square duct for constant wall heat flux boundary condition
Sādhanā Vol. 40, Part 2, April 2015, pp. 467 485. c Indian Academy of Sciences Laminar flow heat transfer studies in a twisted square duct for constant wall heat flux boundary condition RAMBIR BHADOURIYA,
More informationANALYSIS OF HEAT AND MASS TRANSFER OF THE DIFFERENT MOIST OBJECT GEOMETRIES WITH AIR SLOT JET IMPINGING FOR FORCED CONVECTION DRYING Doğan Engin ALNAK a, Koray KARABULUT b* a Cumhuriyet University, Technology
More informationCFD modelling of multiphase flows
1 Lecture CFD-3 CFD modelling of multiphase flows Simon Lo CD-adapco Trident House, Basil Hill Road Didcot, OX11 7HJ, UK simon.lo@cd-adapco.com 2 VOF Free surface flows LMP Droplet flows Liquid film DEM
More informationA CFD Analysis Of A Solar Air Heater Having Triangular Rib Roughness On The Absorber Plate
International Journal of ChemTech Research CODEN( USA): IJCRGG ISSN : 0974-4290 Vol.5, No.2, pp 964-971, April-June 2013 ICGSEE-2013[14th 16th March 2013] International Conference on Global Scenario in
More informationTheoretical Study of Forced Convective Heat Transfer in Hexagonal Configuration with 7Rod Bundles Using Zirconia-water Nanofluid
Theoretical Study of Forced Convective Heat Transfer in Hexagonal Configuration with 7Rod Bundles Using Zirconia-water Nanofluid Mojtaba Maktabifard1, a*, Nathanael P. Tian1, b 1 Faculty of Mechanical
More informationCFD Analysis of Mixing in Polymerization Reactor. By Haresh Patel Supervisors: Dr. R. Dhib & Dr. F. Ein-Mozaffari IPR 2007
CFD Analysis of Mixing in Polymerization Reactor By Haresh Patel Supervisors: Dr. R. Dhib & Dr. F. Ein-Mozaffari Introduction Model development Simulation Outline Model Setup for Fluent Results and discussion
More informationNumerical simulations of heat transfer in plane channel flow
Numerical simulations of heat transfer in plane channel flow Najla EL GHARBI 1, 3, a, Rafik ABSI 2, b and Ahmed BENZAOUI 3, c 1 Renewable Energy Development Center, BP 62 Bouzareah 163 Algiers, Algeria
More informationABSTRACT I. INTRODUCTION
2016 IJSRSET Volume 2 Issue 4 Print ISSN : 2395-1990 Online ISSN : 2394-4099 Themed Section: Engineering and Technology Analysis of Compressible Effect in the Flow Metering By Orifice Plate Using Prasanna
More informationFlow field in the compressor blade cascade NACA
Flow field in the compressor blade cascade NACA 65-100 Tomáš Turek Thesis Supervisor: Ing. Tomáš Hyhlík, Ph.D. Abstract An investigation is made into the effects of a flow field in the compressor blade
More informationNPC Abstract
NPC-2013-15002 Development of Mach 3.6 water cooled Facility Nozzle By Jayaprakash C*, Sathiyamoorthy K*, Ashfaque A. Khan*, Venu G*, Venkat S Iyengar*, Srinivas J**, Pratheesh Kumar P** and Manjunath
More informationOptimization of Shell & Tube Heat Exchanger by Baffle Inclination & Baffle Cut
Optimization of Shell & Tube Heat Exchanger by Baffle Inclination & Baffle Cut Joemer.C.S 1, Sijo Thomas 2, Rakesh.D 3, Nidheesh.P 4 B.Tech Student, Dept. of Mechanical Engineering, Toc H Institute of
More informationUnsteady RANS and LES Analyses of Hooper s Hydraulics Experiment in a Tight Lattice Bare Rod-bundle
Unsteady RANS and LES Analyses of Hooper s Hydraulics Experiment in a Tight Lattice Bare Rod-bundle L. Chandra* 1, F. Roelofs, E. M. J. Komen E. Baglietto Nuclear Research and consultancy Group Westerduinweg
More informationSOE3213/4: CFD Lecture 1
What is CFD SOE3213/4: CFD Lecture 1 3d 3d Computational Fluid Dynamics { use of computers to study uid dynamics. Solve the Navier-Stokes Equations (NSE) : r:u = 0 Du Dt = rp + r 2 u + F 4 s for 4 unknowns,
More informationIntroduction to ANSYS FLUENT
Lecture 6 Turbulence 14. 0 Release Introduction to ANSYS FLUENT 1 2011 ANSYS, Inc. January 19, 2012 Lecture Theme: Introduction The majority of engineering flows are turbulent. Successfully simulating
More informationTurbulence Solutions
School of Mechanical, Aerospace & Civil Engineering 3rd Year/MSc Fluids Turbulence Solutions Question 1. Decomposing into mean and fluctuating parts, we write M = M + m and Ũ i = U i + u i a. The transport
More informationNumerical Simulation of the Hagemann Entrainment Experiments
CCC Annual Report UIUC, August 14, 2013 Numerical Simulation of the Hagemann Entrainment Experiments Kenneth Swartz (BSME Student) Lance C. Hibbeler (Ph.D. Student) Department of Mechanical Science & Engineering
More informationCFD Analysis of Mass Flow under Non-Uniformity constraints through Heat Exchanger
International Journal of Scientific and Research Publications, Volume 6, Issue 7, July 2016 300 CFD Analysis of Mass Flow under Non-Uniformity constraints through Heat Exchanger Kirti Onkar Prajapati 1,
More informationCFD ANALYSIS OF TRIANGULAR ABSORBER TUBE OF A SOLAR FLAT PLATE COLLECTOR
Int. J. Mech. Eng. & Rob. Res. 2013 Basavanna S and K S Shashishekar, 2013 Research Paper ISSN 2278 0149 www.imerr.com Vol. 2, No. 1, January 2013 2013 IJMERR. All Rights Reserved CFD ANALYSIS OF TRIANGULAR
More informationAnalysis of Flow over a Convertible
69 Analysis of Flow over a Convertible Aniket A Kulkarni 1, S V Satish 2 and V Saravanan 3 1 PES Institute of Technology, India, aniket260919902@gmail.com 2 PES Institute of Technology, India, svsatish@pes.edu
More informationNUMERICAL INVESTIGATION OF VERTICAL AXIS WIND TURBINE WITH TWIST ANGLE IN BLADES
Eleventh International Conference on CFD in the Minerals and Process Industries CSIRO, Melbourne, Australia 7-9 December 05 NUMERICAL INVESTIGATION OF VERTICAL AXIS WIND TURBINE WITH TWIST ANGLE IN BLADES
More informationA high-order discontinuous Galerkin solver for 3D aerodynamic turbulent flows
A high-order discontinuous Galerkin solver for 3D aerodynamic turbulent flows F. Bassi, A. Crivellini, D. A. Di Pietro, S. Rebay Dipartimento di Ingegneria Industriale, Università di Bergamo CERMICS-ENPC
More informationParticles Removal from a Moving Tube by Blowing Systems: A CFD Analysis
Engineering, 2013, 5, 268-276 http://dx.doi.org/10.4236/eng.2013.53037 Published Online March 2013 (http://www.scirp.org/journal/eng) Particles Removal from a Moving Tube by Blowing Systems: A CFD Analysis
More informationV (r,t) = i ˆ u( x, y,z,t) + ˆ j v( x, y,z,t) + k ˆ w( x, y, z,t)
IV. DIFFERENTIAL RELATIONS FOR A FLUID PARTICLE This chapter presents the development and application of the basic differential equations of fluid motion. Simplifications in the general equations and common
More informationHeat processes. Heat exchange
Heat processes Heat exchange Heat energy transported across a surface from higher temperature side to lower temperature side; it is a macroscopic measure of transported energies of molecular motions Temperature
More informationA 2-D Test Problem for CFD Modeling Heat Transfer in Spent Fuel Transfer Cask Neutron Shields. G Zigh and J Solis U.S. Nuclear Regulatory Commission
CFD4NRS2010 A 2-D Test Problem for CFD Modeling Heat Transfer in Spent Fuel Transfer Cask Neutron Shields G Zigh and J Solis U.S. Nuclear Regulatory Commission Abstract JA Fort Pacific Northwest National
More informationNumerical Investigation of the Hydrodynamic Performances of Marine Propeller
Numerical Investigation of the Hydrodynamic Performances of Marine Propeller Master Thesis developed at "Dunarea de Jos" University of Galati in the framework of the EMSHIP Erasmus Mundus Master Course
More informationTo study the motion of a perfect gas, the conservation equations of continuity
Chapter 1 Ideal Gas Flow The Navier-Stokes equations To study the motion of a perfect gas, the conservation equations of continuity ρ + (ρ v = 0, (1.1 momentum ρ D v Dt = p+ τ +ρ f m, (1.2 and energy ρ
More informationInternational Engineering Research Journal Comparative Study of Sloshing Phenomenon in a Tank Using CFD
International Engineering Research Journal Comparative Study of Sloshing Phenomenon in a Tank Using CFD Vilas P. Ingle, Dattatraya Nalawade and Mahesh Jagadale ϯ PG Student, Mechanical Engineering Department,
More informationPrediction of Performance Characteristics of Orifice Plate Assembly for Non-Standard Conditions Using CFD
International Journal of Engineering and Technical Research (IJETR) ISSN: 2321-0869, Volume-3, Issue-5, May 2015 Prediction of Performance Characteristics of Orifice Plate Assembly for Non-Standard Conditions
More informationA Computational Fluid Dynamics Investigation of Solar Air Heater Duct Provided with Inclined Circular Ribs as Artificial Roughness
Bonfring International Journal of Industrial Engineering and Management Science, Vol. 4, No. 3, August 2014 115 A Computational Fluid Dynamics Investigation of Solar Air Heater Duct Provided with Inclined
More informationCFD study for cross flow heat exchanger with integral finned tube
International Journal of Scientific and Research Publications, Volume 6, Issue 6, June 2016 668 CFD study for cross flow heat exchanger with integral finned tube Zena K. Kadhim *, Muna S. Kassim **, Adel
More informationTaylor Dispersion Created by Robert P. Hesketh, Chemical Engineering, Rowan University Fall 2005
Taylor Dispersion Created by Robert P. Hesketh, Chemical Engineering, Rowan University Fall 005 In this problem you will simulate a tubular reactor with fluid flowing in laminar flow. The governing equations
More informationSTRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS R1. By Kimbal A. Hall, PE. Submitted to: WESTFALL MANUFACTURING COMPANY
STRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS-411519-1R1 By Kimbal A. Hall, PE Submitted to: WESTFALL MANUFACTURING COMPANY OCTOBER 2011 ALDEN RESEARCH LABORATORY, INC. 30 Shrewsbury Street
More informationMulti-Fidelity Computational Flow Assurance for Design and Development of Subsea Systems and Equipment Simon Lo
Multi-Fidelity Computational Flow Assurance for Design and Development of Subsea Systems and Equipment Simon Lo CD-adapco, Trident House, Basil Hill Road, Didcot, OX11 7HJ, UK Multi-Fidelity Computational
More informationStudy on residence time distribution of CSTR using CFD
Indian Journal of Chemical Technology Vol. 3, March 16, pp. 114-1 Study on residence time distribution of CSTR using CFD Akhilesh Khapre*, Divya Rajavathsavai & Basudeb Munshi Department of Chemical Engineering,
More informationNumerical studies on natural ventilation flow in an enclosure with both buoyancy and wind effects
Numerical studies on natural ventilation flow in an enclosure with both buoyancy and wind effects Ji, Y Title Authors Type URL Numerical studies on natural ventilation flow in an enclosure with both buoyancy
More informationABSTRACT I. INTRODUCTION
2017 IJSRSET Volume 3 Issue 3 Print ISSN: 2395-1990 Online ISSN : 2394-4099 Themed Section: Engineering and Technology CFD Analysis of Flow through Single and Multi Stage Eccentric Orifice Plate Assemblies
More informationNumerical simulation of flow past a circular base on PANS methods
IOP Conference Series: Materials Science and Engineering PAPER OPEN ACCESS Numerical simulation of flow past a circular base on PANS methods To cite this article: J T Liu et al 016 IOP Conf. Ser.: Mater.
More informationModelling interfacial heat transfer in a 2-phase flow in a packed bed
Modelling interfacial heat transfer in a 2-phase flow in a paced bed Dariusz ASENDRYCH, Paweł NIEGODAJEW Institute of Thermal Machinery Częstochowa University of Technology, Poland 1 Outline Motivation
More informationOn the transient modelling of impinging jets heat transfer. A practical approach
Turbulence, Heat and Mass Transfer 7 2012 Begell House, Inc. On the transient modelling of impinging jets heat transfer. A practical approach M. Bovo 1,2 and L. Davidson 1 1 Dept. of Applied Mechanics,
More informationNumerical Analysis of Fe 3 O 4 Nanofluid Flow in a Double Pipe U-Bend Heat Exchanger
International Journal of Engineering Studies. ISSN 0975-6469 Volume 8, Number 2 (2016), pp. 211-224 Research India Publications http://www.ripublication.com Numerical Analysis of Fe 3 O 4 Nanofluid Flow
More informationTHE USE OF PB-BI EUTECTIC AS THE COOLANT OF AN ACCELERATOR DRIVEN SYSTEM. Joint research Centre of the European Commission Ispra, Italy.
THE USE OF PB-BI EUTECTIC AS THE COOLANT OF AN ACCELERATOR DRIVEN SYSTEM Alberto Peña 1, Fernando Legarda 1, Harmut Wider 2, Johan Karlsson 2 1 University of the Basque Country Nuclear Engineering and
More informationEjector Pump CFD Model Validation and Performance Improvement Studies
Journal of Scientific & Industrial Research Vol. 77, June 2018, pp. 353-358 Ejector Pump CFD Model Validation and Performance Improvement Studies B H Arun 1, J Vyas 2 *, B M Gopalsamy 2 and M Chimmat 2
More informationNumerical and Experimental Study on the Effect of Guide Vane Insertion on the Flow Characteristics in a 90º Rectangular Elbow
Numerical and Experimental Study on the Effect of Guide Vane Insertion on the Flow Characteristics in a 90º Rectangular Elbow Sutardi 1, Wawan A. W., Nadia, N. and Puspita, K. 1 Mechanical Engineering
More informationINTERNATIONAL JOURNAL OF SCIENTIFIC & TECHNOLOGY RESEARCH VOLUME 5, ISSUE 09, SEPTEMBER 2016 ISSN
Numerical Analysis Of Heat Transfer And Fluid Flow Characteristics In Different V-Shaped Roughness Elements On The Absorber Plate Of Solar Air Heater Duct Jitesh Rana, Anshuman Silori, Rohan Ramola Abstract:
More informationUNSTEADY FREE CONVECTION BOUNDARY-LAYER FLOW PAST AN IMPULSIVELY STARTED VERTICAL SURFACE WITH NEWTONIAN HEATING
FLUID DYNAMICS UNSTEADY FREE CONVECTION BOUNDARY-LAYER FLOW PAST AN IMPULSIVELY STARTED VERTICAL SURFACE WITH NEWTONIAN HEATING R. C. CHAUDHARY, PREETI JAIN Department of Mathematics, University of Rajasthan
More informationComputational Fluid Dynamics Based Analysis of Angled Rib Roughened Solar Air Heater Duct
Research Article International Journal of Thermal Technologies ISSN 2277-4114 2013 INPRESSCO. All Rights Reserved. Available at http://inpressco.com/category/ijtt Computational Fluid Dynamics Based Analysis
More informationDevelopment of Two-Dimensional Convergent-Divergent Nozzle Performance Rapid Analysis Project
International Forum on Energy, Environment Science and Materials (IFEESM 015) Development of Two-Dimensional Convergent-Divergent Nozzle Performance Rapid Analysis Project Yaxiong YANG 1,a *, Eri Qitai,b,
More informationPredictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical and CFD Method
International Journal of Engineering and Technical Research (IJETR) ISSN: 2321-0869, Volume-3, Issue-5, May 2015 Predictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical
More informationFLOW MALDISTRIBUTION IN A SIMPLIFIED PLATE HEAT EXCHANGER MODEL - A Numerical Study
FLOW MALDISTRIBUTION IN A SIMPLIFIED PLATE HEAT EXCHANGER MODEL - A Numerical Study Nityanand Pawar Mechanical Engineering, Sardar Patel College of Engineering, Mumbai, Maharashtra, India nitya.pawar@gmail.com
More informationMODA. Modelling data documenting one simulation. NewSOL energy storage tank
MODA Modelling data documenting one simulation NewSOL energy storage tank Metadata for these elements are to be elaborated over time Purpose of this document: Definition of a data organisation that is
More informationA STUDY ON SLUG INDUCED STRESSES USING FILE-BASED COUPLING TECHNIQUE
A STUDY ON SLUG INDUCED STRESSES USING FILE-BASED COUPLING TECHNIQUE Abdalellah O. Mohmmed, Mohammad S. Nasif and Hussain H. Al-Kayiem Department of Mechanical Engineering, Universiti Teknologi Petronas,
More informationA Numerical Study of Convective Heat Transfer in the Compression Chambers of Scroll Compressors
Purdue University Purdue e-pubs International Compressor Engineering Conference School of Mechanical Engineering 2012 A Numerical Study of Convective Heat Transfer in the Compression Chambers of Scroll
More informationA Discussion of Low Reynolds Number Flow for the Two-Dimensional Benchmark Test Case
A Discussion of Low Reynolds Number Flow for the Two-Dimensional Benchmark Test Case M. Weng, P. V. Nielsen and L. Liu Aalborg University Introduction. The use of CFD in ventilation research has arrived
More informationEVALUATION OF FOUR TURBULENCE MODELS IN THE INTERACTION OF MULTI BURNERS SWIRLING FLOWS
EVALUATION OF FOUR TURBULENCE MODELS IN THE INTERACTION OF MULTI BURNERS SWIRLING FLOWS A Aroussi, S Kucukgokoglan, S.J.Pickering, M.Menacer School of Mechanical, Materials, Manufacturing Engineering and
More informationA Comparative Analysis of Turbulent Pipe Flow Using k And k Models
A Comparative Analysis of Turbulent Pipe Flow Using k And k Models 1 B. K. Menge, 2 M. Kinyanjui, 3 J. K. Sigey 1 Department of Mathematics and Physics. Technical University of Mombasa, P.O BOX 90420-80100,Mombasa,
More informationTHERMAL ANALYSIS OF SECOND STAGE GAS TURBINE ROTOR BLADE
Polymers Research Journal ISSN: 195-50 Volume 6, Number 01 Nova Science Publishers, Inc. THERMAL ANALYSIS OF SECOND STAGE GAS TURBINE ROTOR BLADE E. Poursaeidi, M. Mohammadi and S. S. Khamesi University
More informationHEAT TRANSFER COEFFICIENT CHARACTERIZATION AT THE SOLAR COLLECTOR WALL-FLUID INTERFACE
SASEC15 Third Southern African Solar Energy Conference 11 13 May 15 Kruger National Park, South Africa HEAT TRANSFER COEFFICIENT CHARACTERIZATION AT THE SOLAR COLLECTOR WALL-FLUID INTERFACE Mébarki Ghazali*
More informationCFD-Modeling of Turbulent Flows in a 3x3 Rod Bundle and Comparison to Experiments
CFD-Modeling of Turbulent Flows in a 3x3 Rod Bundle and Comparison to Experiments C. Lifante 1, B. Krull 1, Th. Frank 1, R. Franz 2, U. Hampel 2 1 PBU, ANSYS Germany, Otterfing 2 Institute of Safety Research,
More informationCFD Time Evolution of Heat Transfer Around A Bundle of Tubes In Staggered Configuration. G.S.T.A. Bangga 1*, W.A. Widodo 2
CFD Time Evolution of Heat Transfer Around A Bundle of Tubes In Staggered Configuration G.S.T.A. Bangga 1*, W.A. Widodo 2 1,2 Department of mechanical engineering Field of study energy conversion Institut
More information