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[求助] 救命!关于SolidWorks FloWorks的问题

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发表于 2009-10-15 15:59:04 | 显示全部楼层 |阅读模式 来自: 中国辽宁沈阳

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求助各位大侠,SolidWorks FloWorks 中怎么定义一个逐渐发散的体积流啊。- C, V$ I4 ]3 h  s. `5 O  P# i
      就比如,烧水的时候冒出的蒸汽,水壶口冒出的烟气,然后向上逐渐扩散,怎么定义啊?
) U5 U/ t+ @! y( b( Y& c      请大家帮忙!~~
# b! L; ~) I: [7 `3 B$ j1 i$ v8 D1 m
     谢谢大家了先!~~
发表于 2009-10-15 18:27:13 | 显示全部楼层 来自: 中国上海
MS模拟不了多相流(混在一起的)。
 楼主| 发表于 2009-10-16 08:34:18 | 显示全部楼层 来自: 中国辽宁沈阳
不是多相的,就只是气相的啊。8 }/ V3 P& V3 O7 P

# @4 i8 M" J3 A: k我现在是想模拟下,比如一股热气流,在流动过程中,是逐渐发散的形态。; Q8 W/ X: W7 _( X, a; H

; F# Y2 f, F2 f5 Q+ P7 i9 L- T这个能模拟吗?
发表于 2009-10-28 18:29:52 | 显示全部楼层 来自: 中国上海
在ANSYS CFX中这种问题是按多相流处理的。我想Floworks也类似吧。* s- h2 s+ @, Q& R
两种不同的流体应该算多相,对吧?
发表于 2010-1-15 13:24:50 | 显示全部楼层 来自: 中国江苏盐城
模拟不了多相流
发表于 2010-2-7 13:05:07 | 显示全部楼层 来自: 中国江苏苏州
楼主,俺是来顶你贴的MM.嘎嘎!!热血英雄
: X8 F( S& K1 m  j; H4 f3 f) }+ `' E7 Cdnf外挂" Q5 |4 v1 F( r3 C7 M( G' }
热血英雄7 ?+ j' X1 O' ~5 C  p( I" [% [
面对面视频游戏0 M) {; b2 d0 i8 j
永恒之塔外挂5 e- F" ~; j  f7 m
奇迹助手
3 R: p3 R, z$ h! n+ U, H奇迹勇士9 J! C! A2 ]* w8 x- w
dnf外挂热血宝宝) T) D$ R# j) F8 ~' Z
绿色征途外挂
9 v( ?# ?9 n( J# e# Z" d/ W梦幻诛仙外挂, S  d  {- ?: C- Z, H3 W+ f# Z
名将三国外挂* p. k/ s) ?! q& p4 Z+ k' A
热血江湖外挂2 `3 O, d! n7 A7 R- ~4 s
热血江湖外挂
发表于 2010-6-18 11:31:35 | 显示全部楼层 来自: 中国河南焦作
好像做不了
发表于 2010-6-18 20:30:54 | 显示全部楼层 来自: 中国江西南昌
貌似floworks没这个功能吧
发表于 2010-6-21 23:41:30 | 显示全部楼层 来自: 美国
你问的太含混:
  W. |6 W: L3 k4 w% [
7 i7 K. l5 r  W  A! _1。 若是水, 则应该参考:
) N' Z4 T3 _4 z1 u! [7 L4 A2 ^5 q8 o' q3 L4 }
If the gas whose flow is computed includes steam, COSMOSFloWorks can predict an
7 B5 l3 A5 C; i2 l- R  Bequilibrium volume condensation of water from this steam (without any surface ( \* S" a1 E% o. o/ p7 g
condensation) taking into account the corresponding changes of the steam’s temperature,
0 t7 J" O! F7 M- t# Odensity, enthalpy, specific heat, and sonic velocity. In accordance with the equilibrium
! K0 l& q9 C4 F/ r5 Mapproach, the condensed water’s local mass fraction in the local total mass of the steam : p( W: ]" r1 X& h
and the condensed water is determined from the fluid’s local temperature, pressure, and, if 7 |, w4 O5 B" a. |6 E
a multi-component fluid is considered, the steam’s local mass fraction. Since this   ]& o, [1 m0 x
condensation model is at equilibrium, the condensation has no history, i.e. it is a local fluid
- x* @' o* e" w, C! cproperty only.
+ i8 F7 t* P* }  `' ^& z# `& xIn addition, it is assumed that
: y8 q0 _+ X( M• the condensed water’s volume is equal to zero, so this prediction is correct only if
3 Z% G5 p, \  `the condensed water’s relative volume does not exceed 5%,
6 i; e% {3 B4 |) `8 |• the steam’s temperature lie in the range of 283...610 K and the pressure does not 0 M( s$ ~0 q3 j
exceed 10 MPa.
发表于 2010-6-21 23:43:17 | 显示全部楼层 来自: 美国
2. 若只是某种变干度的二项流, 则应该参考加入粒子,粒子浓度=f(变干度),* ]' }6 u8 r$ N
把该函数输入即可。
发表于 2010-6-21 23:46:32 | 显示全部楼层 来自: 美国
至于有人说模拟不了,那是不对的。Floworks完全可以:参:. e# j, n8 y- ~
6 M+ R" f/ h- L4 B+ y: E9 E
1  Physical Capabilities of COSMOSFloWorks
" Q2 @# T$ }# U) DWith COSMOSFloWorks it is possible to study a wide range of fluid flow and heat 4 _, C  N. ?( z5 h- r. m9 |
transfer phenomena that include the following:
8 W+ {5 ?; K0 Q( S  s, ]: h+ Y• External and internal fluid flows( ~2 i' m5 O4 D( M  ^. \' O* o5 O+ o
• Steady-state and transient fluid flows6 r4 h( ~4 V2 Q: Z
• Compressible gas and incompressible fluid flows (either in different projects or
- n  p+ q: U) [6 c) f& v6 z& ^+ Isimultaneously in different regions not in contact with each other)4 U+ {  F8 g) N2 z! N) a+ R
• Free, forced, and mixed convection3 i* v2 b$ l7 j0 {
• Fluid flows with boundary layers, including wall roughness effects2 s& t/ m8 }- _1 m+ m
• Laminar and turbulent fluid flows
2 u9 T  l, Q: h  o5 O• Multi-species fluids and multi-component solids• Heat transfer in fluid and solid media with/without conjugate heat transfer and/or / H  @1 W4 Y) Q; R% y* m
contact heat resistance between solids and/or radiation heat transfer between
3 A$ W; t5 N9 a$ t  i; M# |8 Oopaque solids (some solids can be considered as transparent for radiation)) X. r5 _5 B' g) f
• Fluid flows in porous media
- n7 t* x' i, V4 D* O• Flows of Non-Newtonian liquids5 F. ^  X9 b& c" C+ E7 v( @4 H8 K
• Flows of compressible liquids+ _( W5 S0 o  r4 h
• Two-phase (fluid + particles) flows: j  A4 K- Y; h  s4 g5 a, T4 Y  Z
• Equilibrium volume condensation of water from steam and its influence on fluid
5 Z, D( e/ i, ?4 H' Jflow and heat transfer* Q; e. ], R$ ^' M3 d4 Z3 R4 I
• Fluid flows in models with moving/rotating surfaces and/or parts
发表于 2010-6-24 17:04:14 | 显示全部楼层 来自: 中国上海
tigerdak说的是对的,模拟不了多相流。也许你们能做到,希望会的人能够做个简单的例子!不胜感激!
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