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#1 |
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Member
bird
Join Date: Sep 2012
Posts: 38
Rep Power: 2 ![]() |
Dear all,
Hi, I am simulating flow in a flume, the inlet boundary is velocity boundary, however every time I begin the simulation, the water level will increase and extend to the outlet boundary and never descend. For example, the fluid elevation I define at the inlet and outlet boundary is 50cm, but after the flow becoming steady the water level keeps 55cm and never change. How can I solve this problem? 1.At the outlet boundary, I have tried continuative, pressure and outflow boundary. 2.I have tried to increase the velocity slowly at the inlet boundary but it doesn't work. 3.I have put an obstacle at the top of the flume to avoid water rising but the simulation will exit anormally. So who can figure out why? |
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#2 |
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New Member
PetiteHerbe
Join Date: Feb 2013
Posts: 1
Rep Power: 0 ![]() |
Model Setup->General->Interface tracking->Free surface or sharp interface
Model Setup->General->Number of fluids->One fluid Model Setup->Meshing & Geometry->Initial->Void initial state->Pressure:101325Pa |
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#3 |
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Member
bird
Join Date: Sep 2012
Posts: 38
Rep Power: 2 ![]() |
Thank you, maybe I should give the pressure of air, I will try it soon.
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#4 | |
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Member
bird
Join Date: Sep 2012
Posts: 38
Rep Power: 2 ![]() |
Quote:
I will show two pitures below. |
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#5 | |
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New Member
Jing
Join Date: Dec 2011
Posts: 18
Rep Power: 3 ![]() |
Quote:
Hi Please send me the file : "prepin" |
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#6 |
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Member
bird
Join Date: Sep 2012
Posts: 38
Rep Power: 2 ![]() |
Title
This is a sample input file $xput remark='!! Remarks beginning with "!! " are automatically added and removed by FLOW-3D.', remark='!! Do not begin any user added remarks with with "!! ". They will be removed', twfin=250, itb=1, ifin=4, ifvisc=1, ifvis=4, ifdynconv=1, gz=-980, ipdis=1, idpth=1, ifmu=1, tpltd(1)=0.5, $end $limits $end $props units='cgs', tunits='c', mu1=0.01, fluid1='Water at 293 K', thexf1=0.00018, cv1=41820000, tstar=100, tl1=-0.149999999999977, ts1=-0.149999999999977, clht1=3350000000, cvs1=21000000, thcs1=221500, rhofs=0.917, teut=-273.15, tmelt=-273.15, ceut=0, pcoef=0, rhof=1.0, sigma=73, thc1=59700, $end $scalar $end &PCAP / &BCDATA remark='!! Boundary condition X Min', ibct(1)=6, ubct(1, 1)=44.1, fbct(1, 1)=1, flhtbct(1, 1)=50, remark='!! Boundary condition X Max', ibct(2)=8, flhtbct(1, 2)=50, remark='!! Boundary condition Z Min', ibct(5)=2, / &MESH ntotal=1000, nxcelt=2500, px(1)=0, px(2)=5000, nycelt=1, py(1)=0, py(2)=1, nzcelt=70, pz(1)=0, pz(2)=70, / $obs remark='!! Component common parameters', avrck=-3.1, $end $fl nfls=1, remark='!! Fluid Region 1', fluidRegionName(1)='Water at 293 K', fzh(1)=50, pvoid=1.01325e+05, iflinittyp=0, $end $bf $end $temp $end $motn $end $grafic anmtyp(1)='dpth', anmtyp(2)='f', anmtyp(3)='vel', $end &HEADER project='pre out', / $parts $end Documentation: general comments, background, expectations, etc. #start tables: #fluid1: #blkmodts #end blkmodts #cv1 #end cv1 #cvnc #end cvnc #elastmodts #end elastmodts #emod1 #end emod1 #fs #end fs #mu1sr #end mu1sr #mu1t #end mu1t #poissonrts #end poissonrts #rhof #end rhof #shrmodts #end shrmodts #sigma #end sigma #thc1 #end thc1 #yield1 #end yield1 #end fluid1 #fluid2: #cv2 #end cv2 #emod2 #end emod2 #mu2sr #end mu2sr #mu2t #end mu2t #rhof2 #end rhof2 #thc2 #end thc2 #yield2 #end yield2 #end fluid2 #end start tables |
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#7 |
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Member
bird
Join Date: Sep 2012
Posts: 38
Rep Power: 2 ![]() |
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#8 |
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Member
CH
Join Date: Jan 2013
Posts: 47
Rep Power: 2 ![]() |
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