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October 15, 2015, 06:02 
UDS equation for liquid water saturation in porous media

#1 
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Location: Portugal
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Hello,
I am simulating the cathode of a PEM fuel cell. I wrote a udf which accounts for the reaction of O2 into the catalyst layer and the consequent formation of water vapor. I am now trying to account for the water vapor condensation by solving a UDS equation for the liquid water saturation in the porous media. I managed to write the UDFs for the UDS diffusivity, flux and source, but i am not getting promise results. The solution either diverges rapidly or, if not, the results are senseless. If fact, I am trying to do the same as in the PEMFC module from Fluent, but without using their module. Does anyone have experience on liquid water saturation simulation in porous media, and has some suggestions? Any comment will be appreciated. Thanks! 

October 15, 2015, 10:16 

#2 
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Bruno Machado
Join Date: May 2014
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I am building an entire fuel cell module as an UDF. I was getting problem in my liquid equation due to the initial condition. Depending on the way you set your initial condition, evaporation/condensation can happen and it leads to a negative liquid fraction.
Have a look at it and let me know if it worked for you. By the way, how did you built your mesh? I am facing problem with mine =/ Regards. 

October 15, 2015, 13:01 

#3 
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Hi Bruno (Português?)
I also did notice that the initial value for the uds (liquid water saturation) is important, and I tried several options. The results did change but they are still far from acceptable (water distribution is senseless and saturation in some areas is greater than 1.0..) Did follow any specific criteria for choosing the initial value? Do you also work with PEM fuel cell type? I built my mesh using the Design Modeler (Geometry) and the ANSYS Meshing (mesh) and so far so good. Regards. 

October 15, 2015, 14:13 

#4 
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Bruno Machado
Join Date: May 2014
Posts: 259
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Hi Rui_27,
Im from Brazil, but I am doing my PhD in the UK. I did not follow any specific criteria, but I considered 0.1 as the initial value for the liquid water and it worked fine (I tried less than this and I got problem and senseless values). In addition to that, I add a if condition to my code that if the liquid saturation scalar is equal to 0.00001, the source term is equal to 0 (no condensation/evaporation), so the liquid phase remains positive. Yes, I am working with PEM fuel cell, but I am studying a Anion Exchange Membrane (AEM) fuel cell. Could you please share how you did your mesh? I am not sure how to do regarding the parts/bodys and also the contact regions. Or if it wont cause you any harm, could you share your mesh/geometry file? I will let my email here, so you can speak in Portuguese and once we solve our issues, we can post the solution here. My email is: brunosouzamachado@gmail.com All the best. 

October 16, 2015, 05:29 

#5 
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Bruno, I just sent you a email with a response.
If anyone else has any other suggestions, they will be greatly appreciated! 

October 20, 2015, 10:33 

#6 
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Bruno
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Try posting the equations you're solving, boundary conditions, etc. Maybe with more info someone could help finding the problem.


October 20, 2015, 11:57 

#7 
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Good ideia Brunoc.
I am trying to solve a UDS equation for the liquid water saturation in a cathode of a PEM fuel cell.  First I have two UDFs with sources terms that account for the condensation/evaporation of water. One applied to the equation of h2o (vapor) and other (same value with opposite sign) applied in the UDS equation (liquid water).  Then I have a UDF for the diffusivity of the UDS. In the porous media it corresponds to the capillary difusivity and in the nonporous media I set the diffusivity as 0.0.  I also have a UDF for the UDS flux. It is equal to dens_liquid*gas_velocity in the nonporous zone and equal to 0.0 in the porous media. The UDFs codes are below. Equations are in the file attached (1.26 for nonporous and 1.28 for porous media). Regards  DEFINE_SOURCE(liquid_source_h2o,c,t,dS,eqn) { real P_h2o; real Psat; real dens_liquid; real s; real term1; real term2; real source; s =MAX(0.0001, MIN(C_UDSI(c,t,0),0.999)); Psat= 100000.0*pow(10,2.1794+0.02953*T9.1387/100000*pow(T,2)+1.4451/10000000*pow(T,3)); dens_liquid=0.0036*pow(T,2)0.0695*T+1000.5; /*kg m3*/ P_h2o= C_YI(c, t, 1)*C_R(c,t)*R*(T+273.15)/(MH2O*0.001); C_UDMI(c,t,66) =P_h2o; term1 = (1s)*(P_h2oPsat)/R/(T+273.15)*(MH2O*0.001); term2 = 1.0*s*dens_liquid; C_UDMI(c,t,67) =term1; C_UDMI(c,t,68) =term2; if (term1>term2) { source = 1.0*kc*term1; dS[eqn] = 1.0*(P_h2oPsat)/R/(T+273.15)*(MH2O*0.001)*kc; } else { source = 1.0*kc*term2; dS[eqn] = 1.0*dens_liquid*kc; } C_UDMI(c,t,69) =source; C_UDMI(c,t,70) =dS[eqn]; C_UDMI(c,t,71) = 1.0*(P_h2oPsat)/R/(T+273.15)*(MH2O*0.001)*kc; return source; } DEFINE_SOURCE(liquid_source_s,c,t,dS,eqn) { real source; source= 1.0*C_UDMI(c,t,69); dS[eqn]=1.0*C_UDMI(c,t,70); C_UDMI(c,t,81) =source; C_UDMI(c,t,82) =dS[eqn]; return source; } DEFINE_DIFFUSIVITY(liquid_diffusivity2, c, t, i) { real K_abs; real surf_tension; real visc_liquid; real dens_liquid; real dpcds=0.0; real K_rel=0.0; real s; real ss=0.0; real diff; s = MAX(0.0001, MIN(C_UDSI(c,t,0),0.999)); K_abs = 2.55e13; /*m2*/ surf_tension = 0.0002*T+0.0761; /*N m2*/ visc_liquid= (0.0026*pow(T,3)+0.5874*pow(T,2)47.598*T+1763.4)*1e6; /*Pa.s*/ dens_liquid=0.0036*pow(T,2)0.0695*T+1000.5; /*kg m3*/ K_rel=s*s*s; if (cos(GDL_c_angle*2*pi/360)>0.0) ss=1s; else ss=s; dpcds = surf_tension*ABS(cos(GDL_c_angle*2*pi/360))/sqrt(K_abs/C_POR(c, t))*(1.417 + 3*1.263*ss*ss  2*2.12*ss); if (C_POR(c,t)==1.0) diff=1e20; else diff= dens_liquid*K_abs*K_rel*dpcds/visc_liquid; C_UDMI(c,t,80)=diff; return diff; } DEFINE_UDS_FLUX(uds_flux2,f,t,i) { cell_t c0, c1 = 1; Thread *t0, *t1 = NULL; real NV_VEC(psi_vec), NV_VEC(A), flux = 0.0; c0 = F_C0(f,t); t0 = F_C0_THREAD(f,t); F_AREA(A, f, t); if (C_POR(c0,t0)==1.0) { if (BOUNDARY_FACE_THREAD_P(t)) { real dens; if (NNULLP(THREAD_STORAGE(t,SV_DENSITY))) dens = (0.0036*pow(T,2)0.0695*T+1000.5); else dens = (0.0036*pow(T,2)0.0695*T+1000.5); NV_DS(psi_vec, =, F_U(f,t), F_V(f,t), F_W(f,t), *, dens); flux = NV_DOT(psi_vec, A); } else { c1 = F_C1(f,t); t1 = F_C1_THREAD(f,t); NV_DS(psi_vec, =, C_U(c0,t0),C_V(c0,t0),C_W(c0,t0),*,dens); NV_DS(psi_vec, +=, C_U(c1,t1),C_V(c1,t1),C_W(c1,t1),*,dens); flux = NV_DOT(psi_vec, A)/2.0; } } else { flux=1e20; } C_UDMI(c0,t0,73)=flux; return flux; } 

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