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- - **Fluent UDF urgent! Variable reaction rate**
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Fluent UDF urgent! Variable reaction rateHi
I've written a UDF in Fluent for a volumetric reaction rate. I want to know how I can make the reaction rate variable along my reactor due to variation in catalyst activity. Any idea? Example: r= p* k C^2 ( p is a function of distance into the reactor) How do you implement this, I'm new to UDf Thanks |

Hi,
I guess what you need is a function which gives you the position of the each cell center, which is C_CENTROID(x,c,ct). Here, x is an array which holds the x,y,z coordinates, while c and ct are the cell and thread pointers which are passed from the solver through an appropriate macro. Assuming you are using a DEFINE_ADJUST macro to update your reaction rate, and that your reaction rate is r=x*k*C^2 (x being the x-coordinate), I would use ------ DEFINE_ADJUST(adjustRXR,domain) { Thread *ct; cell_t c; real x[ND_ND]; real k, C,r,pos; k=0.25; /* just an example*/ C=0.1; /* just an example*/ r=0.0; /* initialization to be sure*/ pos=0.0; /* initialization to be sure*/ thread_loop_c(ct,domain) /*Loop over the threads in the domain*/ { begin_c_loop(c,ct) /*Loop over all cells in the thread*/ { C_CENTROID(x,c,ct); /*Find position of cell and store in x*/ pos = x[0]; /*Store the x-coordinate as pos. y-coordinate is x[1], z-coordinate is x[2]*/ r=pos*k*C*C; /*Store reaction rate in local variable r*/ C_UDMI(c,ct,0) = r; /*Store reaction rate in user defined memory position 0 so that other functions can access it*/ }end_c_loop(c,ct) } } ----- You will need one UDM to store the reaction rate if you do it in this way. Remember to hook the DEFINE_ADJUST function before running your simulations. For a more complete example, see section 2.3.22.3 in the UDF-guide. Good luck! -KE |

Thanks A lot for the comment
The problem is my reaction is defined through a volumetric reaction rate DEFINE_VR_RATE , the reaction needs the temperature and mass fraction of each node (300000 nodes) at each iteration. Apparently inside the ADJUST udf we don't ahve access to node values. I get error. Below is my original UDf for VR_Rate, if you like take a look at it. #include"udf.h" DEFINE_VR_RATE(proprate,c,t,r,mw,yi,rr,rr_t) { /*mass fraction of species i */ real y_c3h8=yi[3]; real y_h2o=yi[4]; real y_h2=yi[0]; real y_co=yi[1]; real y_co2=yi[2]; real y_n2=yi[5]; real Nsum, R, Keq1, T_w, r1,r2; /*calculate species i in the unit of kgmol i/kg mix*/ y_c3h8 *= 1/mw[3]; y_h2o *= 1/mw[4]; y_h2 *= 1/mw[0]; y_co *= 1/mw[1]; y_co2 *= 1/mw[2]; y_n2 *= 1/mw[5]; Nsum = y_c3h8+ y_h2o + y_h2 + y_co + y_co2 + y_n2; y_c3h8 *= 1/Nsum; y_h2o *= 1/Nsum; y_h2 *= 1/Nsum; y_co *= 1/Nsum; y_co2 *= 1/Nsum; y_n2 *= 1/Nsum; R=8.314; T_w=C_T(c,t); Keq1=pow(10,(2073/T_w)-2.029); if(STREQ(r->name, "reaction-1")){ /*unit for rr, kg/m3s*/ r1= 44*3e8*exp(-105000/(R*T_w))*(y_c3h8*y_h2o)/(1+105*exp(3000/(R*T_w))*pow(y_c3h8,2)); *rr = r1; } elseif (STREQ(r->name, "reaction-2")){ r2= 28*3.4e9*exp(-130000/(R*T_w))*(y_co*y_h2o-(y_h2*y_co2)/Keq1) ; *rr = r2; } } |

Hello again,
If I understand your original post correctly, your problem is that you want to include a position dependency in your DEFINE_VR_RATE? This can be done by the following modification (I have made my changes in bold text for clarity): #include"udf.h" DEFINE_VR_RATE(proprate,c,t,r,mw,yi,rr,rr_t) { /*mass fraction of species i */ real Nsum, R, Keq1, T_w, r1,r2,x[ND_ND],xpos,ypos,zpos;real y_c3h8=yi[3]; real y_h2o=yi[4]; real y_h2=yi[0]; real y_co=yi[1]; real y_co2=yi[2]; real y_n2=yi[5]; /* Find and store coordinates for each cell*/C_CENTROID(x,c,t); /* store position in array x*/xpos = x[0];ypos = x[1];zpos = 0.0;#if RP_3Dzpos = x[2];#endif/* The above #if statement ensures that you only can access the z-position (x[2]) if you are doing a 3D-simulation *//* The coordinates of each cell are now stored in xpos,ypos and zpos (if 3D) for future use*//*calculate species i in the unit of kgmol i/kg mix*/ y_c3h8 *= 1/mw[3]; y_h2o *= 1/mw[4]; y_h2 *= 1/mw[0]; y_co *= 1/mw[1]; y_co2 *= 1/mw[2]; y_n2 *= 1/mw[5]; Nsum = y_c3h8+ y_h2o + y_h2 + y_co + y_co2 + y_n2; y_c3h8 *= 1/Nsum; y_h2o *= 1/Nsum; y_h2 *= 1/Nsum; y_co *= 1/Nsum; y_co2 *= 1/Nsum; y_n2 *= 1/Nsum; R=8.314; T_w=C_T(c,t); Keq1=pow(10,(2073/T_w)-2.029); if(STREQ(r->name, "reaction-1")){ /*unit for rr, kg/m3s*/ r1= 44*3e8*exp(-105000/(R*T_w))*(y_c3h8*y_h2o)/(1+105*exp(3000/(R*T_w))*pow(y_c3h8,2)); *rr = r1; } elseif (STREQ(r->name, "reaction-2")){ r2= 28*3.4e9*exp(-130000/(R*T_w))*(y_co*y_h2o-(y_h2*y_co2)/Keq1) ; *rr = r2; } } Another point; note that the values you are using are *not* node values but *cell* values, as it is the cell pointer "c" which is passed from the macro DEFINE_VR_RATE. Happy simulating! -KE |

Calcination ReactionHello all, first of all i would like to introduce myself as new on this field... I've read your posts and i have some doubts... How do you access the molecular weight of each component?? Have you defined it previously?? Because i coudn't realise where are these values on your program line...
Another doubt is about making an User Defined Function for this reaction: caco3=cao+co2 I'm simulating a rotary kiln used for calcination... I need to compilate this reactions in the Fluent but i have no idea about how to do this... Can anyone help me?? Thank you in advance |

Hello
Can someone please help me write a FLUENT UDF the reaction below which is defined by reaction rate equation of (R) below CO+3H2=>CH4+H2O R=k exp (E/RT)*(Pco^m*Ph2^n) Where: R is the volumetric reaction rate k is Rate constant E is Activation energy for reaction R is Universal gas constant T is Temperature Pco is Partial pressure of carbon monoxide Ph2 is Partial pressure of hydrogen m is Power for CO partial pressure n is Power for H2 partial pressure UDF for volumetric reaction rate-unnamed.png Thank you.:) |

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