關(guān)于水蒸氣的相變udf方程
請(qǐng)教各位大神,我在百度上找到了水蒸氣的相變udf,放到我的模型中后,水蒸氣在溶液區(qū)域冷凝放熱,溶液區(qū)域溫度升高過(guò)快,是正確溫升的五百倍左右,請(qǐng)問(wèn)除了改相變潛熱以外還有什么解決方案?因?yàn)楦牧讼嘧儩摕嶂笪锢硪饬x就不正確了
#include "udf.h"
#include "sg_mphase.h"
#define T_SAT 373
#define LAT_HT 2640000
end_f_loop(f,thread)
}
DEFINE_SOURCE(liq_src, cell, pri_th, dS, eqn)
{
Thread *mix_th,*sec_th;
real m_dot_l;
mix_th=THREAD_SUPER_THREAD(pri_th);
sec_th=THREAD_SUB_THREAD(mix_th,1);
if(C_T(cell,mix_th)>=T_SAT)
{
m_dot_l=-0.1*C_VOF(cell,pri_th)*C_R(cell,pri_th)*fabs(C_T(cell,mix_th)-T_SAT)/T_SAT;
dS[eqn]=-0.1*C_R(cell,pri_th)*fabs(C_T(cell,mix_th)-T_SAT)/T_SAT;
}
else
{
m_dot_l=0.1*C_VOF(cell,sec_th)*C_R(cell,sec_th)*fabs(T_SAT-C_T(cell,mix_th))/T_SAT;
dS[eqn]=0.0;
}
return m_dot_l;
}
DEFINE_SOURCE(vap_src,cell,sec_th,dS,eqn)
{
Thread *mix_th,*pri_th;
real m_dot_v;
mix_th=THREAD_SUPER_THREAD(sec_th);
pri_th=THREAD_SUB_THREAD(mix_th,0);
if(C_T(cell, mix_th)>=T_SAT)
{
dS[eqn]=0.;
}
else
{
m_dot_v=-0.1*C_VOF(cell,sec_th)*C_R(cell,sec_th)*fabs(T_SAT-C_T(cell,mix_th))/T_SAT;
dS[eqn]=-0.03141*C_R(cell,sec_th)*fabs(C_T(cell,mix_th)-T_SAT)/T_SAT;
}
return m_dot_v;
}
DEFINE_SOURCE(enrg_src,cell,mix_th,dS,eqn)
{
Thread *pri_th,*sec_th;
real m_dot;
pri_th=THREAD_SUB_THREAD(mix_th,0);
sec_th=THREAD_SUB_THREAD(mix_th,1);
if(C_T(cell, mix_th)>=T_SAT)
{
m_dot=-0.1*C_VOF(cell,pri_th)*C_R(cell,pri_th)*fabs(C_T(cell,mix_th)-T_SAT)/T_SAT;
dS[eqn]=-0.1*C_VOF(cell,pri_th)*C_R(cell,pri_th)/T_SAT;
}
else
{
m_dot=0.1*C_VOF(cell,sec_th)*C_R(cell,sec_th)*fabs(T_SAT-C_T(cell,mix_th))/T_SAT;
dS[eqn]=0.1*C_VOF(cell,sec_th)*C_R(cell,sec_th)/T_SAT;
}
return LAT_HT*m_dot;
}@wuming524@wuming524@wuming524
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development of pressure-based phase change model for CFD modeling of heat pipes, 建議研讀這篇論文
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