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gml123456新虫 (小有名气)
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[求助]
请教各位懂Fortran的大侠！！！！！！！！！！
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本人在做铁水脱硫过程的数学模型的程序设计，使用的是Fortran语言，vs2010和Intel Fortran Composer XE 2011，在调试过程中出现警告 警告 4 warning #13380 Compiler configuration problem encountered. Compiler cannot load imf dispatching library. D:\软件安装\My Project\Console2\Console2\Source1.f901 。本人初学，哪位大侠知道是怎么回事？不胜感激！！！ 求帮助！ 源代码如下： ！ 主程序 ! 将原来的计算粉剂停留时间中的0.815改为0.45再改为0.37,Ps=2200 external f external ff external taofnf integer taofnn,taofnm,TN,TN1 dimension y(1),d(1),z(1,3600),b(1),zz(1,3600) double precision y,d,z,t,h,b,zz DIMENSION TAOFNY(1),TAOFND(1),TAOFNZ(1,150*2),TAOFNB(1) double precision taoFNy,taoFNd,taoFNz,taoFNh,taoFNb,taoFNt !双精度语句 real a,A0,bei,Ip,Tao,Yi,Ps,Pm,Pz,WD,L,dm,Ws0,Wm,FeO0,CaO0,MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00,QLIU,ZT common a,a0,bei,Ip,Tao,Yi,Ps,Pm,Pz,WD,L,dm,Ws0,Wm,FeO0,CaO0, MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00, ZT common /Q1/QLIU open(unit=1,file='cSjladle.DAT',access='sequential',form='formatted') read(1,100) a,$a read(1,100) A0,$a read(1,110) Ip,$a read(1,100) Yi,$a read(1,100) Ps,$a read(1,100) Pm,$a read(1,100) Pz,$a read(1,100) wd,$a read(1,100) L,$a read(1,200) dm,$a read(1,300) Ws0,$a read(1,300) Wm,$a read(1,400) FeO0,$a read(1,400) CaO0,$a read(1,400) MgO0,$a read(1,400) SiO20,$a read(1,400) Al2O30,$a read(1,400) CaOp,$a read(1,400) CaC2p,$a read(1,400) Ecs,$a read(1,400) Esis,$a read(1,400) Eps,$a read(1,400) Emns,$a read(1,500) C,$a read(1,500) Si,$a read(1,110) P,$a read(1,110) Mn,$a read(1,600) S0,$a read(1,600) S00,$a read(1,400) qliu,$a read(1,700) TN,$a read(1,700) TN1,$a 100 format(F6.1,A) !格式说明语句 110 format(F6.3,A ) 200 FORMAT(F10.8,A) 300 format(F8.1,A) 400 format(F7.4,A) 500 format(F4.2,A) 600 format(F7.5,A) 700 format(I4,A) ! 调用求粉剂停留时间子程序 TAOFNT=0 TAOFNY(1)=0 TAOFNH=0.03 TAOFNH=0.005 TAOFNM=1 TAOFNN=142 ! TAOFNN=257 CALL grktTFN(TAOFNt,TAOFNY,TAOFNm,TAOFNh,TAOFNn,TAOFNz,TAOFNf,TAOFNd,TAOFNb) open(unit=3,file='mcFENtao.dat') do 1000 i=1,TAOFNn TAOFNt=(i-1)*TAOFNh write(3,2000) TAOFNT,(TAOFNz(j,i),j=1,taoFNm) 1000 continue 2000 format(F7.3,E18.6) tao=taoFNz(1,taoFNn) ! 调用喷粉脱硫子程序 t=0.0 y(1)=S00 h=1 m=1 n=tn+1 n1=tn1+1 zt=h*n call grkt1(t,y,m,h,n,z,f,d,b) write(*,*) open(unit=2,file='ladlecac2csjladle01.DAT') do 10 i=1,n t=(i-1)*h+0.0 write(2,50)t,(z(j,i),j=1,m) 10 continue WRITE(*,*) Z(1,N) ! 调用喷粉之后吹气脱硫子程序 t=(n-1)*h y(1)=z(1,n) m1=1 call grkt2(t,y,m1,h,n1,zz,ff,d,b) write(*,*) open(unit=2,file='ladlecac2csjladle01.dat') do 20 i=2,n1 t=(i-2)*h+h*n write(2,50)t,(zz(j,i),j=1,m1) 20 continue ! ***************************************************************** 50 format(f7.2,e18.10,e18.10) close(1) close(2) close(3) end ! 粉剂停留时间子程序 subroutine grktTFN(TAOFNt,TAOFNY,TAOFNm,TAOFNh,& TAOFNn,TAOFNz,TAOFNf,TAOFNd,TAOFNb) integer TAOFNm, TAOFNn dimension TAOFNy(TAOFNm),TAOFNd(TAOFNm),TAOFNz(TAOFNm,TAOFNn),A(4),TAOFNb(TAOFNm) double precision TAOFNy,TAOFNd,TAOFNz,a,TAOFNb,TAOFNt,TAOFNh,x,tt a(1)=TAOFNh/2.0 a(2)=a(1) a(3)=TAOFNh a(4)=TAOFNh do 5 i=1,TAOFNm 5 TAOFNz(i,1)=TAOFNy(i) x=TAOFNt do 100 j=2,TAOFNn call TAOFNF(TAOFNt,TAOFNm,TAOFNd) do 10 i=1,TAOFNm 10 TAOFNb(i)=TAOFNy(i) do 30 k=1,3 do 20 i=1,TAOFNm TAOFNy(i)=TAOFNz(i,j-1)+a(k)*TAOFNd(i) TAOFNb(i)=TAOFNb(i)+a(k+1)*TAOFNd(i)/3.0 20 continue tt=TAOFNt+a(k) call TAOFNf(tt,TAOFNm,TAOFNd) 30 continue do 40 i=1,TAOFNm 40 TAOFNy(i)=TAOFNb(i)+TAOFNh*TAOFNd(i)/6.0 do 50 i=1,TAOFNm 50 TAOFNz(i,j)=TAOFNy(i) TAOFNt=TAOFNt+TAOFNh 100 continue TAOFNt=x return end ! 喷粉脱硫子程序 subroutine grkt1(t,y,m,h,n,z,f,d,b) dimension y(m),d(m),z(m,n),a(4),b(m) double precision y,d,z,a,b,t,h,x,tt a(1)=h/2.0 a(2)=a(1) a(3)=h a(4)=h do 5 i=1,m 5 z(i,1)=y(i) x=t do 100 j=2,n call f(t,y,m,d) do 10 i=1,m 10 b(i)=y(i) do 30 k=1,3 do 20 i=1,m y(i)=z(i,j-1)+a(k)*d(i) b(i)=b(i)+a(k+1)*d(i)/3.0 20 continue tt=t+a(k) call f(tt,y,m,d) 30 continue do 40 i=1,m 40 y(i)=b(i)+h*d(i)/6.0 do 50 i=1,m z(i,j)=y(i) 50 continue t=t+h 100 continue t=x return end ! 计算停留时间子程序的外部函数 subroutine TAOFNf(taoFNt,taoFNm,taoFNd) COMMON /Q1/QLIU integer taoFNm dimension taoFNd(taoFNm) double precision taoFNd,taoFNt REAL QLIU taoFNd(1)=1.0/(4.945*(3093*QLIU/4)**0.0539563*(0.0049952-0.03896*(taoFNt+0.37)+0.12842*(taoFNt+0.37)**2-0.035039*(taoFNt+0.37)**3+0.001948*(taoFNt+0.37)**4)**0.957432) ! 鱼雷罐车参数 taoFNd(1)=1.0/(4.945*(3093*QLIU)**0.0539563*(0.0049952-0.0824*(taoFNt+0.9)+0.5744*(taoFNt+0.9)**2-0.3314*(taoFNt+0.9)**3+0.03897*(taoFNt+0.9)**4)**0.957432) return end ! 计算喷粉脱硫子程序的外部函数 subroutine f(t,y,m,d) dimension y(m),d(m) double precision y,d,t,u,Dk,w,Re,Sc,Pe,Sh,Km,u2,Dk1,Re1,Sc1,Sh1,Km1,Q,Se,w1 double precision XX,XXX,XXXX,VC,DP,BEILI DOUBLE PRECISION UUS,DDS,WWS,RES,SCS,SHS,KMS REAL a,A0,bei,Ip,Tao,Yi,Ps,Pm,Pz,WD,L,dm,Ws0,Wm,FeO0,CaO0,MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00,ZT,Qliu ,tm ,gqm DOUBLE PRECISION Xfeo,Xsialp,Xcamnmg,Afeo,Rjd ,Ls COMMON a,a0,bei,Ip,Tao,Yi,Ps,Pm,Pz,WD,L,dm,Ws0,Wm,FeO0,CaO0,MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00,ZT COMMON /Q1/QLIU ! ********************************************************************* write(*,*) yi,mn,s00,ecs,WD ! *************************************************************** w1=0.51967*(QLIU)**(1.0/3.0) Q=Ecs*C+Emns*Mn+Esis*Si+Eps*P Se=0.00000100 tm=1.22*167.2*(76.12*QLIU)**(-0.22721) tm=167.2*(76.12*QLIU)**(-0.22721) tm=60.7*(76.128*qliu)**(-0.52527) ! 计算传质系数 u=0.30805*1.0E-003*EXP(5284.6079/(wd-0.014*t)) Dk=4.33*1.0E-008*EXP(-4281.9/(wd-0.014*t)) w=(Pm-Ps)*9.8*dm**2/(18.0*u) Re=Pm*w*dm/u Sc=u/(Pm*Dk) Pe=Sc*Re Sh=(4.0+1.21*Pe**(2.0/3.0))**(1.0/2.0) Km=Sh*Dk/dm u2=8.0*1.0E-009*EXP(258208.6/(8.314*(wd-0.014*t))) Dk1=1.4*1.0E-004*EXP(-205020.0/(8.314*(wd-0.014*t))) Re1=Pz*w1*L/u2 Sc1=u2/(Pz*Dk1) Sh1=0.664*Sc1**(1.0/3.0)*Re1**(1.0/2.0) Km1=Sh1*Dk1/L gqm=Ip/(0.62144*qliu) BEI=(1.2)**(gqm-10.638)*0.01*7.75858*(Ip/(0.62144*qliu))**0.40928 BEI=0.01*7.75858*(Ip/(0.62144*qliu))**0.40928 VC=1.2732*(QLIU+Ip/2200)/(2*0.042**2) VC=1.2732*(QLIU+Ip/2200)/(0.019**2) DP=80.207/VC**2 BEILI=100-(-1.65745+2591.3*DP-23765.66*DP**2+78006.6*DP**3) BEI=0.01*(73.88724-0.39327*BEILI) BEI=(1.05)**(gqm-10.638)*0.01*(73.88724-0.39327*BEILI) ! 求顶渣脱硫各参数 UUS=8.0*1.0E-009*EXP(258208.6/(8.314*(WD-0.014*t))) DDS=1.4*1.0E-004*EXP(-205020.0/(8.314*(WD-0.014*t))) WWS=0.51967*(QLIU)**(1.0/3.0) ReS=Pz*WWS*L/UUS ScS=UUS/(Pz*DDS) ShS=0.664*ScS**(1.0/3.0)*ReS**(1.0/2.0) KmS=ShS*DDS/L ! 求硫的分配系数与时间的关系 Xfeo=(FeO0*Ws0/72.0)/(FeO0*Ws0/72.0+SiO20*ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40.0+(CaO0*Ws0+Ip*t*(CaOp+CaC2p*7.0/8.0))/56.0) XsiAlP=(SiO20*Ws0/60.0+AL2O30*Ws0/102.0)/(FeO0*Ws0/72.0+SiO20*Ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40.0+(CaO0*Ws0+Ip*t*(CaOp+CaC2p*7.0/8.0))/56.0) Xcamnmg=(MgO0*Ws0/40.0+(CaO0*Ws0+Ip*t*(CaOp+CaC2p*7.0/8.0))/56.0)/(FeO0*Ws0/72.0+SiO20*ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40.0+(CaO0*Ws0+Ip*t*(CaOp+CaC2p*7.0/8.0))/56.0) Afeo=0.14935*Xfeo**0.936719*XsiALP**(-2.83381)*Xcamnmg**0.114412 Rjd=(CaO0*Ws0+Ip*t*(CaOp+CaC2p*7.0/8.0)+0.69*MgO0*Ws0)/(0.93*SiO20*Ws0+0.18*Al2O30*Ws0) Ls=10**(Q-6.929+1.39*Rjd+5384.0/(wd-0.0140*t))/(Afeo) xx=-((a*a0*Pz)/Wm)*KmS*Ls xxx=xx*(y(1)*EXP(-tm/ZT)-((S0*Ws0+(S00-Y(1)*EXP(-tm/ZT))*Wm)/(Ws0+Ip*Yi*t))/Ls) D(1)=-6*bei*Ip*Tao*Pm*Km*(Y(1)*EXP(-tm/ZT)-Se)/(dm*Wm*Ps)-a*A0*Pz*Km1*Ls*(Y(1)*EXP(-tm/ZT)-((S0*Ws0+(S00-Y(1)*EXP(-tm/ZT))*Wm)/(Ws0+Ip*Yi*t))/Ls)/Wm XXXX=-6*bei*Ip*Tao*Pm*Km*(Y(1)*EXP(-tm/ZT)-Se)/(dm*Wm*Ps) write(*,*) d(1),ls return end ! 吹气脱硫子程序 ? subroutine grkt2(t,y,m1,h,n1,zz,ff,d,b) dimension y(m1),d(m1),zz(m1,n1),a(4),b(m1) double precision y,d,zz,a,b,t,h,x,tt a(1)=h/2.0 a(2)=a(1) a(3)=h a(4)=h do 5 i=1,m1 5 zz(i,1)=y(i) x=t do 100 j=2,n1 call ff(t,y,m1,d) do 10 i=1,m1 10 b(i)=y(i) do 30 k=1,3 do 20 i=1,m1 y(i)=zz(i,j-1)+a(k)*d(i) b(i)=b(i)+a(k+1)*d(i)/3.0 20 continue tt=t+a(k) call ff(tt,y,m1,d) 30 continue do 40 i=1,m1 40 y(i)=b(i)+h*d(i)/6.0 do 50 i=1,m1 zz(i,j)=y(i) 50 continue t=t+h 100 continue t=x return end ! 计算吹气脱硫子程序的外部函数 subroutine ff(t,y,m1,d) dimension y(m1),d(m1) double precision y,d,t,u2,u3,Dk1,Re1,Sc1,Sh1,Km1,Q,w1 REAL a,A0,bei,Ip,Tao,Yi,Ps,Pm,Pz,wd,L,dm,Ws0,Wm,FeO0,CaO0,MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00,ZT,QLIU,tm DOUBLE PRECISION Xfeo,Xsialp,Xcamnmg,Afeo,Rjd ,Ls,xx common a,a0,bei,Ip,Tao,Yi,Ps,Pm,Pz,WD,L,dm,Ws0,Wm,FeO0,CaO0,MgO0,SiO20,Al2O30,CaOp,CaC2p,Ecs,Esis,Eps,Emns,C,Si,P,Mn,S0,S00,ZT COMMON /Q1/QLIU ! ********************************************************************* write(*,*) yi,mn,s00,ecs,wd ! *************************************************************** w1=0.51967*(QLIU)**(1.0/3.0) Q=Ecs*C+Emns*Mn+Esis*Si+Eps*P tm=167.2*(76.128*QLIU)**(-0.22721) ! 求顶渣脱硫参数 u2=8.0*1.0E-009*EXP(258208.6/(8.314*(wd-0.014*t))) Dk1=1.4*1.0E-004*EXP(-205020.0/(8.314*(wd-0.014*t))) u3=0.1*u2 Re1=Pz*w1*L/u3 Sc1=u3/(Pz*Dk1) Sh1=0.664*Sc1**(1.0/3.0)*Re1**(1.0/2.0) Km1=Sh1*Dk1/L ! 求硫的分配系数与时间的关系 write(*,*) km1 Xfeo=(FeO0*Ws0/72.0)/(FeO0*Ws0/72.0+SiO20*ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40+(CaO0*Ws0+Ip*ZT*(CaOp+CaC2p*7/8))/56.0) XsiAlP=(SiO20*Ws0/60.0+AL2O30*Ws0/102.0)/(FeO0*Ws0/72.0+SiO20*Ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40.0+(CaO0*Ws0+Ip*ZT*(CaOp+CaC2p*7.0/8.0))/56.0) Xcamnmg=(MgO0*Ws0/40.0+(CaO0*Ws0+Ip*ZT*(CaOp+CaC2p*7.0/8.0))/56.0)/(FeO0*Ws0/72.0+SiO20*ws0/60.0+AL2O30*WS0/102.0+MgO0*Ws0/40.0+(CaO0*Ws0+Ip*ZT*(CaOp+CaC2p*7.0/8.0))/56.0) Afeo=0.14935*Xfeo**0.936719*XsiALP**(-2.83381)*Xcamnmg**0.114412 Rjd=(CaO0*Ws0+Ip*ZT*(CaOp+CaC2p*7.0/8.0)+0.69*MgO0*Ws0)/(0.93*SiO20*Ws0+0.18*Al2O30*Ws0) Ls=10**(Q-6.929+1.39*Rjd+5384.0/(wd-0.0140*t))/(Afeo) xx=-((a*a0*Pz)/Wm)*Km1*Ls d(1)=xx*(y(1)*EXP(-tm/ZT)-((S0*Ws0+(S00-Y(1)*EXP(-tm/ZT))*Wm)/(Ws0+Ip*Yi*t))/Ls) write(*,*) d(1),Rjd,LS end |
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