| 查看: 406 | 回复: 0 | ||
[求助]
求大神帮助,急
|
|
!放热率计算 PROGRAM MAIN !数组定义(曲轴转角,放热率,已燃燃料百分数,温度,压力,压升率……) DIMENSION AA(87),QED(87),X0(88),T(87),PD(87),AL(87),QA(87),AD(87),WD(87),QW(87),QE(87),V(87),WF(87) !压力数据输入 !其他数据输入 DATA NN,N1,N2,AN3,AN4,AN5,N6,N7,C1,DCA,S0,S1,S2,S3,GC,GH,GO,D,R,DL,& OM,RR,DN,AP,AB,GE,Z1,HU,TW,T1,T2,VV,A1,A2,A3,A4,A5,A6& /87,6,36,2.0,1.0,2.0,0,5,-16.0,0.0,1.0,0.0,9.80665E+03,0.0,0.86,0.13,0.01,& 0.093,0.051,0.168,0.25395E-04,0.05,3614,3.14159,18.1,13.984,4,41868.0,& 400.0,455.0,420.0,0.001,4.678,0.687232E-06,& -0.60683E-07,4.7513,0.1199E-02,-0.14232E-06/ !压力光顺 DIMENSION X(87),Y(87),A(20),P0(87),PP(87) DOUBLE PRECISION X,Y,A,DT1,DT2,DT3,B,T,U DATA P0/37.87,41.62,45.40,49.43,52.78,56.20,57.78,58.70,59.55,59.90,& 60.37,60.50,61.11,60.91,61.10,62.47,68.60,74.81,82.82,89.19,& 91.43,94.02,90.22,93.49,91.88,89.70,89.23,85.95,84.42,81.28,& 79.45,76.92,73.19,71.02,68.31,65.51,60.18,54.34,49.50,45.16,& 40.74,37.27,34.03,30.83,28.51,25.74,23.68,21.91,20.06,18.76,& 17.33,15.68,14.66,13.92,12.37,11.66,10.78,9.9366,9.4113,8.6481,& 7.9915,7.4662,7.0395,6.5060,6.5306,5.8617,5.3365,5.0205,5.1806,4.8112,& 4.1259,4.1259,4.0357,3.6294,3.5063,3.3373,3.2108,2.9728,2.7677,2.9400,& 2.5748,2.1275,2.4065,2.4312,2.2999,2.2014,1.7705/ B=0.0 DO 15 I=1,87 X(I)=B+(I-1)*0.1 Y(I)=P0(I) 15 CONTINUE N=87 M=20 T=4.3 CALL HPIR1(X,Y,A,N,M,DT1,DT2,DT3) DO 55 I=1,87 Y(I)=A(1)+A(2)*(X(I)-T)+A(3)*(X(I)-T)**2+A(4)*(X(I)-T)**3+A(5)*(X(I)-T)**4+A(6)*(X(I)-T)**5+A(7)*(X(I)-T)**6+A(8)*(X(I)-T)**7+A(9)*(X(I)-T)**8& +A(10)*(X(I)-T)**9+A(11)*(X(I)-T)**10+A(12)*(X(I)-T)**11+A(13)*(X(I)-T)**12+A(14)*(X(I)-T)**13+A(15)*(X(I)-T)**14& +A(16)*(X(I)-T)**15+A(17)*(X(I)-T)**16+A(18)*(X(I)-T)**17+A(19)*(X(I)-T)**18+A(20)*(X(I)-T)**19 PP(I)=Y(I) 55 CONTINUE !曲轴转角 AA(1)=C1+DCA DO 10 I=2,NN IF(I-N1)2,2,3 3 IF(I-N2)4,4,2 2 AA(I)=AA(I-1)+AN3*S0 GOTO 10 4 AA(I)=AA(I-1)+AN4*S0 10 CONTINUE GE=GE*AN5/Z1/60.0/DN !循环供油量 VC=AP*R*D*D/2.0/(AB-1.0) !余隙容积 AF=OM*0.21/GE/(1.0+RR)/(GC/12.0+GH/4.0-GO/32.0) !过量空气系数 AME=0.21/29.09/(GC/12.0+GH/4.0-GO/32.0) DO 40 I=1,NN QED(I)=0.0 X0(I)=0.0 T(I)=0.0 PD(I)=0 AL(I)=0.0 QA(I)=0.0 AD(I)=0.0 WF(I)=0.0 QE(I)=0.0 QW(I)=0.0 WD(I)=0.0 40 V(I)=0.0 DO 50 I=1,NN V(I)=AP*D*D/4.0*(R*(1.0-COS(AP*AA(I)/180.0))+DL-SQRT(DL*DL-R*R*SIN(AP*AA(I)/180.0)**2))+VC !汽缸容积 PP(I)=(PP(I)+S1+S3)*S2 !缸内压力 50 CONTINUE DO 60 I=2,NN PD(I)=(PP(I)-PP(I-1))/(AA(I)-AA(I-1))/10000.0 !压升率 60 AL(I)=AL(I-1)+(PP(I)+PP(I-1))*(V(I)-V(I-1))/2.0 !做功 X0(1)=0.0 DO 80 I=1,NN 90 T(I)=AF*(1.0+RR)*PP(I)*V(I)/(AF*(1.0+RR)+AME*X0(I))/831.4/OM !缸内温度 CA=A1+A2*T(I)+A3*T(I)*T(I) CB=A4+A5*T(I)+A6*T(I)*T(I) UU=((AF-X0(I))*CA+((1.0+AME)*X0(I)+AF*RR)& *CB)*PP(I)*V(I)/848.0/(AF*(1.0+RR)+AME*X0(I)) IF(I.EQ.2)UI=UU IF(I.LT.3)GOTO 82 QA(I)=UU-UI+(AL(I)-AL(2))/426.936 IF(I.LE.4)GOTO 82 AD(I)=(QA(I)-QA(I-1))/(AA(I)-AA(I-1)) IF(QA(I).LE.0.0)WF(I)=2.28E+07*2.0*DN*R*29.09*PP(I)/(9.91*30.0*0.528*848.0) IF(QA(I).GT.0.0)WF(I)=29.09E+07*PP(I)/9.81/848.0/0.528*& (2.28*2.0*R*DN/30.0+3.24*1.0E-03*(AP*D*D/2.0*R+VC)*T(N7)*(PP(I)-& PP(N7)*((V(N7)/V(I))**1.369))/PP(N7)/V(N7)) IF(WF(I).LT.0.0)WF(I)=-WF(I) WD(I)=(1.099E-05*WF(I)**0.8/(D**0.2)/(T(I)**0.548))*(4.0& *V(I)/D*(TW-T(I))+AP*D*D/4.0*(T1+T2-2.0*T(I)))/(2.16E+04*DN) QW(4)=0.0 QW(I)=QW(I-1)+WD(I)*(AA(I)-AA(I-1)) QED(I)=AD(I)-WD(I) QE(4)=0.0 QE(I)=QE(I-1)+QED(I)*(AA(I)-AA(I-1)) S=QE(I)/GE/HU YY=ABS((S-X0(I))/S) IF(YY.LE.VV)GOTO 81 X0(I)=S GOTO 90 81 X0(I)=S 82 X0(I+1)=X0(I) 80 CONTINUE IF(N6.NE.1)GOTO 300 PPI=AL(NN)/(V(NN)-VC) ANI=AL(NN)*DN/60.0/75.0/AN5 GI=GE*DN*60/ANI/AN5 EI=632.3/GI/HU 300 CONTINUE DO 305 I=1,NN PP(I)=PP(I)/10000.0 305 CONTINUE !数据输出 OPEN(08,FILE='E:\FOR77\DAT.TXT',STATUS='NEW') WRITE(08,900)(AA(I),PD(I),X0(I),QED(I),PP(I),T(I),I=1,NN) WRITE(*,900)(AA(I),PD(I),X0(I),QED(I),PP(I),T(I),I=1,NN) 900 FORMAT(1X,F7.2,2E15.6,2F15.6,F12.1) CLOSE(08) END PROGRAM MAIN !压力光顺子例行程序 SUBROUTINE HPIR1(X,Y,A,N,M,DT1,DT2,DT3) DIMENSION X(N),Y(N),A(M),S(20),T(20),B(20) DOUBLE PRECISION X,Y,A,S,T,B,DT1,DT2,DT3,Z,D1,P,C,D2,G,Q,DT DO 5 I=1,M 5 A(I)=0.0 IF (M.GT.N) M=N IF (M.GT.20) M=20 Z=0.0 DO 10 I=1,N 10 Z=Z+X(I)/N B(1)=1.0 D1=N P=0.0 C=0.0 DO 20 I=1,N P=P+(X(I)-Z) C=C+Y(I) 20 CONTINUE C=C/D1 P=P/D1 A(1)=C*B(1) IF (M.GT.1) THEN T(2)=1.0 T(1)=-P D2=0.0 C=0.0 G=0.0 DO 30 I=1,N Q=X(I)-Z-P D2=D2+Q*Q C=Y(I)*Q+C G=(X(I)-Z)*Q*Q+G 30 CONTINUE C=C/D2 P=G/D2 Q=D2/D1 D1=D2 A(2)=C*T(2) A(1)=C*T(1)+A(1) END IF DO 100 J=3,M S(J)=T(J-1) S(J-1)=-P*T(J-1)+T(J-2) IF (J.GE.4) THEN DO 40 K=J-2,2,-1 40 S(K)=-P*T(K)+T(K-1)-Q*B(K) END IF S(1)=-P*T(1)-Q*B(1) D2=0.0 C=0.0 G=0.0 DO 70 I=1,N Q=S(J) DO 60 K=J-1,1,-1 60 Q=Q*(X(I)-Z)+S(K) D2=D2+Q*Q C=Y(I)*Q+C G=(X(I)-Z)*Q*Q+G 70 CONTINUE C=C/D2 P=G/D2 Q=D2/D1 D1=D2 A(J)=C*S(J) T(J)=S(J) DO 80 K=J-1,1,-1 A(K)=C*S(K)+A(K) B(K)=T(K) T(K)=S(K) 80 CONTINUE 100 CONTINUE DT1=0.0 DT2=0.0 DT3=0.0 DO 120 I=1,N Q=A(M) DO 110 K=M-1,1,-1 110 Q=Q*(X(I)-Z)+A(K) DT=Q-Y(I) IF (ABS(DT).GT.DT3) DT3=ABS(DT) DT1=DT1+DT*DT DT2=DT2+ABS(DT) 120 CONTINUE RETURN END 编译出现一个错误 F:\xitao\shi\1.f90(45) : Error: The shapes of the array expressions do not conform. [Y] Y(I)=A(1)+A(2)*(X(I)-T)+A(3)*(X(I)-T)**2+A(4)*(X(I)-T)**3+A(5)*(X(I)-T)**4+A(6)*(X(I)-T)**5+A(7)*(X(I)-T)**6+A(8)*(X(I)-T)**7+A(9)*(X(I)-T)**8& 求指导~谢谢啦 |
» 猜你喜欢
基金申报
已经有3人回复
国自然申请面上模板最新2026版出了吗?
已经有9人回复
溴的反应液脱色
已经有6人回复
纳米粒子粒径的测量
已经有7人回复
常年博士招收(双一流,工科)
已经有4人回复
推荐一本书
已经有10人回复
参与限项
已经有5人回复
有没有人能给点建议
已经有5人回复
假如你的研究生提出不合理要求
已经有12人回复
萌生出自己或许不适合搞科研的想法,现在跑or等等看?
已经有4人回复
找到一些相关的精华帖子,希望有用哦~
这样的rna能不能做克隆,求大神分析。。。急。。。
已经有14人回复
求一篇毕业论文 急 猴肠道中需养菌和兼性厌氧菌的分离和鉴别
已经有3人回复
急急急!!!请教投过chemical commun. 的大神
已经有12人回复
rt-pcr图,请大神们帮助分析一下,急。。。谢谢。。。
已经有20人回复
急急急,哪位大神帮忙分析一下透镜图~~看不懂~汗一个先
已经有20人回复
pvp(聚维酮)可以作为食品的添加剂吗?求帮助,急
已经有19人回复
求有关化学的专业介绍,徘徊的人,万分感谢~
已经有5人回复
紧急求助!!离子交换色谱的两个小问题
已经有7人回复
matlab作业哪位大神麻烦给做一下,十万火急,周五之间要交
已经有3人回复
急!加拿利海枣长虫,
已经有3人回复
科研从小木虫开始,人人为我,我为人人












回复此楼
点击这里搜索更多相关资源