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matlab擬合反應(yīng)動力學(xué) 已有2人參與
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剛?cè)腴Tmatlab的小白,最近想做反應(yīng)的動力學(xué),按照B站up主的視頻自己寫了一段代碼,但是運行總是出問題: 錯誤使用 odearguments (第 93 行);FUNC 必須返回列向量,出錯 ode45 (第 115 行),odearguments(FcnHandlesUsed, solver_name, ode, tspan, y0, options, varargin); 出錯 Kinetics>fun (第 67 行),[t,x]=ode45(@func,tspan,x0,[],k); 出錯 lsqnonlin (第 218 行),initVals.F = feval(funfcn{3},xCurrent,varargin{:});出錯 Kinetics (第 18 行),lsqnonlin(@fun,k0,lb,ub,[],yexp);%非線性最小二乘法。原因:Failure in initial objective function evaluation. LSQNONLIN cannot continue. 下面是我寫的代碼,讀取的Excel表格里有5列*7行的實驗數(shù)據(jù),勞煩大佬幫我瞅瞅哪里需要改動,萬分感謝。 function Kinetics %反應(yīng)一:A+B=C+M %r=k*XA*XB-K*XC*XM %反應(yīng)二:A+C=D+M %r=K*XA*XC-K*XD*XM %反應(yīng)三:B+C=E+M %r=K*XB*XC-K*XE*XM %XM=0.175 clc clear all; global a b tspan=[0.5 1 4 6 8 12 16]; yexp=xlsread('reaction.xls'); k0=[0.1 0.01 0.01 0.001 0.001 0.001];%參數(shù)初值 lb=[0 0 0 0 0 0];%下邊界 ub=[+inf +inf +inf +inf +inf +inf];%上邊界 [k,resnorm,residual,exitflag,output,lambda,jacobian]=... lsqnonlin(@fun,k0,lb,ub,[],yexp);%非線性最小二乘法 tspan=[0.5 1 4 6 8 12 16]; a=1; b=a+6; x0=yexp(a, ;%積分初值[t,x]=ode45(@func,tspan,x0,[],k); t1=linspace(0.5,16,200); ya1=spline(t,x(:,1),t1);%動力學(xué)計算得到的點進(jìn)行樣條插值 ya2=spline(t,x(:,2),t1); ya3=spline(t,x(:,3),t1); ya4=spline(t,x(:,4),t1); ya5=spline(t,x(:,5),t1); for m=1:7 for n=1:5 yy(a+m-1,n)=x(m,n);%每一次的值存入yy矩陣 end end figure(1) plot(tspan,yexp(a:b,1),'k^',t1,ya1,'k-',tspan,yexp(a:b,2),'ro',t1,ya2,'r-',tspan,yexp(a:b,3),'bd',t1,ya3,'b-',... tspan,yexp(a:b,4),'g*',t1,ya4,'g-',tspan,yexp(a:b,5),'yp',t1,ya5,'y-'); legend('','A濃度','','B濃度','','C濃度','','D濃度','','E濃度'); xlabel('t(h)');ylabel('濃度(mol/L)');title('170℃ 0.1wt%催化劑'); t1=linspace(0.5,16,200); z1=spline(t,yy(1:7,1),t1); h1=spline(t,yy(1:7,2),t1); s1=spline(t,yy(1:7,3),t1); b1=spline(t,yy(1:7,4),t1); u1=spline(t,yy(1:7,5),t1); xlswrite('result.xls',[t1' z1' h1' s1' b1' u1'],'sheet1'); xlswrite('result.xls',residual,'sheet2'); Ne = length(yexp(:,2)); %模型適定性判別 Np = length(k); [rho2,F] = rho2_F(k,yexp,resnorm,Ne,Np); ci=nlparci(k,residual,jacobian) fprintf('\t k1,0=%.1f ± %.4f\n',k(1),ci(1,2)-k(1)); fprintf('\t k2,0=%.1f ± %.4f\n',k(2),ci(2,2)-k(2)); fprintf('\t k3,0=%.1f ± %.4f\n',k(3),ci(3,2)-k(3)); fprintf('\t k4,0=%.1f ± %.4f\n',k(4),ci(4,2)-k(4)); fprintf('\t k5,0=%.1f ± %.4f\n',k(5),ci(5,2)-k(5)); fprintf('\t 殘差平方和:%.3f\n',resnorm) fprintf('\t 實驗點數(shù)和自由度分別為 Ne = %d和 Np = %d\n',Ne,Np) fprintf('\t 決定性指標(biāo)ρ^2: %.4f\n',rho2) fprintf('\t F比: %.3f\n\n',F) %================================================================================= function f=fun(k,yexp) f=[]; tspan=[0.5 1 4 6 8 12 16]; a=1; x0=yexp(a, ;[t,x]=ode45(@func,tspan,x0,[],k) d=a+6; yc1=x(:,1); yc2=x(:,2); yc3=x(:,3); yc4=x(:,4); yc5=x(:,5); f11=yexp(a:d,1)-yc1; f12=yexp(a:d,2)-yc2; f13=yexp(a:d,3)-yc3; f14=yexp(a:d,4)-yc4; f15=yexp(a:d,5)-yc5; ff=[f11 f12 f13 f14 f15]; f=[f;ff]; %================================================================================= function dxdt=func(t,x,k) r1=-k(1)*x(1)*x(2)-k(2)*x(1)*x(3)+k(4)*x(3)*0.175+k(5)*x(4)*0.175; r2=-k(1)*x(1)*x(2)-k(3)*x(2)*x(3)+k(4)*x(3)*0.175+k(6)*x(5)*0.175; r3=k(1)*x(1)*x(2)+k(5)*x(4)*0.175+k(6)*x(5)*0.175-k(2)*x(1)*x(3)-k(3)*x(2)*x(3)-k(4)*x(3)*0.175; r4=k(2)*x(1)*x(3)-k(5)*x(4)*0.175; r5=k(3)*x(2)*x(3)-k(6)*x(5)*0.175; dxdt=[r1 r2 r3 r4 r5] %================================================================================= function [rho2,F] = rho2_F(k,yexp,s,Ne,Np) y=yexp.^2; sy = sum(y( );rho2 = 1 - s/sy; %rho2: 決定性指標(biāo) F = (sy - s)*(Ne-Np)/(Np*s); %F:F比 |


送紅花一朵 |
每列數(shù)據(jù)對應(yīng)的變量就是五中物質(zhì)的濃度變化:x1 x2 x3 x4 x5,就是后面的微分速率方程里面的x1 x2 x3 x4 x5 發(fā)自小木蟲Android客戶端 |
鐵桿木蟲 (職業(yè)作家)
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參考下: Root of Mean Square Error (RMSE): 0.0602102835008095 Sum of Squared Residual: 0.108758347177436 Correlation Coef. (R): 0.963380309380527 R-Square: 0.928101620502121 Parameter Best Estimate -------------------- ------------- k1 0.0431976858691231 k2 0.0204925345429154 k4 8.27595775884273E-20 k5 3.49573492337918E-16 k3 0.0313036416446144 k6 2.17399315624263E-18 |
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