Page 360 - Defrosting for Air Source Heat Pump
P. 360

356                                                          Appendices

               swatertray(j,i)=sum(watertray(:,i)); % kg
               hro(j,i)=44518+1170.36*Tro(j,i)+1.68674*Tro(j,i)^2+5.2703/
            1000*Tro(j,i)^3;
            % kJ/kg
               qr2(j,i)=kMr*(khri-hro(j,i)); % W
               s_qr2(j,i)=sum(qr2(:,i))*5; % W

            % here is the end of stage 2: frost melting without water flow to
            down circuit
            %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
                 end
               end
             end
            end
            end
            %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%

            for i=1
             for j=18:45
                % for the 18*5 seconds for the 1st Circuit
                  kmw1=mf(j-1,i)+0.0192; % 0.0192 kg stands for the mass of
            flowing water is the sum of the melting and the melted on the coil,
            kg/s
                  ksmrw=sfrost(17,i); % the total mass of water retained on
            the coil, the flowing part 0.0192 kg was neglected, kg
                  kTw1=Tw(j-1,i); %, °C
                  kTri=Tri(j,i); %, °C
                                    2
                  kRr=Rr(j,i); % (K m )/W
                  kMr=Mr(j,i); % kg/s
                  khri=hri(j,i); % kJ/kg
                 % all the input parameters in the function listed here
                  x0=[0.0042 0.0042 0.335 1200 0.001]; % mf=x(1), mr=x(2),
            Tw=x(3); qr=x(4); Tro=x(5) the values for debugging;
                  options=optimset(’display’,’off’,’MaxIter’,100000,
            ’MaxFunEvals’,20000); % number
                  [A,fval,exit]=fsolve(@(x)mystage31(x,kmw1,ksmrw,kTw1,i,
            kTri,kRr,kMr,khri),x0,options);
                  mf(j,i)=A(1); % melted water, kg/s; after this stage, mf is 0 kg/s
                  mrw(j,i)=A(2); % retained water, kg/s
                  Tw(j,i)=A(3); % retained water temperature, °C
                  qr(j,i)=A(4); % energy used in defrosting from refrigerant, W
                  Tro(j,i)=A(5); % the temperature of tube surface at exit of
            each circuit, °C

                  A
                  x00=real(A);
                  fval
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