The CSTR given in the figure is fed while running with a feed concentration (Cao) of 0.5mol/m3 in a sedentary state its concentration was suddenly increased to 1.0mol/m3. All other process variables ( T,V and F) are constant. For this system: a. Develop a dynamic model for the concentration in the reactor (CA). The reaction rate term is given by defined by: Ta (1+k2Cla) b. Obtain a transfer function (G(s)) that shows the relationship between Ca and Cao. Dec. c. Obtain the dynamic response of Ca(t) for the step change that occurs in Cao. Using the following data Find the new steady state value of Ca. V=2.0m3F=1.0m3/hk.=1.0h1k2=1.0m3/mol ekilde verilen CSTR, yatkn halde 0,5mol/m3 'lk bir besleme konsantrasyonu (CA0) ile altrimaktayken besleme konsantrasyonu aniden 1,0 mol/m 3 'e ikarilmitir. Dier tm proses degikenleri (T, V ve F) sabittir. Bu sistem iin: a. Reaktrdeki (CA) konsantrasyon iin dinamik bir model gelitiriniz. Reaksiyon hz terimi u ekilde tanmlanmtr: rA=(1+k2CA)k1cA b. CA ve CA0 arasindaki ilikiyi gosteren bir transfer fonksiyonu (G(s)) elde ediniz. c. CA0 'da meydana gelen adm degiikligii iin CA(t) 'nin dinamik yantn elde ediniz. Aadaki verileri kullanarak CA 'nn yeni kararl durum degerini bulunuz. V=2.0m3F=1.0m3/hk1=1.0h1k2=1.0m3/mol The CSTR given in the figure is fed while running with a feed concentration (Cao) of 0.5mol/m3 in a sedentary state its concentration was suddenly increased to 1.0mol/m3. All other process variables ( T,V and F) are constant. For this system: a. Develop a dynamic model for the concentration in the reactor (CA). The reaction rate term is given by defined by: Ta (1+k2Cla) b. Obtain a transfer function (G(s)) that shows the relationship between Ca and Cao. Dec. c. Obtain the dynamic response of Ca(t) for the step change that occurs in Cao. Using the following data Find the new steady state value of Ca. V=2.0m3F=1.0m3/hk.=1.0h1k2=1.0m3/mol ekilde verilen CSTR, yatkn halde 0,5mol/m3 'lk bir besleme konsantrasyonu (CA0) ile altrimaktayken besleme konsantrasyonu aniden 1,0 mol/m 3 'e ikarilmitir. Dier tm proses degikenleri (T, V ve F) sabittir. Bu sistem iin: a. Reaktrdeki (CA) konsantrasyon iin dinamik bir model gelitiriniz. Reaksiyon hz terimi u ekilde tanmlanmtr: rA=(1+k2CA)k1cA b. CA ve CA0 arasindaki ilikiyi gosteren bir transfer fonksiyonu (G(s)) elde ediniz. c. CA0 'da meydana gelen adm degiikligii iin CA(t) 'nin dinamik yantn elde ediniz. Aadaki verileri kullanarak CA 'nn yeni kararl durum degerini bulunuz. V=2.0m3F=1.0m3/hk1=1.0h1k2=1.0m3/mol