10.37 Chemical and Biological Reaction Engineering, Spring 2007 Prof. William H. Green Lecture 16: Catalysis This lecture covers: Inorganic and enzyme catalysis and their properties; kinetics of heterogeneous catalytic reactions; adsorption isotherms, derivation of rate laws; and Langumuir-Hinshelwood kinetics What initiates the reaction? A + B → starts upon mixing B A Product Figure 1. Bi-molecular reaction in a CSTR. Temperature drastically increases reaction rate. Hot C2H6 Rxn occurs Fire Figure 2. Schematic of tube reactor. Catalyst dramatically increases reaction rate. A catalyst Figure 3. Schematic of packed bed reactor. Catalyst: Accelerates rate of reaction but is not consumed Cite as: William Green, Jr., course materials for 10.37 Chemical and Biological Reaction Engineering, Spring 2007. MIT OpenCourseWare (http://ocw.mit.edu), Massachusetts Institute of Technology. Downloaded on [DD Month YYYY]. transition state E reactants ~Ea products rxn coordinate Figure 4. Reaction diagram. rate constant: k BT ⎡ (G − Greactants ) ⎤ exp ⎢ − ts ⎥ h RT ⎣ ⎦ G = H − TS k= e − G / RT = e− H / RT e S / R no catalyst E with catalyst rxn coordinate Figure 5. Reaction diagram with and without catalyst. The reaction forms many intermediates. A catalyst lowers the energy of these intermediates. Acid/Base catalysis ROR + H 2O → 2ROH k1 ROR + H ⊕ k−1 H H ROR ⊕ k2 ROR → ROH + R ⊕ ⊕ k3 R ⊕ + H 2O → ROH + H ⊕ 10.37 Chemical and Biological Reaction Engineering, Spring 2007 Prof. William H. Green Lecture 16 Page 2 of 4 Cite as: William Green, Jr., course materials for 10.37 Chemical and Biological Reaction Engineering, Spring 2007. MIT OpenCourseWare (http://ocw.mit.edu), Massachusetts Institute of Technology. Downloaded on [DD Month YYYY]. H ROR , R ⊕ QSSA ⊕ ⎡ H ⎤ d ⎢ ROR ⎥ H ⊕ ⎦ = k ⎡ H + ⎤ ROR − (k + k ) ⎡ ROR ⎤ O≈ ⎣ [ ] ⎢ ⎥ − 1⎣ 1 2 ⎦ dt ⎣ ⊕ ⎦ ⎡ H ⎤ k1 ⎡⎣ H + ⎤⎦ [ ROR ] = ⎢ ROR ⎥ ⊕ k k + −1 2 ⎣ ⎦ QSSA d [ ROH ] dt ⎡ H ⎤ = 2k2 ⎢ ROR ⎥ ⎣ ⊕ ⎦ QSSA d [ ROH ] 2k1k2 ⎡⎣ H + ⎤⎦ [ ROR ] = r ≈ dt k−1 + k2 rA ∼ [ A] rA ∼ [ catalyst ] (where ∼ denotes “proportional to”) N + ⎡ H ⎤ ⎡⎣ H + ⎤⎦ + ⎢ R O R ⎥ + ⎡⎣ R + ⎤⎦ = H added = ⎡⎣ H + ⎤⎦ added ⊕ V ⎣ ⎦ ⎛ k [ ROR ] ⎞ k1k2 [ ROR ] ⎡⎣ H + ⎦⎤ ⎜1 + 1 = ⎣⎡ H + ⎦⎤ + ⎟ ⎜ ⎟ added k1 + k2 k3 (k−1 + k2 ) [ H 2O ] ⎠ ⎝ r= r= keff [ ROR ] ⎡⎣ H + ⎤⎦ 1+ k [ ROR ] added k [ catalyst ] [ A] 1+ k A [ A] + k B [ B ] + ... All the things that the catalyst binds to Langmuir-Hinshelwood: all reagents bind to catalyst, bound forms react Eley-Rideal: one reagent binds, 2nd reagent reacts with bound form dN A = VrA dt f ([ A] , ⎡⎣ H ⎤⎦ ) + 10.37 Chemical and Biological Reaction Engineering, Spring 2007 Prof. William H. Green Lecture 16 Page 3 of 4 Cite as: William Green, Jr., course materials for 10.37 Chemical and Biological Reaction Engineering, Spring 2007. MIT OpenCourseWare (http://ocw.mit.edu), Massachusetts Institute of Technology. Downloaded on [DD Month YYYY]. moles dN A = ( area of dt metal ) rA′′ area s f (θ A ) where θA = N A bound N total sites on surface 10.37 Chemical and Biological Reaction Engineering, Spring 2007 Prof. William H. Green Lecture 16 Page 4 of 4 Cite as: William Green, Jr., course materials for 10.37 Chemical and Biological Reaction Engineering, Spring 2007. MIT OpenCourseWare (http://ocw.mit.edu), Massachusetts Institute of Technology. Downloaded on [DD Month YYYY].