Process Calculations Supplementary Notes Material Balance with Chemical Reactions Dr. Maher Al-Jabari Think of Environmental applications! Think of related chemistry topics and Terminology? Think of Form of material balance equation Input + Generation = Output + Consumption Review and Definitions • • • • • • • Stoichiometry Stoichiometric Coefficient / Ratio Stoichiometry proportions Limiting Reactant Excess Reactant Fractional Excess Fractional Conversion Reaction Equilibrium • • • • • Reversibility? Reversible versus irreversible reactions Equilibrium Reaction Yield Multiple Reactions – Reaction Selectivity Chemical Equation-1 n1 A + n2 B n3 C + n4 D Contains qualitative and quantitative information Stoichiometry: theory of proportions in reactions What are the stoichiometric coefficients in the above equation? Stoichiometric Ratio of A/B is n1 / n 2 Example C7H16 + 11 O2 7 CO2 + 8 H2O Check number of atoms in both sides of the equation – reaction balance? Stoichiometric Ratio of O2 / C7H16 is With masses given– change to moles… 11/1 = 11 Chemical Equation-2 Same Example C7H16 + 11 O2 7 CO2 + 8 H2O If a feed contains 1 mole C7H16 of and 11 mole of O2 The reactant present: choose? a) with excess oxygen b) in Stoichiometry proportions c) none of the above The reaction proceeds to completion = all reactants are consumed I f a feed contains 1 mole C7H16 of and 16 mole of O2 Which is the limiting reactant (run out)? Which is the excess reactant? What is the fractional excess (of the …………. Reactant)? Fractional Excess Same Example C7H16 + 11 O2 7 CO2 + 8 H2O Fractional Excess of …….. = (16-11)/11 Fractional Excess = moles of excess reactant in the feed – moles of excess reactant needed to react with all moles of the limiting reactant moles of excess reactant needed to react with all moles of the limiting reactant Fractional Conversion Same Example C7H16 + 11 O2 7 CO2 + 8 H2O Fractional Conversion f (for incomplete reaction) f = moles reacted of A moles fed of A If the feed contains 10 moles of C7H16 and if fractional conversion is 80%. What is The amount of C7H16 reacted = The amount of C7H16 leaving (unreacted) = Reaction Extent (x) Starting with (moles): 20 + 50 50 Reacted (Known) Reacted (calculated) 30/2 At the end 30 30/2 5 20 65 Reaction Extent (x) Try this question at home – Reaction Stoichiometry Reaction Equilibrium Distinguish between Chemical Equilibrium (final amounts / composition) Reaction Kinetics (Time needed) What is the difference between reversible and irreversible reactions. What is the Equilibrium Constant K = f (Temperature) Equilibrium Calculations For a sample reaction – extent analysis – x • Given Initial Moles of Reactants (and Products) • Suppose x for reaction • Determine Final (Equilibrium) moles of all– (reactants and products) • Estimate total number of moles • Determine Composition of each reactant and product • Substituting in expression for K • Solve for extent x – and choose the reasonable answer. • Determine number of moles of each reactant and product • Estimate other required variables e.g. fractional conversion • See example 4.6.2 • Try this reaction on board Example- Follow on Board in the class CO is toxic, it can be converted to CH3OH by reaction with hydrogen For a reactor containing initially equimolar amounts of CO and H2 but no CH3OH, the following reversible reaction occur: CO + 2 H2 CH3OH The reaction proceeds till reaching equilibrium, with K = 1.11 Calculate a) the molar composition of the components in the final products b) The fractional conversion of CO Solve…. Answers: X = 0.156 (& 0.844?) and YCO= 0.5, YH2= 0.408 …etch f = 0.156 Try this question at home - Reaction Equilibrium For the reaction At T = 1300 K, K = 0.55 Reaction Design aims at - Maximizing rate of desired reaction (1) - Minimizing rate of undesired reactions (2 and 3) Maximize Profit Thus, define Yield and Selectivity Yield Definitions may vary: Moles of desired product / moles of reacted (Fed or consumed) Example- Follow on Board in the class Given Fractional conversion of CH4 = 95% Fractional yield of HCHO = 90% Determine a) Output Compositions b) Selectivity of HCHO relative to CO2 HW 3 – Mass balance with Reactions 40 43 46 57 Try this question at home - Balance on Atomic and Molecular Species • What are the types of Balances you can make? – Balance on total masses: input = output – Balances on any of the molecules – Form for each? Input + Generation? = Output + Consumption? – What about balances for H-atoms and C-atoms? input = output Atoms can neither be created no destroyed? In a …. Reaction Hydrogen Balance – H versus H2 balance Follow example-text in the book How many moles of C in C2H6? How many moles of H in C2H6? What about this balance? Atomic Balances – Simple? • What is the type of this balance - Molecular or Atomic Balances? Independent Species • For non-reactive systems No. of Equations = No. of independent Species? • Are Oxygen and Nitrogen in air independent species? • Read Analyze Independent Species The process is Physical-chemical? Analysis Techniques Mass Balance Problems with Reactions Three methods 1. Molecular species balances (approach with no reactions) 2. Atomic species 3. Extent of Reaction Do they lead to SAME results? Choose the most convenient - which for which? Based on problem type (or your convenience?) Cases: one reaction, equilibrium, multiple reactions See example 4.7.1 Read Sections 4.7 c, d and e – and practice methods Independent Reactions/Equations Are these 2 equations independent For Reactive systems: the degree of freedom analysis must count only independent reactions Molecular Species Balances Read p.128 Atomic Species Balances Read p.129 Extent of Reaction - Balance Read p.130 Follow the book – in three methods - Notice the common starting steps (for methane and nitrogen) - Compare simplicity. Combustion Reactions-1 Fuel + O CO2, CO, H2O & SO2 (NOx at High T) + Heat Comment on Environment – Energy Types of Fuel - Coal - C (with H and S content) - Fuel Oil - Natural Gas (mainly CH4) - Liquefied petroleum gas (e.g. C3H12) Types of Combustion reactions: complete versus incomplete (partial) combustion Combustion Reactions-2 Oxygen Supply From air 79% N2 and 21% O2 N2/O2 = 3.76 (dependent species?) Also contains humidity (water vapor). The product gas – Flue gases- Stack gases Dry basis: without including water vapor in calculations Wet basis: with including water vapor in calculations How you convert from given basis to another – Recall conversion between mass and molar composition! See example 4.8.1 – can be a quiz See example 4.7.1 on combustion Combustion Process Fuel - Expensive Limiting Combustion Chamber air (free) excess Theoretical air? %excess air? Example – Methane Combustion Flue gases CO2 CO H2O N2 Unreacted Fuel NOx (at High T) SO2 (from sulfur) Use wet or dry basis Combustion Process – Air Supply Fuel Combustion Chamber Flue gases air C CO2 and H H2O Combustion Calculations Given Find Fuel and entering air Composition of Flue gases Composition of Flue gases Find Fuel and air rate, excess ratio Similar Mass Balance Calculations - Use Molecular Species Balance - Use Atomic Species Balance (more convenient with multiple reactions) Example – Combustion of Ethane – Follow on the board Find Composition of Flue gases In class using molecular species balance At home using atomic species balance If nitrogen is not withdrawn from the system (purged) At the same rate it enters the process Where shall it go? HW 4 – Mass balance with Reactions Read section 4.9 P.151 64 69 73 68 70