Question: II. Write a program that computes the theoretical flame temperature when a mixture of methane, propane, n-butane, and n-pentane (0% to 100% mole methane in

 II. Write a program that computes the theoretical flame temperature when

a mixture of methane, propane, n-butane, and n-pentane (0% to 100% molemethane in 5 % increments: 0 to 100 mol% propane in 5%increments: 0% to 100% mole n-butane in 5 % increments) at 25C

II. Write a program that computes the theoretical flame temperature when a mixture of methane, propane, n-butane, and n-pentane (0% to 100% mole methane in 5 % increments: 0 to 100 mol% propane in 5% increments: 0% to 100% mole n-butane in 5 % increments) at 25C is burned with excess air (0% to 100% excess in 5% increments) preheated to preheated to (50C to 200C in 10C increments) TABLE 1-1. REPRESENTATIVE PFAUDLER CSTR/BATCH REACTOR SIZES AND 2004 PRICES Volume Price Volume Price $85,000 $150.000 5 Gallons (wastebasket) 50 Gallons (garbage can 500 Gallons (Jacuzzi) $29.000 1000 Gallons (2 Jacuzzis) $38.000 4000 Gallons (8 Jacuzzis) $70,000 8000 Gallons (gasoline tanker) $280,000 TABLE 5-3 TYPICAL CYCLE TIME FOR A BATCH POLYMERIZATION PROCESS Time (h) Batch operation times Activity 1. Charge feed to the reactor and agitate, ly 2. Heat to reaction temperature, te 3. Carry out reaction, IR 4. Empty and clean reactor, 0.5-2.0 0.5-2.0 (varies) 1.5-3.0 Total time excluding reaction 2.5-7.0 TABLE 2-6 REPRESENTATIVE PFAUDLER CSTR/BATCH REACTOR SIZES AND PRICES Volume Price 20 dm (Waste Basket) $30,000 200 dm (Garbage Can) $40,000 2,000 dm3 (Jacuzzi) $75,000 30,000 dm3 (Gasoline Tanker) $300,000 Doesn't include instrumentation costs

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