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Give step-by-step solution with explanation and final answer: (give me answer without using bullet points)Derive the rate expression for a solid-catalyzed reaction following the Eley-Rideal mechanism, hers the ga: phase reactant A colices dict withthe adsorbed species I - § oor the produc. The drain ist asus that the saface reactions the rate sep and {hat adsrption follows a Lange sohar, knKuPaPy Tras Re PA = Tp, + KB Sketch the Levenspiel plot of Fa — 7.4 versus conversion X for an autocatalyti reaction deny the aptml reactor confueaton consisting of a CSTR operating at the conversion corresponding othe minimum at reciprocal, followed by a PPR to achive the final Osta the vm reduction percentage compared oa sla FR Establish the integrated rat law fo sscond-orde reversible reaction A.» J cared out in arabe woe batch reactor The solution eqs he sibstituion of the volume expansion factor 4 nto the concentration terms Cg = N.x/V. leading ta transcendental integral function of conversion X. ven [F dX _f* (1+ ex X)dx “ou Sv mn x Rare Analyze the Kintic cat fom a iret reactor test povided below detain the teaction order vith respect othe paris pressure of Hycrogen Pir The at is messed at low comarsion eure th conceiration of reactants reais efectiely constant across tho catalyst bed [Pusfatm) T15 T5045 [60 [75 | (=r... (mol/g 3) [0.045 [0.064 | 0.078 | 0.091] 0.107] Caloitethe expan using no fnr regression.

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Give step-by-step solution with explanation and final answer: (give me answer without using bullet points)Uploaded ImageDerive the rate expression for a solid-catalyzed reaction following the Eley-Rideal mechanism, hers the ga: phase reactant A colices dict withthe adsorbed species I - § oor the produc. The drain ist asus that the saface reactions the rate sep and {hat adsrption follows a Lange sohar, knKuPaPy Tras Re PA = Tp, + KB Sketch the Levenspiel plot of Fa — 7.4 versus conversion X for an autocatalyti reaction deny the aptml reactor confueaton consisting of a CSTR operating at the conversion corresponding othe minimum at reciprocal, followed by a PPR to achive the final Osta the vm reduction percentage compared oa sla FR Establish the integrated rat law fo sscond-orde reversible reaction A.» J cared out in arabe woe batch reactor The solution eqs he sibstituion of the volume expansion factor 4 nto the concentration terms Cg = N.x/V. leading ta transcendental integral function of conversion X. ven [F dX _f* (1+ ex X)dx “ou Sv mn x Rare Analyze the Kintic cat fom a iret reactor test povided below detain the teaction order vith respect othe paris pressure of Hycrogen Pir The at is messed at low comarsion eure th conceiration of reactants reais efectiely constant across tho catalyst bed [Pusfatm) T15 T5045 [60 [75 | (=r... (mol/g 3) [0.045 [0.064 | 0.078 | 0.091] 0.107] Caloitethe expan using no fnr regression.

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Asked by: Francis
Created at: 2026-01-17 15:21:27

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Let's solve the last part: **Analyze the kinetic data and calculate the exponent n using non-linear regression.** We are given: - \( -r_A = k' P_{H_2}^n \) - Experimental data: | \( P_{H_2} \) (atm) | 1.5 | 3. | 4.5 | 6. | 7.5 | |---------------------|-----|-----|-----|-----|-----| | \( -r_A \) (mol/g·s)| .045 | .064 | .078 | .091 | .102 | **Step 1: Write the rate law equation** \[ -r_A = k' P_{H_2}^n \] **Step 2: Take the logarithm of both sides** \[ \ln(-r_A) = \ln k' + n \ln P_{H_2} \] This is in the form \( y = a + bx \), where - \( y = \ln(-r_A) \) - \( x = \ln(P_{H_2}) \) - \( b = n \) (the exponent we want to find) **Step 3: Prepare the data for linearization** | \( P_{H_2} \) | \( -r_A \) | \( \ln(P_{H_2}) \) | \( \ln(-r_A) \) | |---------------|------------|--------------------|-----------------| | 1.5 | .045 | .405 | -3.101 | | 3. | .064 | 1.099 | -2.749 | | 4.5 | .078 | 1.504 | -2.551 | | 6. | .091 | 1.792 | -2.398 | | 7.5 | .102 | 2.015 | -2.284 | **Step 4: Perform linear regression** The slope \( n \) is found using the formula: \[ n = \frac{N \sum (x_i y_i) - \sum x_i \sum y_i}{N \sum x_i^2 - (\sum x_i)^2} \] where \( N = 5 \). Calculate the required sums: \[ \sum x_i = .405 + 1.099 + 1.504 + 1.792 + 2.015 = 6.815 \] \[ \sum y_i = -3.101 + (-2.749) + (-2.551) + (-2.398) + (-2.284) = -13.083 \] \[ \sum x_i^2 = (.405)^2 + (1.099)^2 + (1.504)^2 + (1.792)^2 + (2.015)^2 = .164 + 1.208 + 2.263 + 3.214 + 4.060 = 10.909 \] \[ \sum x_i y_i = (.405)(-3.101) + (1.099)(-2.749) + (1.504)(-2.551) + (1.792)(-2.398) + (2.015)(-2.284) \] \[ = -1.256 + (-3.021) + (-3.838) + (-4.299) + (-4.601) = -17.015 \] Now, substitute: \[ n = \frac{5(-17.015) - (6.815)(-13.083)}{5(10.909) - (6.815)^2} \] \[ = \frac{-85.075 + 89.158}{54.545 - 46.454} \] \[ = \frac{4.083}{8.091} \] \[ = .505 \] **Final Answer** The exponent \( n \) calculated using non-linear regression (linearized as above) is approximately **.51**. --- **Summary:** The exponent \( n \) in the rate law \( -r_A = k' P_{H_2}^n \) is **.51** using the provided experimental data and linear regression analysis.

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