4.7 1000 kg (38/h heated at 6782 reactor n₂ (W/h) 0.973 (3/18/15 0.03 5 3/18 по no (n/a) 03 distillat n (US (31/18/h) m (ns (3/16/h) ^p (us (nu/h) nycus H12/ h) X1800°c) n₁ (multi/h) n3 kompresen Tn, CA (318/h nz (Ms (3Mc/h) ny (mol H/h), Malms/ пустинни E Stripper absorber 100°2 ni (ng (3 Mo/h) m² (hy (3 Huh) ts tuzaith) ⑤ preheater: This is used to raise the temperature of the reactants to get an increase in reaction rate reactore This is used to get the reention performed
4.7 1000 kg (38/h heated at 6782 reactor n₂ (W/h) 0.973 (3/18/15 0.03 5 3/18 по no (n/a) 03 distillat n (US (31/18/h) m (ns (3/16/h) ^p (us (nu/h) nycus H12/ h) X1800°c) n₁ (multi/h) n3 kompresen Tn, CA (318/h nz (Ms (3Mc/h) ny (mol H/h), Malms/ пустинни E Stripper absorber 100°2 ni (ng (3 Mo/h) m² (hy (3 Huh) ts tuzaith) ⑤ preheater: This is used to raise the temperature of the reactants to get an increase in reaction rate reactore This is used to get the reention performed
Solid Waste Engineering
3rd Edition
ISBN:9781305635203
Author:Worrell, William A.
Publisher:Worrell, William A.
Chapter7: Thermal Processes
Section: Chapter Questions
Problem 7.14P
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I need help with these three questions
1. Develop a mass balance equation for the removal of contaminants based on figure 1 (shown in the next photo. For individual steps and an overall mass balance)
2. Pick two contaminants, their concentrations and look at the mass balance and compare your mass balance to the data reported in the paper - Does it match? Hint: Use the frequency of detection, load variation, daily flows, and concentration to find the average concentrations - you can develop your own way of obtaining this but state all assumptions.
3. What would you change in this study to get a better mass balance of the contaminants on a day-to-day basis?
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