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18-Env-B5 Industrial & Hazardous Waste Management · December 2018

Question 10 of 11: Chemical Reduction of Hexavalent Chromium with Sulfur Dioxide

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Reference texts: LaGrega, Buckingham & Evans, Hazardous Waste Management, 2nd ed.; Nemerow & Dasgupta, Industrial and Hazardous Waste Treatment, 2nd ed.; Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed.; Davis & Cornwell, Introduction to Environmental Engineering, 6th ed.; Cooper & Alley, Air Pollution Control: A Design Approach; CCME, Guidelines for the Management of Biomedical Waste in Canada (1992); Ontario Environmental Protection Act, R.S.O. 1990, c. E.19 and O. Reg. 347 (Waste Management – General); Transportation of Dangerous Goods Act, 1992 (Canada) and Regulations; Canadian Environmental Protection Act (CEPA), 1999.

Question 10: Chemical Reduction of Hexavalent Chromium with Sulfur Dioxide (15 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantityValue
Hexavalent chromium concentration650 mg/L
Flow rate35 L/min

Find. The mass rate of SO2 required to reduce all Cr6+ to the far less toxic Cr3+.

Approach. Balance the reduction reaction (Cr6+→Cr3+ by SO2, SO2 oxidized to sulfate) to get the stoichiometric mole ratio, convert to a mass ratio, then apply it to the chromium mass-loading rate.

  1. Balance the reduction reaction. Cr6+ gains 3 electrons to become Cr3+; SO2 (S4+) loses 2 electrons, oxidizing to sulfate (S6+). Equating electrons transferred (3 mol e- per mol Cr; 2 mol e- per mol SO2) gives the overall balanced reaction: $$2\text{H}_2\text{CrO}_4+3\text{SO}_2\longrightarrow\text{Cr}_2(\text{SO}_4)_3+2\text{H}_2\text{O}$$ i.e. $\boxed{1.5\ \text{mol SO}_2\ \text{per mol Cr}}$ (3 mol SO2 per 2 mol Cr).
  2. Convert to a mass ratio. Using $MW_{Cr}=52.0$ g/mol and $MW_{SO_2}=64.06$ g/mol: $$\frac{m_{SO_2}}{m_{Cr}}=1.5\times\frac{64.06}{52.0}=\boxed{1.848\ \text{g SO}_2/\text{g Cr}}$$
  3. Chromium mass-loading rate. From the given concentration and flow: $$\dot{m}_{Cr}=650\ \text{mg/L}\times35\ \text{L/min}=22{,}750\ \text{mg/min}=22.75\ \text{g/min}$$
  4. SO2 required. Apply the mass ratio from Step 2 to the chromium loading rate: $$\dot{m}_{SO_2}=22.75\ \text{g/min}\times1.848=\boxed{42.0\ \text{g/min}\ (60.5\ \text{kg/day},\ 133\ \text{lb/day})}$$
Final results
QuantityValue
Reaction2H2CrO4 + 3SO2 → Cr2(SO4)3 + 2H2O
Stoichiometric mass ratio1.848 g SO2/g Cr
Cr6+ loading rate22.75 g/min
SO2 required42.0 g/min (60.5 kg/day)
Check: this is the stoichiometric (theoretical) minimum SO2 demand from the balanced electron-transfer reaction; a full-scale design would apply a safety/excess factor (commonly 1.2–1.5× stoichiometric) to ensure complete reduction given imperfect mixing and competing side reactions, and would also confirm the reaction is carried out at low pH (typically 2–3), since Cr6+ reduction by SO2 is acid-catalyzed and proceeds far more slowly near neutral pH.