23-Chem-B6 Petroleum Refining and Petrochemicals · December 2019
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 16-Chem-B6, Petroleum Refining and Petrochemicals — December 2019. 3 hours, OPEN BOOK (any non-communicating calculator permitted). Per the exam notes, FIVE (5) questions constitute a complete paper and each is of equal value (10 marks). The paper prints five questions; the last (the refining-process question on page 6) is mislabelled “IV” in the source but is the fifth question and is answered here as Question 5. All five questions are worked in full.
Reference texts: Gary, Handwerk & Kaiser, Petroleum Refining: Technology and Economics, 5th ed. (CRC, 2007); Fahim, Al-Sahhaf & Elkilani, Fundamentals of Petroleum Refining (Elsevier, 2010); J. G. Speight, The Chemistry and Technology of Petroleum, 5th ed.; M. R. Riazi, Characterization and Properties of Petroleum Fractions (ASTM MNL50, 2005); Felder & Rousseau, Elementary Principles of Chemical Processes, 4th ed. (material balances).
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.
Definition. API gravity is the American Petroleum Institute’s standard inverse-density scale for petroleum liquids, defined from the specific gravity measured at 60/60 °F: $^{{\circ}}\text{API}=\dfrac{{141.5}}{{\mathrm{{SG}}}}-131.5$. By construction water (SG = 1.000) is exactly 10 °API.
Heavy vs. light. A heavy crude is dense (high specific gravity), and because °API varies inversely with SG, a heavy crude has a low API gravity (typically below ≈22 °API, and below 10 °API it is denser than water). Light, more valuable crudes have high API gravity (> 31 °API). Thus API gravity is a quick proxy for crude quality: higher °API generally means a lighter, sweeter, more easily refined and higher-priced crude.
Given. Feed $F=100\ \text{mol/h}$ salt solution at $x_F=0.10$ salt. Desired product $x_P=0.35$ salt; single-pass evaporator concentrate limited to $x_C=0.50$ salt; the bypass stream is raw feed. Only pure water leaves the evaporator as vapour.
| Stream | Salt fraction | Note |
|---|---|---|
| Feed F | 0.10 | 100 mol/h |
| Evaporator concentrate C | 0.50 | single-pass maximum |
| Bypass | 0.10 | raw feed, un-evaporated |
| Product P | 0.35 | target |
Find. (1) water evaporation rate; (2) bypass fraction; (3) concentrated-product rate; plus a labelled flowsheet.
Approach. Salt is conserved (only water evaporates), so the overall salt balance fixes the product rate and the evaporated water; a salt balance across the final mixer then fixes the bypass split.
| Quantity | Value |
|---|---|
| (1) Water evaporation rate $\dot W$ | 71.4 mol/h |
| (2) Fraction of feed bypassing the evaporator | 0.107 (10.7%) |
| (3) Concentrated product rate P | 28.6 mol/h at 35% salt |
| Evaporator concentrate C / bypass B | 17.9 / 10.7 mol/h |