23-Chem-A1 Process Balances and Chemical Thermodynamics · December 2013
Question 4 of 7: Time to Heat a Stirred Tank and Its Contents
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — December 2013 — 04-Chem-A1 Process Balances and Chemical Thermodynamics. Three-hour, open-book exam; any non-communicating calculator permitted. Format: seven questions in three parts — answer one of Q1–Q2 (Part A), one of Q3–Q4 (Part B) and two of Q5–Q7 (Part C); four questions of equal value constitute a complete paper. All seven are solved below for completeness. Property data needed (densities, molar masses, steam-table and thermochemical values) are stated explicitly in each Given block. Units follow the paper (mixed SI and US customary).
Reference texts: Felder, Rousseau & Bullard, Elementary Principles of Chemical Processes (4th ed., Wiley) — material & energy balances, humidity and gas laws; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — excess properties, VLE, residual properties and reaction equilibrium; supporting property data from Perry's Chemical Engineers' Handbook (9th ed.), the NIST/ASME steam tables and the NIST Chemistry WebBook.
Question 4: Time to Heat a Stirred Tank and Its Contents (equal value)
Given. A closed, well-stirred system heated at constant rate $\dot Q = 300$ kW.
Body
Mass (kg)
$C_v$ (J/kg·K)
Tank (vessel)
5000
500
Reaction mixture
1500
3765
Temperature change
25 → 250 °C ($\Delta T = 225$ K)
Find. the heating time.
Figure 3 — Closed stirred tank: 300 kW warms both the 5000 kg vessel and the 1500 kg mixture from 25 °C to 250 °C.
Approach. With no reaction, no phase change and negligible stirrer work, the closed-system energy balance is simply the heat added equals the sensible-heat rise of the tank plus contents; divide the required energy by the power.
Lumped heat capacity of tank + contents. Both the vessel and the mixture warm together through the same $\Delta T$:
$$C_\text{tot} = m_\text{tank}C_{v,\text{tank}} + m_\text{mix}C_{v,\text{mix}} = 5000(500) + 1500(3765) = 8.148\times10^{6}\ \text{J/K}.$$
Energy required for the 225 K rise. For a closed system with only sensible heating, $Q = C_\text{tot}\,\Delta T$:
$$Q = (8.148\times10^{6})(225) = 1.833\times10^{9}\ \text{J} = \boxed{1.833\ \text{GJ}}.$$
Time at constant heating rate. Dividing by the 300 kW input,
$$t = \frac{Q}{\dot Q} = \frac{1.833\times10^{9}\ \text{J}}{3.0\times10^{5}\ \text{W}} = 6111\ \text{s} = \boxed{1.70\ \text{h}\;(101.8\ \text{min})}.$$