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23-Chem-A1 Process Balances and Chemical Thermodynamics · December 2015

Question 6 of 6: Adiabatic Mixing of Acetone and Dichloromethane

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

Notes on this paper

National Exams — December 2015 — 04-Chem-A1 Process Balances and Chemical Thermodynamics. Three-hour, open-book exam; any non-communicating calculator permitted. Format: six questions in two parts — Part A (Q1–Q3, Process Mass & Energy Balances) and Part B (Q4–Q6, Chemical Thermodynamics). Candidates answer two from Part A and two from Part B; four equally-weighted questions (25 marks each) constitute a complete paper. All six are solved below for completeness. Property data are stated explicitly in each Given block.

Reference texts: Felder, Rousseau & Bullard, Elementary Principles of Chemical Processes (4th ed., Wiley) — combustion stoichiometry, humidity, recycle/purge and reactive material balances; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — reaction equilibrium, van’t Hoff analysis, VLE with ideal solutions and excess-property/heat-of-mixing energy balances; supporting data from Perry’s Chemical Engineers’ Handbook (9th ed.) and the NIST Chemistry WebBook.

Question 6: Adiabatic Mixing of Acetone and Dichloromethane (Part B — 25 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. Equal masses of two pure liquids at 298 K are mixed adiabatically at 1 bar with no work. Acetone + dichloromethane mix exothermically: the C–H···O=C hydrogen bond between the two liquids gives a negative excess enthalpy, the same behaviour as acetone–chloroform. The tabulated positive heat of mixing is therefore read as heat released per kg of solution, so the product warms above 298 K.

QuantityValue
$C_p$ acetone / dichloromethane2.173 / 1.193 kJ/kg·K
Solution $C_p$ (equal mass)½(2.173+1.193) = 1.683 kJ/kg·K
Heat of mixing at 293 / 298 / 303 K12.468 / 12.380 / 12.292 kJ/kg
Feed temperature298 K, adiabatic, 1 bar, no work

Find. The temperature $T$ of the solution formed.

AdiabaticMixerAcetone 298 KDichloromethane 298 KSolution at T = ?
Figure 6 — Adiabatic mixer: equal masses of acetone and dichloromethane enter at 298 K; the exothermic heat of mixing raises the product temperature.

Approach. Adiabatic and work-free means the overall enthalpy change is zero. Follow a path that first heats the pure components from 298 K to the final $T$, then mixes them at $T$; setting the total to zero equates the sensible heat gained to the heat of mixing released (evaluated at $T$, using the tabulated temperature dependence).

  1. Zero-enthalpy path. Per kg of solution, heating the (still-pure) components 298 → $T$ costs $C_{p,soln}(T-298)$ and mixing at $T$ releases $q_{mix}(T)$; adiabatic operation sets their sum to zero: $$C_{p,soln}\,(T-298)=q_{mix}(T).$$
  2. Temperature dependence of the heat of mixing. The three data points are linear in $T$ with slope $\dfrac{12.292-12.468}{303-293}=-0.0176$ kJ/kg·K, so $q_{mix}(T)=12.380-0.0176\,(T-298)$.
  3. Solve for the mixing temperature. Substituting with $C_{p,soln}=1.683$ and letting $u=T-298$: $$1.683\,u=12.380-0.0176\,u\;\Rightarrow\;u=\frac{12.380}{1.683+0.0176}=7.28\ \text{K}\;\Rightarrow\;T=\boxed{305.3\ \text{K}\;(32.1\ ^\circ\text{C}).}$$ The weak temperature dependence barely matters here — ignoring it gives 305.4 K — but including it is the rigorous route the three data points invite.
Assumption
The exam prints the heat of mixing as a positive number without stating a sign convention. It is taken here as heat released, because acetone–dichloromethane mixing is exothermic. If the same values were instead read as an endothermic $\Delta H_{mix}$ (heat absorbed), the balance becomes $1.683\,u=-(12.380-0.0176\,u)$, giving $u=-7.43$ K and $T\approx290.6$ K. State whichever convention you adopt; the method is unchanged.
QuantityResult
Solution heat capacity1.683 kJ/kg·K
Temperature rise+7.3 K
Solution temperature305.3 K (32.1 °C)
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