Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Glycerin \(\left(c_{p}=2400 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) at \(20^{\circ} \mathrm{C}\) and \(0.5 \mathrm{~kg} / \mathrm{s}\) is to be heated by ethylene glycol $\left(c_{p}=2500 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)60^{\circ} \mathrm{C}$ and the same mass flow rate in a thin-walled double-pipe parallelflow heat exchanger. If the overall heat transfer coefficient is \(380 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\) and the heat transfer surface area is \(6.5 \mathrm{~m}^{2}\), determine \((a)\) the rate of heat transfer and \((b)\) the outlet temperatures of the glycerin and the glycol.

Short Answer

Expert verified
The rate of heat transfer is 98,760 W. The outlet temperature of glycerin is 102.3°C, and the outlet temperature of ethylene glycol is -19.0°C.

Step by step solution

01

Calculate the heat capacity rates of glycerin and glycol

First, let's find the heat capacity rate (\(C_{r}\)) for each fluid, which is the product of their respective mass flow rates and specific heat capacities. The formulas are: \(C_{r_{glycerin}} = \dot{m}_{glycerin} \cdot c_{p_{glycerin}}\) \(C_{r_{glycol}} = \dot{m}_{glycol} \cdot c_{p_{glycol}}\) For glycerin, we have: \(C_{r_{glycerin}} = 0.5 \frac{kg}{s} \cdot 2400 \frac{J}{kg\cdot K} = 1200 \frac{J}{s\cdot K}\) For ethylene glycol, we have: \(C_{r_{glycol}} = 0.5 \frac{kg}{s} \cdot 2500 \frac{J}{kg\cdot K} = 1250 \frac{J}{s\cdot K}\)
02

Determine the heat transfer rate

The heat transfer rate (\(\dot{Q}\)) can be found using the overall heat transfer coefficient (U), the surface area of the heat exchanger (A), and the difference in the inlet temperatures of the two fluids (\(\Delta T_i\)): \(\dot{Q} = U\cdot A\cdot \Delta T_i\) We are given that \(U = 380 \frac{W}{m^2 K}\) and \(A = 6.5 m^2\). The temperature difference can be found as: \(\Delta T_i = T_{glycol,in} - T_{glycerin,in} = 60°C - 20°C = 40 K\) Now, we can calculate the heat transfer rate: \(\dot{Q} = 380 \frac{W}{m^2 K} \cdot 6.5 m^2 \cdot 40 K = 98760 W\)
03

Calculate the temperature change of each fluid

The temperature change in each fluid can be calculated as: \(\Delta T_{glycerin} = \frac{\dot{Q}}{C_{r_{glycerin}}}\) \(\Delta T_{glycol} = -\frac{\dot{Q}}{C_{r_{glycol}}}\) For glycerin: \(\Delta T_{glycerin} = \frac{98760 W}{1200 \frac{J}{s\cdot K}} = 82.3 K\) For ethylene glycol: \(\Delta T_{glycol} = -\frac{98760 W}{1250 \frac{J}{s\cdot K}} = -79.0 K\)
04

Find the exit temperatures of glycerin and glycol

Finally, we can find the outlet temperatures of both fluids by adding their temperature changes to their inlet temperatures: \(T_{glycerin,out} = T_{glycerin,in} + \Delta T_{glycerin} = 20°C + 82.3 K = 102.3°C\) \(T_{glycol,out} = T_{glycol,in} + \Delta T_{glycol} = 60°C - 79.0 K = -19.0°C\) So, the outlet temperatures of glycerin and ethylene glycol are \(102.3°C\) and \(-19.0°C\), respectively. In summary: (a) The rate of heat transfer is \(98760 W\). (b) The outlet temperatures of glycerin and ethylene glycol are \(102.3°C\) and \(-19.0°C\), respectively.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Cold water $\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters a counterflow heat exchanger at \)10^{\circ} \mathrm{C}\( at a rate of \)0.35 \mathrm{~kg} / \mathrm{s}$, where it is heated by hot air $\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the heat exchanger at \)50^{\circ} \mathrm{C}$ at a rate of \(1.9 \mathrm{~kg} / \mathrm{s}\) and leaves at $25^{\circ} \mathrm{C}$. The effectiveness of this heat exchanger is (a) \(0.50\) (b) \(0.63\) (c) \(0.72\) (d) \(0.81\) (e) \(0.89\)

A shell-and-tube heat exchanger with two shell passes and eight tube passes is used to heat ethyl alcohol $\left(c_{p}=2670 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( in the tubes from \)25^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)2.1 \mathrm{~kg} / \mathrm{s}$. The heating is to be done by water $\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the shell at \)95^{\circ} \mathrm{C}$ and leaves at \(60^{\circ} \mathrm{C}\). If the overall heat transfer coefficient is $800 \mathrm{~W} / \mathrm{m}^{2} . \mathrm{K}$, determine the heat transfer surface area of the heat exchanger using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method. Answer: \((a) 11.4 \mathrm{~m}^{2}\)

The radiator in an automobile is a crossflow heat exchanger $\left(U A_{s}=10 \mathrm{~kW} / \mathrm{K}\right)\( that uses air \)\left(c_{p}=1.00 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)$ to cool the engine-coolant fluid \(\left(c_{p}=4.00 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\). The engine fan draws \(22^{\circ} \mathrm{C}\) air through this radiator at a rate of \(8 \mathrm{~kg} / \mathrm{s}\) while the coolant pump circulates the engine coolant at a rate of \(5 \mathrm{~kg} / \mathrm{s}\). The coolant enters this radiator at \(80^{\circ} \mathrm{C}\). Under these conditions, the effectiveness of the radiator is \(0.4\). Determine \((a)\) the outlet temperature of the air and \((b)\) the rate of heat transfer between the two fluids.

A shell-and-tube heat exchanger with one shell pass and 14 tube passes is used to heat water in the tubes with geothermal steam condensing at $120^{\circ} \mathrm{C}\left(h_{f g}=2203 \mathrm{~kJ} / \mathrm{kg}\right)$ on the shell side. The tubes are thin-walled and have a diameter of \(2.4 \mathrm{~cm}\) and a length of \(3.2 \mathrm{~m}\) per pass. Water \(\left(c_{p}=4180\right.\) \(\mathrm{J} / \mathrm{kg} \cdot \mathrm{K}\) ) enters the tubes at $18^{\circ} \mathrm{C}\( at a rate of \)6.2 \mathrm{~kg} / \mathrm{s}$. If the temperature difference between the two fluids at the exit is \(46^{\circ} \mathrm{C}\), determine \((a)\) the rate of heat transfer, \((b)\) the rate of condensation of steam, and \((c)\) the overall heat transfer coefficient.

Steam is to be condensed on the shell side of a twoshell-passes and eight- tube-passes condenser, with 20 tubes in each pass. Cooling water enters the tubes at a rate of \(2 \mathrm{~kg} / \mathrm{s}\). If the heat transfer area is \(14 \mathrm{~m}^{2}\) and the overall heat transfer coefficient is $1800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, the effectiveness of this condenser is (a) \(0.70\) (b) \(0.80\) (c) \(0.90\) (d) \(0.95\) (e) \(1.0\)

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free