How Does Cooling Water Temperature Affect Heat Exchanger Efficiency?

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Discussion Overview

The discussion revolves around the calculation of heat exchanger efficiency, specifically focusing on how the cooling water temperature affects the heat transfer process in a co-current heat exchanger. The context includes a homework problem involving the cooling of hydraulic fluid, requiring participants to determine the heat load and the area needed for the heat exchanger.

Discussion Character

  • Homework-related
  • Mathematical reasoning
  • Technical explanation

Main Points Raised

  • One participant expresses uncertainty about how to begin solving the problem, indicating a need for guidance.
  • Another participant suggests starting from the basics and emphasizes the importance of attempting the problem before seeking help.
  • A participant points out that the heat load can be calculated using the flow rate, heat capacity, and temperature change of the hydraulic fluid.
  • There is a discussion about the use of the LMTD formula to calculate the logarithmic mean temperature difference, with one participant providing a calculation that results in a negative value.
  • Another participant clarifies the definition of heat load and suggests that two equations related to heat load should be set equal to each other for solving the problem.
  • One participant successfully calculates the heat removed from the hydraulic fluid and the area required for the heat exchanger, confirming their methodology but not the arithmetic.

Areas of Agreement / Disagreement

Participants generally agree on the approach to calculate the heat load and the area required for the heat exchanger, but there is some confusion regarding the application of the LMTD formula and the correct interpretation of the results. The discussion does not resolve all uncertainties, particularly around the calculations and the implications of the negative LMTD value.

Contextual Notes

Limitations include potential misunderstandings of the heat exchanger equations and the implications of negative values in the LMTD calculation. The discussion does not clarify whether the assumptions made about the system are valid or if additional factors should be considered.

ScienceChem
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Homework Statement


A hydraulic fluid initially at 60◦C is cooled to 35◦C using a co-current heat exchanger. Cooling water is available at 15◦C, which must not exceed 30◦C on leaving the heat exchanger. The flow rate of the hydraulic fluid is 1.5 kg/s, which has a specific heat of 5.2 J/gํ C. Calculate the heat to be removed from the hydraulic fluid and the area required for the heat exchanger. Assume no fouling takes place. U = 520 W/m2°C

Homework Equations


Co-current heat exchanger: LMTD = {(Ti-ti)-(To-to)} / ln{(Ti-ti)/(To-to)}
Ti = temp of cooling / heating water in
ti = temp of liquid to be cooled / heated in

The Attempt at a Solution


I have no idea where to begin with this!
 
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"Start at the beginning. Go on to the end. Then, stop." ___ Caterpillar to Alice(?)

You really do need to take a stab at it before we jump in.
ScienceChem said:
1. (snip)
A hydraulic fluid initially at 60◦C is cooled to 35◦C ... (snip) The flow rate of the hydraulic fluid is 1.5 kg/s, which has a specific heat of 5.2 J/gํ C. Calculate the heat to be removed from the hydraulic fluid and the area required for the heat exchanger. Assume no fouling takes place. U = 520 W/m2°C
(snip)
 
From the information in the first two sentences, you can calculate the heat load of the heat exchanger. You know the flow rate of the fluid, its heat capacity, and its temperature change. So, what's the heat load?

Chet
 
So the heat load, using the formula given would then be:
LMTD = {(Ti-ti)-(To-to)} / ln{(Ti-ti)/(To-to)}
= {(15-60)-(30-35)}/ln{(15-60)/(30-35)}
= {(-45)-(-5)} / ln(-45/-5)
= {(-40) / (2.197)}
= -18.20
So I know:
-flow rate is 1.5 kg/s
-specific heat is 5.2 J/g degree C
-LMTD is -18.20

Would I then put this into the Q = Qin - Qout = flowrate*heat_capacity*(Tout - Tin)
But substitute as Q= flowrate*heat capacity*LMTD?
 
You seem to be very confused. I am going to recommend that you go back to your text and re-read the chapter on this again.

The heat load is defined as the rate at which heat gets removed from the hot stream, and you correctly gave one equation for it as: Q = = flowrate*heat_capacity*(Tout - Tin)

But, there is another equation involving the heat transfer coefficient, the heat transfer area, and the LMTD. You need to write this equation down also, and then you have to set the two heat load relationships equal to one another.

Chet
 
Okay I think I got this!
We use q=m*Cp*deltaT to find our heat that would be removed
thus: q = (1.5kg/s)*(5200 J/kgdegreesC)*(60-35)
q=195 000 J/s

then to get the area, we would use A= q / h(or U)*LMTD
so A= 195000 J/S / (520 W/m^2degreesC * 18.20)
A=20.60 m^2

Seems right now?
 
ScienceChem said:
Okay I think I got this!
We use q=m*Cp*deltaT to find our heat that would be removed
thus: q = (1.5kg/s)*(5200 J/kgdegreesC)*(60-35)
q=195 000 J/s

then to get the area, we would use A= q / h(or U)*LMTD
so A= 195000 J/S / (520 W/m^2degreesC * 18.20)
A=20.60 m^2

Seems right now?
Yes. Your methodology is correct now. I haven't checked your arithmetic.

Chet
 

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