Calculate energy required to heat water using a steam coil

AI Thread Summary
The discussion focuses on calculating the energy required to heat 200 hectoliters of water from 15°C to 85°C using a steam coil. The initial calculation for the mass of water is confirmed as 199,800 kg, leading to a heat requirement of approximately 58,461,480 kJ. However, it is noted that the mass of the stainless steel tank and coil must also be included in the total energy calculation, which adjusts the total heat required to about 5,986,134 kJ. Additionally, the discussion highlights the importance of significant figures in exam responses and provides an estimate for the mass of steam needed, ultimately arriving at approximately 3,020 kg. The conversation emphasizes the need for clarity in calculations and assumptions regarding the heating process.
sci0x
Messages
83
Reaction score
5
Homework Statement
Cold water at 15°C is heated to 85°C in a hot water tank by means of a steam coil
immersed in the water at the bottom of the tank. The combined (empty) tank and steam
coil weigh 1000 kg and are made of 304 stainless steel with a specific heat of 1.8 kJ kg-1 K
-1
.
Using the table below for water and steam properties data, calculate the amount of
energy required to heat 200 hL of water from 15°C to 85°C assuming the tank is well
insulated and there are negligible thermal losses to the environment.
Relevant Equations
Q = m c dT
1614021587148.png


I'm trying to complete this past exam paper Q.

Water volume = 200hl = 20000L
1L=10^-3 m^3
20000L = 200 m^3
Density of water at 15 deg C = 999 kg m^3

Density = Mass/Volume
999 kg m^3 = Mass/(200 m^3)
Mass of water = (200)(999) = 199800 kg

Heat required to to heat 199800 kg water:
Q =m C dT
= (199800 kg)(4.18 kJ kg-1K-1)((85-15)
=58461480 kJ

Am I correct here?
 
Physics news on Phys.org
20 m^3
 
  • Like
Likes Steve4Physics
sci0x said:
Homework Statement:: Cold water at 15°C is heated to 85°C in a hot water tank by means of a steam coil
immersed in the water at the bottom of the tank. The combined (empty) tank and steam
coil weigh 1000 kg and are made of 304 stainless steel with a specific heat of 1.8 kJ kg-1 K
-1
.
Using the table below for water and steam properties data, calculate the amount of
energy required to heat 200 hL of water from 15°C to 85°C assuming the tank is well
insulated and there are negligible thermal losses to the environment.
Relevant Equations:: Q = m c dT

View attachment 278494

I'm trying to complete this past exam paper Q.

Water volume = 200hl = 20000L
1L=10^-3 m^3
20000L = 200 m^3
Density of water at 15 deg C = 999 kg m^3

Density = Mass/Volume
999 kg m^3 = Mass/(200 m^3)
Mass of water = (200)(999) = 199800 kg

Heat required to to heat 199800 kg water:
Q =m C dT
= (199800 kg)(4.18 kJ kg-1K-1)((85-15)
=58461480 kJ

Am I correct here?
In addition to @Chestermiller's (admirably concise) observation, note that in heating the water, you will unavoidably have to heat the container. You are probably expected to include the energy required to do this. The wording of the question doesn't make this clear, but I guess you are given the mass of the container and its specific heat capacity for this reason.

Also '58461480 kJ' has 7 significant figures. (Lose 1 mark in an exam'!) You have given your answer with a precision of about 1 part in about 6 million. But the data you are using are far less precise.

EDIT: Although it will only change the answer slightly, you might consider using the average specific heat capacity of water over the temperature range.
 
  • Like
Likes hutchphd and Chestermiller
Thanks.

Density = Mass/Volume
999 kg m^3 = Mass/(20 m^3)
Mass of water = (20)(999) = 19980 kg

Heat required to to heat 199800 kg water:
Q =m C dT
= (19980 kg)(4.19 kJ kg-1K-1)((85-15)
= 5,860,134 kJ

Also heating the stainless steel & Coil:
Q = m C dT
= 1000kg (1.8 kJ kg-1 K-1)(85-15)
= 126,000 kg

Total heat req to heat water and stainless steel:
5,860,134 + 126,000 = 5,986,134 kJ

The next part of the Q is:
If the steam feeding the heating tube is at 1 bar gauge pressure and has a dryness fraction of 90%, estimate the amount of steam required to perform this heating task.

1 bar G = 10^5 Pa or 100 kPa
At 100 kPa
Enthalpy of steam = 2676 kJ kg-1
Enthalpy of water = 419 kJ kg-1
Change of enthalpy of steam = 2676 - 419 = 2257 kJ kg-1
Dryness factor is 90%: (2257)(0.9) = 2031.3 kj kg-1

5,986,134 kJ = Mass of Steam (2031.3 kj kg-1)
2946.94 kg = Mass of Steam
 
sci0x said:
Total heat req to heat water and stainless steel:
5,860,134 + 126,000 = 5,986,134 kJ
You've given the answer to 7 significant figures. What would you write if this were a value required in an exam' and you didn't want to lose a mark for an inappropiate number of significant figures?

sci0x said:
1 bar G = 10^5 Pa or 100 kPa
At 100 kPa
Enthalpy of steam = 2676 kJ kg-1
Enthalpy of water = 419 kJ kg-1
Change of enthalpy of steam = 2676 - 419 = 2257 kJ kg-1
Dryness factor is 90%: (2257)(0.9) = 2031.3 kj kg-1

5,986,134 kJ = Mass of Steam (2031.3 kj kg-1)
2946.94 kg = Mass of Steam
Why state '100kPa' when the table explicitly uses 101kPa?

Edit - the above pressure is wrong.
See @Chestermiller's post #6 below.


No need to say "Change of enthalpy of steam = 2676 - 419" when this value has already been calculated for you (penultimate column of table).

You are asked for an *estimate* of the steam mass. An 'estimate' is an approximate value. You have given you answer to 6 significant figures!

Can you suggest why your value (suitably rounded) might be a reasonable rough estimate - given that you have ignored the water from the steam cooling from 100ºC to 85ºC?
 
Last edited:
I bar gauge pressure is 2 bars absolute pressure. So the temperature is not 100 C.
 
  • Like
Likes Steve4Physics
Steve4Physics said:
Can you suggest why your value (suitably rounded) might be a reasonable rough estimate - given that you have ignored the water from the steam cooling from 100ºC to 85ºC?
The steam is not cooled to 85 C. The streams are not mixed. It is a heat exchanger. The steam exits as saturated liquid at 2 bars.
 
  • Like
Likes sci0x and Steve4Physics
Chestermiller said:
The steam is not cooled to 85 C. The streams are not mixed. It is a heat exchanger. The steam exits as saturated liquid at 2 bars.
OK but I don't get why the condensed liquid leaving the heat exchanger cannot have cooled nearer to 85ºC. Mixing is not needed to achieve this.

There is nothing in the question which requires input and output temperatures of the heat exchanger to be equal.

My gut feel is that there could be a temperature-drop along the heat exchanger but its contribution to heating the water is negligible (compared to the contribution from the condensation process). So it need not be calculated and this is the basis for the question asking only for an 'estimate'.
 
Thanks Chester

1 bar G = 2 bar absolute
2 bar = 200kPa (so using 199 kPa data)
Enthalpy of Steam - Enthalpy of water = Enthalpy of Evaporation = 2202 kJ kg-1
Dryness factor = (2202)(0.9) = 1981.84 kJ kg-1

5,986,134 kJ =(Mass of steam)(1981.8 kJ kg-1)
Mass of steam = 3020 kg

Would you agree or am i gone wrong here
 
  • #10
Looks OK
 
  • Like
Likes sci0x
Back
Top