Claudio156
Mechanical
- Feb 22, 2016
- 1
Hello,
I am busy with a feasibility analysis of a sea water air conditioning system. This is a system that provides cooling with deep sea water. Therefore, I need a heat exchanger, especially a plate heat exchanger. In my research, they are always saying that the overall heat transfer coefficient for this kind of heat exchange is around 4000 W/(m^2K).
The problem is that I never come to this value (only when I am playing with some values, but that is not the way it has to go). Mostly I have a value around 1500 W/(m^2K) without taking into account some fouling factors.
The general purpose is to dimension a plate heat exchanger starting from temperature values across the heat exchanger. I assume in the beginning that the geometrical information is known and that I just have to choose how many plates I need.
I am using the following technique:
First I assume that I know the temperatures in the in- and outlet of my heat exchanger at both side. Thus, I can calculate my LMTD value. Next, I want to calculate the Reynolds number of both fluid: sea water and district cool water. Therefore I make an assumption: I assume the plate heat exchanger consists only 1 plate for the sea water and for the district cool water. The Reynolds number are calculated and then the heat transfer coefficients are calculated with a Dittus Boelter relationship.
With the formula 1/U= 1/Hcold + 1/HHot + PLThickness/KMaterial
I can calculate my U-value. This new U-value, I am using for calculating my heat transfer area:
A=Q/(U*LMTD)
With information about the plate area, I can calculate how many plates I would need. This value will be compared with the previous value and if the difference is larger than 5%, the new value is assumed and the calculation are redone.
The iteration gives me always a value around 1500 W/(m^2K).
*If the explanation is not clear, I can give you a site where the procedure is explained:
On page 422
Two important remarks:
• I have a very high cooling duty, in the order of 30-120 MW. Thus, I am considering that the amount of plates will be split over a few heat exchangers.
• The assumed plate geometry is:
Plate area= 3 m^2
Plate Height: 3.567 m
Plate Thickness= 0.5*10^-3 m
Plate gap=2.8*10^-3
Plate width=1.172 m
Plate diameter= 0.5 m
It is maybe because of the choice of plate heat exchanger that I am using. If I increase the area of my plate heat exchanger to 4, I am in the good range. But then, I am not working with a real plate heat exchanger because above values are taken from some data sheet.
Can anyone help me? I already investigated a lot of time in this topic and need some feedback in how to solve this problem.
Kind regards,
Claudio
I am busy with a feasibility analysis of a sea water air conditioning system. This is a system that provides cooling with deep sea water. Therefore, I need a heat exchanger, especially a plate heat exchanger. In my research, they are always saying that the overall heat transfer coefficient for this kind of heat exchange is around 4000 W/(m^2K).
The problem is that I never come to this value (only when I am playing with some values, but that is not the way it has to go). Mostly I have a value around 1500 W/(m^2K) without taking into account some fouling factors.
The general purpose is to dimension a plate heat exchanger starting from temperature values across the heat exchanger. I assume in the beginning that the geometrical information is known and that I just have to choose how many plates I need.
I am using the following technique:
First I assume that I know the temperatures in the in- and outlet of my heat exchanger at both side. Thus, I can calculate my LMTD value. Next, I want to calculate the Reynolds number of both fluid: sea water and district cool water. Therefore I make an assumption: I assume the plate heat exchanger consists only 1 plate for the sea water and for the district cool water. The Reynolds number are calculated and then the heat transfer coefficients are calculated with a Dittus Boelter relationship.
With the formula 1/U= 1/Hcold + 1/HHot + PLThickness/KMaterial
I can calculate my U-value. This new U-value, I am using for calculating my heat transfer area:
A=Q/(U*LMTD)
With information about the plate area, I can calculate how many plates I would need. This value will be compared with the previous value and if the difference is larger than 5%, the new value is assumed and the calculation are redone.
The iteration gives me always a value around 1500 W/(m^2K).
*If the explanation is not clear, I can give you a site where the procedure is explained:
On page 422
Two important remarks:
• I have a very high cooling duty, in the order of 30-120 MW. Thus, I am considering that the amount of plates will be split over a few heat exchangers.
• The assumed plate geometry is:
Plate area= 3 m^2
Plate Height: 3.567 m
Plate Thickness= 0.5*10^-3 m
Plate gap=2.8*10^-3
Plate width=1.172 m
Plate diameter= 0.5 m
It is maybe because of the choice of plate heat exchanger that I am using. If I increase the area of my plate heat exchanger to 4, I am in the good range. But then, I am not working with a real plate heat exchanger because above values are taken from some data sheet.
Can anyone help me? I already investigated a lot of time in this topic and need some feedback in how to solve this problem.
Kind regards,
Claudio