2 Heat Exchangers
Learning Objectives
Operate the Plant in full generating capacity and study the effect of heat exchanger surface area using the Low Pressure Feed Heater 3.
Theory
A heat exchanger is equipment in which heat exchange takes place between two working media that enter and exit at different temperatures. The main function of heat exchanger is to either remove heat from a hot working media or to add heat to the cold working media. Depending on direction of working media-fluid flow the heat exchanger is either parallel (concurrent) flow heat exchanger or counter flow heat exchanger (see Figures below).
The terms are related to how the fluid flows through their respective flow passages relative to each other. If fluids flow in the same direction such as in Figure 1 it is termed a parallel flow. If fluids flow in opposite directions as in Figure 2 it is termed counter flow.
Parallel flow in heat exchangers occurs when both fluids enter the heat exchanger at their largest temperature difference. The temperature difference becomes less over the length of the heat exchanger. In the counter flow heat exchanger, fluids enter at opposite ends and therefore at different ends of the temperature scale Figure 2. The temperature difference between two fluids is relatively constant over the length of the exchanger.
The heat transfer process that occurs in any heat exchanger can be described by the following equations.
[latex]Q_{hot} = m_{hot}c_{p hot}\Delta T_{hot}[/latex]
[latex]Q_{cold} = m_{cold}c_{p cold}\Delta T_{cold}[/latex]
Considering the surface area involved in heat transfer, Newton’s Law of cooling states that the rate of heat loss is proportional to the difference in temperatures between the body and its surroundings and given by,
[latex]Q = \alpha Area \Delta T[/latex]
where α is called the heat transfer coefficient [W/m2K], area is taken in m2 and ΔT is the temperature difference.
Furthermore Q, heat transferred between the hot water and cold water can be calculated as follows:
[latex]Q = \frac{F(LMTD)}{R_{T}}[/latex]
Or
[latex]Q = F(UA)(LMTD)[/latex]
where F is the correction factor which equals 1 for this SIMLAB (it takes values between 0.5 and 1). RT is the overall resistance, U, overall heat transfer coefficient and LMTD is the Log Mean Temperature Difference.
The overall resistances can be calculated using:
[latex]R_{T}=R_{hf}+R_{w}+R_{cf}[/latex]
[latex]R_{hf} = \frac{1}{A_{1}\alpha_{h}}[/latex]
[latex]R_{w} = \frac{ln\frac{D_{2}}{D_{1}}}{2\pi L\lambda_{w}}[/latex]
[latex]R_{cf} = \frac{1}{A_{2}\alpha_{c}}[/latex]
Heat transfer coefficients ah and ac can be calculated using the following expression for Nusselt number for hot and cold water:
For cooling
[latex]\alpha_{h} = \frac{Nu_{h}\lambda_{h}}{D_{h}}[/latex]
[latex]Nu_{h} = 0.3Re_{h}^{0.8}Pr_{h}^{0.3}[/latex]
For heating
[latex]\alpha_{c} = \frac{Nu_{c}\lambda_{c}}{D_{c}}[/latex]
[latex]Nu_{c} = 0.3Re_{c}^{0.8}Pr_{c}^{0.3}[/latex]
And the LMTD is given by the following correl