Formula Used:
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The heat transfer coefficient for condensation outside horizontal tubes is a critical parameter in heat exchanger design that quantifies the efficiency of heat transfer during the condensation process on the external surfaces of horizontal tubes.
The calculator uses the following formula:
Where:
Explanation: This formula calculates the average heat transfer coefficient for condensation outside horizontal tubes, considering fluid properties, tube geometry, and flow conditions.
Details: Accurate calculation of condensation heat transfer coefficient is crucial for designing efficient heat exchangers, optimizing energy transfer, and ensuring proper sizing of condensation equipment in various industrial applications.
Tips: Enter all required parameters with appropriate units. Ensure all values are positive and within reasonable physical limits for accurate results.
Q1: What is the significance of the 0.95 factor in the formula?
A: The 0.95 factor is an empirical coefficient that accounts for deviations from ideal condensation conditions and provides a more accurate prediction of the average heat transfer coefficient.
Q2: How does tube arrangement affect condensation heat transfer?
A: The vertical tube arrangement (NVertical) affects condensate drainage and film thickness, which significantly influences the heat transfer coefficient during condensation.
Q3: What are typical values for condensation heat transfer coefficients?
A: Typical values range from 1000-5000 W/m²·K for steam condensation and 500-2000 W/m²·K for organic vapors, depending on fluid properties and operating conditions.
Q4: When is this formula most applicable?
A: This formula is particularly suitable for laminar film condensation on the outside of horizontal tubes and provides good accuracy for most engineering applications.
Q5: What limitations should be considered when using this formula?
A: The formula assumes ideal conditions and may need modification for high vapor velocities, non-condensable gases, or complex tube bundle arrangements.