KNOWLEDGE
CONVECTION HEAT EXCHANGE
Concerning the exchanger, Q kcal/h represents the quantity of heat for exchange
- W:The quantity of flow for low-temperature side fluid(kg/h)
- i1,i2:Quantity of heat for the entry and exit of low-temperature fluid(kcal/kg)
- W':The quantity of flow for high-temperature side fluid(kg/h)
- i'1, i'2:The quantity of heat for exit and entry of high-temperature side fluid(kcal/kg)
- A:Area of valid heat transfer(m²)
- θm=Logarithm average temperature difference(°C)
- θ1=Whatever direct current or reverse current, the part of large temperature difference(°C)
- θ2=Whatever direct current or reverse current, the part of little temperature difference(°C)
- K=The flow rate of thermos(kcal/m² h°C)
The general value of K is shown as follow
Kinds of Liquid | K Kcal/m²h°C | Abstract |
---|---|---|
LIQUID & LIQUID | 25-50 | viscosity liquid, laminar flow and natural convection |
100-250 | viscosity liquid and forced convection | |
120-300 | water and natural convection | |
250-800 | water and mixed stream | |
800-1500 | water and forced convection | |
800-2000 | membrane,highly-speeded stream, heat for metal plate,and heat for centrifuge | |
LIQUID AND GAS | 5-15 | air and natural convection |
10-50 | air and forced convection | |
50-500 | high pressure(300 atmosphere) air and double tube | |
GAS AND GAS | 3-10 | natural convection |
10-30 | viscosity liquid & stream linen |
LOGARITHMIC AVERAGE TEMPERATURE DIFFERENCE
自然對流之熱傳導
流體在水平管外部時
流體在垂直管外部時
- h=熱傳導係數 kcal/m² hr°C
- Cp=Constant-Pressure Specific Heat of Fluid kcal/kg°C
- λ=Thermal Conductivity of Fluid kcal/mhr°C
- ρ=Fluid Density kg/m³
- β=Coefficient of Expansion of Fluid 1/°C
- μ=Fluid Viscosity kg/mhr
- g=Acceleration of Gravity m/ hr²
- Δt=Temperature Difference between Fluid Itself and the Side of Conduction of Heat °C
Thermal Conductivity of Forced Convection
Fluid flows out of the pipe
intricate Permutation
Square Permutation
- d=external diameter of pipe m
- h=Thermal Conductivity of Border Membrane kcal/m²hr°C
- υ=Average Speed of Fluid m/hr
- λ=Average Thermal Conductivity of Fluid kcal/mhr°C
- μ=Average Viscosity of Fluid kg/mhr
- ρ=Average Density of Fluid kg/m³
空氣流中之管群熱傳導係數,平均溫度60°C方格式排列之場合,適用於蒸氣、氧氣、氮氣、烟道氣體亦可得相當近似值
Piping Permutation | Intricate Permutation (C) | Square Permutation (C') |
---|---|---|
2 | 0.100 | 0.122 |
3 | 0.113 | 0.126 |
4 | 0.123 | 0.129 |
5 | 0.131 | 0.131 |
6 | 0.136 | 0.132 |
7 | 0.140 | 0.133 |
8 | 0.143 | 0.134 |
9 | 0.145 | 0.135 |
10 | 0.147 | 0.135 |