# Heat Transfer In Buried Liquid Pipelines

Dear All,

Today's blog entry relates to heat transfer from liquids flowing in long-distance buried pipelines. When liquids have to be transported at relatively high temperatures, e.g. viscous crudes/products, temperatures and cooling rates can be determined using the following formulae:

where:
TL = average temperature in cross-section of pipeline at distance L, K
Ts = soil temperature at pipeline depth, K
Tinlet = temperature at pipeline inlet (L = 0), K
Ueff = Effective Heat Transfer Coefficient, W/m2-K
d = pipe internal diameter, m
L = pipeline distance at which TL is to be measured, m
m = mass flow rate of liquid, kg/s
Cp =Specific Heat Capacity of pipeline contents, J/kg-K

Calculation of Ueff

Uconvective
For turbulent flow (Re > 4000)

For Laminar flow (Re < 2300)

where:
Uconvective = Convective heat transfer coefficient, W/m2-K
λliq = liquid thermal conductivity, W/m-K (for crude oil, λliq = 0.13 W/m-K)
u = average liquid velocity, m/s
ρ = liquid density, kg/m3
d = pipe internal diameter, m
Cp = Specific Heat Capacity of pipeline contents, J/kg-K
ν = liquid kinematic viscosity, m2/s
g = acceleration due to gravity = 9.81 m/s2
α = thermal expansion coefficient, 1/K (for crude oil, α = 8*10-4 K-1)
µb = bulk liquid viscosity, Pa.s
μw = liquid viscosity at wall temperature, Pa.s
Tb = bulk temperature, K
Tw = inside wall temperature, K

Notes:
1. The inside wall temp. (Tw) is generally assumed 2-3 degrees lower than the bulk temp. (Tb) in laminar flow
2. The bulk liquid viscosity (μb) and the liquid viscosity at wall temperature (μw) can be assumed same for turbulent flow thus reducing the term (μb / μw) to 1

Specific Heat Capacity of Crude Oil

where:
Cp = Specific heat capacity at temperature T, J/kg-K
T = Temperature, ⁰C
ρ = crude oil density at temperature T, kg/m3

Uwall

where:
Uwall = steel wall heat transfer coefficient, W/m2-K
λsteel = thermal conductivity of steel, W/m-K (for Carbon Steel, λsteel = 52 W/m-K)
do = outside diameter of the steel pipe, m

d = pipe internal diameter, m
twall = wall thickness, m

Ucoating (Note: External Coating could be a polyolefin liner or insulation)

where:
Ucoating = coating heat transfer coefficient, W/m2-K
do = outside diameter of the steel pipe, m
λcoating = thermal conductivity of coating or insulation, W/m-K
tcoating = coating thickness, m

Uenvironment (For Buried pipes the environment is soil)

where:
Uenvironment = heat transfer coefficient to the environment (soil), W/m2-K
λsoil = thermal conductivity of soil, W/m-K
z = burial depth of the pipe up to the pipe axis, m

I have developed a spreadsheet for temperature drop in a buried crude oil pipeline based on the above methodology. For a set of conditions that I have used and for a pipeline inlet crude oil temperature of 55C, the temperature drops to 48.5C at a distance of 50 km for a 16 inch NPS pipeline based on the above method. The pipeline is also externally coated.

That is all for today's blog entry. Hope to have comments from the knowledgeable members of the forum.

Regards,
Ankur.

where do I get spread sheet for the above calculation.

ankur2061

where do I get spread sheet for the above calculation.

You don't get a readymade spreadsheet. You need to make one on your own. If I had to provide a spreadsheet there was no need to provide this article.

Regards,

Ankur.

is the above steps applicable for highly congealing oil like short and long residue, lubricating oils etc

STEVENLEE

Good share. Could you provide the reference of source of material to where this was derived. Most of us just borrow from the engineering gods that developed equations and I'm no different.

Thanks.

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