2017
DOI: 10.1016/j.energy.2017.01.125
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Effects of air gap on insulation thickness and life cycle costs for different pipe diameters in pipeline

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Cited by 20 publications
(9 citation statements)
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“…Using the degree day method, the annual energy amount transferred by fluid within the pipe with the heating process is assumed to be equal to the annual heat losses from within the pipe to the external environment, and it may be generally expressed as : Qnormalp,loss=86,4000.12emHDD0.12emUp where U p is the total heat transfer coefficient for all pipe layers. For Case 1, with uninsulated pipe layers (internal fluid + pipe + external fluid) and Case 2 with air gapped and insulated pipe layers (internal fluid + pipe + air gap + insulation material + external fluid), the total heat transfer coefficients are given below : 1Up,unins=1hiAi+ln0.12em()r1r02πLkp+1hoAo and 1Up,agins=1hiAi+ln0.12em()r1r02πLkp++ln0.12em()r2r12πLkag+ln0.12em()r3r22πLkins+1hoAo where A is heat transfer surface area of the pipe, A i = 2 π L r 0 , A o = 2 π L r 1 , and Ao=2π0.12emL0.12emr3. In the pipe layer, the convection heat transfer coefficients for the internal and external environments can be calculated as follows :…”
Section: Discussionmentioning
confidence: 99%
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“…Using the degree day method, the annual energy amount transferred by fluid within the pipe with the heating process is assumed to be equal to the annual heat losses from within the pipe to the external environment, and it may be generally expressed as : Qnormalp,loss=86,4000.12emHDD0.12emUp where U p is the total heat transfer coefficient for all pipe layers. For Case 1, with uninsulated pipe layers (internal fluid + pipe + external fluid) and Case 2 with air gapped and insulated pipe layers (internal fluid + pipe + air gap + insulation material + external fluid), the total heat transfer coefficients are given below : 1Up,unins=1hiAi+ln0.12em()r1r02πLkp+1hoAo and 1Up,agins=1hiAi+ln0.12em()r1r02πLkp++ln0.12em()r2r12πLkag+ln0.12em()r3r22πLkins+1hoAo where A is heat transfer surface area of the pipe, A i = 2 π L r 0 , A o = 2 π L r 1 , and Ao=2π0.12emL0.12emr3. In the pipe layer, the convection heat transfer coefficients for the internal and external environments can be calculated as follows :…”
Section: Discussionmentioning
confidence: 99%
“…The annual total energy cost, C f , and total cost of insulation material, C ins , for heat losses occurring in the pipe with insulation applications are determined as follows : Cf=mf0.12emCF and Cins=CI0.12emV where C F is unit cost of any fuel as $/kg, $/m 3 , $/kWh, C I is cost of insulation material per unit volume as $/m 3 and V=π(r32r22)L as m 3 .…”
Section: Discussionmentioning
confidence: 99%
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