Dear Experts,
I have to design a low pressure, Double walled, Ethylene Product Storage tank for liquefied hydrocarbon gases using API-620. This is my first time. I need your suggestions / help. The details are as follows:-
Inside Dia. inner Tank = 30 m
Design Temp = -105 dgree cel.inner tank & 65 dgree cel. outer tank
Corrosion = 1.6 mm
Nominal Capacity = 18,096 m3
Vertical Cylindrical Dome roof Double Wall
STD API 620
Product Ethylene
Sp. Gravity = 0.56
Vapour Press = 1.035 barA @ -103.2 deg. cel.
Operating Press = 0.022 barg
Design Press = 0.173 barg inner tank & -50 mm H2O outer tank
Opearting Press = 0.022 barg
Material = Ni 9% inner tank & A283 Gr. C Outer tank
Cold Insulation reqd.
Note: Inner & outer tank Dimension should be specified based on 0.1% per day of heat evaporation rate pls suggest resonable heat evaporation rate.
Regards
ashishpvnit
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Sample Design Calculation For Low Pressure Storage Tanks For Liquefied
Started by ashishpvnit, Sep 22 2010 05:51 AM
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Posted 22 September 2010 - 05:51 AM
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