11/14/14

UNFIRED PRESSURE VESSEL AND STORAGE TANK DESIGN CRITERIA


All unfired pressure vessels, shall be designed, fabricated and tested in accordance with ASME Section VIII Boiler and Pressure Vessel Code Div.1, API 650 Welded Steel Tanks for oil storage, ASME VIII Div 1/ API 2510 Design and Construction of LPG Installations, Uniform Building Code and refer to Pressure Vessel/ Storage Tank/ Spherical Tank specification and their relevant datasheets.
Allowable stress of pressure parts shall be in accordance with the applicable code. Allowable stress for vessels and tanks material which not covered by any code shall be prohibited.
Process conditions shall dictate the materials used for vessel construction, taking into account the corrosive nature of fluids, maximum/minimum and design operating pressure and temperature requirements.
Manholes (18" nominal diameter minimum) with davits or inspection openings (8” nominal diameter minimum) shall be provided for removal of vessel internals and internal inspections unless otherwise specified.
Piping arrangements around vessels or tanks shall allow for maintenance, testing, service of the vessels or tanks and their associated instrumentation with a minimum dismantling of piping. Vessel internals and tanks (if any) shall be bolted for ease of removal.
Filters/ filter separators/ coalescers up to 24” diameter, which require replacement of filter elements, shall be provided with full size, quick-opening end closures, complete with davits.  Vessels greater than 24” diameter may be provided with a full size bolted flange assembly complete with davit and cover lifting features.
Surface preparation for protective coating shall be accomplished by blast cleaning method. However for small and inaccessible areas, or areas where equipment may be damaged by blasting, hand tool or power cleaning tool methods may be utilized.
In case the equipments applied for hot temperature services (70oC or more), they should be furnished with hot insulation and or personal protection. Unless otherwise stated on the individual vessel data sheets and/or drawings, the corrosion allowance shall be 3 mm minimum on the shells, heads and nozzles.

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