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Custom Process Equipment, LLC 4727 NW Evangeline Thwy Carencro, LA 70520 Tel 337-896-3815 Fax 337-896-3816 www.cpe-llc.com Design Basis (job#) Author Check Approved Revisio n Dat e Rev Description A Preliminary Design Process Description (briefly describe the process, identify the field or location to be installed, state designers understanding of up and down stream equipment, lifespan(if not explicitly stated in RFQ OMIT), state if it’s a single unit or a system. Include the process objectives. Environmental Conditions Air Temperature: Minimum Temperature Dry Bulb (value with units) Maximum Temperature Dry Bulb Design Max Temperature Design Min Temperature Min Design metal Temperature Design Temp for Air Coolers Relative Humidity: Relative Humidity Design (Value in %) Maximum Normal Minimum

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Page 1: Design Basis

Custom Process Equipment, LLC4727 NW Evangeline ThwyCarencro, LA 70520Tel 337-896-3815Fax 337-896-3816www.cpe-llc.com

Design Basis(job#)

Author Check Approved Revision Date Rev DescriptionA Preliminary Design

Process Description(briefly describe the process, identify the field or location to be installed, state designers understanding of up and down stream equipment, lifespan(if not explicitly stated in RFQ OMIT), state if it’s a single unit or a system. Include the process objectives.

Environmental Conditions

Air Temperature:Minimum Temperature Dry Bulb (value with units)Maximum Temperature Dry BulbDesign Max TemperatureDesign Min TemperatureMin Design metal TemperatureDesign Temp for Air Coolers

Relative Humidity:Relative Humidity Design (Value in %)

MaximumNormalMinimum

Barometric Pressure

RainfallRainfall Yearly High (value with Units)

MeanLow

2-year 15 minutes100-year 15 minutes

Page 2: Design Basis

Custom Process Equipment, LLC4727 NW Evangeline ThwyCarencro, LA 70520Tel 337-896-3815Fax 337-896-3816www.cpe-llc.com

Design Basis(job#)

Wind Speed and DirectionPrevailing Wind Direction (max intensity & Direction)Basic Wind Speed Cat. I Buildings

Cat. II BuildingsCat III Buildings

Wind Loads per Code (code)

GeotechnicalElevation (value with units)Earth Quack ZoneSoil BearingSeismic Loads per Code (Code)Site Class DSpectral Response 0.2 sec, SsSpectral Response 1.0 sec, S1Redundancy Factor ρ 1Importance Factor I 1.25Structural steel per Code

Process Inlet(Briefly describe as it is understood the nature of the fluid entering the process, is it held back by a choke of a well head or is it being pumped, how was it determined, by a test separator, was it recombined in a process simulator? etc.)

Gas PropertiesBulk Property Parameter UnitSpecific gravity .65 (Air=1 @ 14.73 psia & 60 0F)Molecular weight Lb/lbmoleCompressibility factor, Z @ std conditionsWater content Sat. @ op. cond.Pseudo Critical Press. PsiaPseudo Critical Temp. Rankine

Page 3: Design Basis

Custom Process Equipment, LLC4727 NW Evangeline ThwyCarencro, LA 70520Tel 337-896-3815Fax 337-896-3816www.cpe-llc.com

Design Basis(job#)

Gas Composition(Attach or create & fill out a table)

Oil PropertiesBulk Property Parameter Unit Test NameAPI Gravity @ 60 0F ASTM D-1298Sulpher X-ray Wt.% ASTM D-4294Water & Sediment Vol% ASTM D-4007Flash Point 0F ASTM D-93AVanadium Ppm ASTM D-5863Nickel Ppm ASTM D-5863Ash Wt.% ASTM D-482Pour Point 0F ASTM D-97Salt Content PTB ASTM D-3230Viscosity @ 100 0F cSt ASTM D-445Viscosity @ 122 0F cSt ASTM D-445Viscosity @ 210 0F cSt ASTM D-445Asphaltenes Wt.% IP-143Paraffin Content Wt% UOP-46Distillation curve (example) EnglerIBP 428 0F5% 498 0F10% 552 0F20% 612 0F30% 648 0F

Oil Composition(Attach, or create new table)

Inlet ConditionsCondition Min Normal Max DesignPressure (psig)Temperature (0F)

Inlet FlowsFluid Type Min Normal Max Design FactorGas (MMSCFD)Oil (BPD)Water (BPD)

Page 4: Design Basis

Custom Process Equipment, LLC4727 NW Evangeline ThwyCarencro, LA 70520Tel 337-896-3815Fax 337-896-3816www.cpe-llc.com

Design Basis(job#)

SolidsType Amount UnitSand .25 Vol.%

NotesIs slugging to be considered, pigging operations? Is the flow instantaneous? Are the design factors reasonable, is anything known about the expected future flows of the well, is there a large pressure drop immediately upstream of the process or unit? Will a small change in the conditions or composition create a large change or upset in the process. IS FOAMING AN ISSUE. Address each of these concerns and explain why they should or should not be considered during the preliminary design phase.

Product SpecificationsBriefly reiterate the process objective and create a table which lists all of the expected outlet conditions. (such as RVP, water content, carryover, system losses) State weather a process guarantee is expected and if it should be provided by CPE or an internals’ provider such as SULZER or FABCO