12/4/14

DESIGN TEMPERATURE PHILOSOPHY

The design temperature shall be based on the maximum operating temperature plus a minimum margin of 20°F.  For equipment operating at ambient conditions, the upper design temperature shall be at least equal to a maximum black bulb temperature of 160°F unless it is insulated or other corrective action is taken.  Fire conditions will not be considered in establishing the design temperature of a vessel.
For process coolers, consideration should be given to designing downstream equipment for the upstream design condition. Reliance on devices such as temperature trips to protect downstream equipment in the event of cooling failure may introduce risk, as the instrument response time may not be sufficiently rapid to offer adequate protection. This will be reviewed on a case by case basis.
Compressor suction scrubber design temperatures are defined as the highest of the following:
a)     Maximum operating temperature at the compressor suction in the event of air cooler failure.
b)    Maximum recycle temperature (discharge minus JT drop across anti-surge valve) in the event of air cooling failure.
c)     Maximum normal operating temperature plus 50°F.
Compressor Discharge
Maximum operating temperature on compressor discharge will be defined as 20°F above the predicted maximum normal operating temperature to allow for lower efficiency at off-design operation.  The maximum discharge temperature shall be confirmed by the compressor vendor.
Shell and Tube Heat Exchanger
For shell and tube heat exchangers, whenever the shell side fluid is hotter than the tube side fluid, the design temperature on the tube side shall be made equal to the shell side design temperature.
Protection of equipment against overpressure and other excessive operating conditions shall be in accordance with API RP 14C (Basic Safety System), API RP 520 (Pressure Relieving Systems) and API RP 521 (Pressure Relief and Depressuring Systems).

12/3/14

INSTRUMENT ACCESSIBILITY TECHNICAL REQUIREMENTS

1.      Technical Requirements

All materials and equipment furnished shall be new, un­used and free of defects.  Materials and equipment shall be protected from construction damage, particularly damage due to sandblasting and painting. Each instrument furnished shall be provided with fully completed data sheets.  Data Sheets shall be numbered and indicate manufacturer and model numbers. Stan­dard ISA instrument data sheets will be acceptable.
Multiple listing of instruments on one sheet is permitted; however, they must be arranged in numerical sequence by tag number.  Only identical instruments may be listed on each data sheet i.e. the only difference allowed is tag numbers. An assigned tag number which is cancelled due to instru­ment revisions shall not be re-used.
Where possible, the instrument selection shall represent the man­ufacturer's standard.  Standardization of instru­ments types, manufacturer, and model shall be considered for the purpose of simplifying design and reducing spare parts. Selection of instruments and supporting hardware shall be made with consideration of the process fluid, the operat­ing environment, and the electrical area classification. Process fluids, steam or water shall not be channeled into control rooms for direct measurements.
Instrument pneumatic analog signals shall be 3 - 15 psig, un­less otherwise specified or required by the equipment such as valve operators.  Instrument pneumatic on-off signals shall generally be 30 psig. Pneumatic instruments requiring a regulated air supply shall be furnished with a SS 316 filter regulator and output gauge of SS 316.
The use of transmitters shall be maximized to improve overall reliability and availability. All transmitters shall be “SMART” electronic type utilizing ‘dual mode’ output with 2 wire 4 – 20 mA signal with superimposed ‘HART’ protocol communication signal.
Local electric control switches shall be DPDT, unless oth­erwise specified. Discrete (On-off) electric signals shall be 24 VDC unless otherwise specified. Use of local electronic control switches in lieu of electronic type transmitters requires Company approval. Separate instruments along with separate piping and vessel tapping / connections shall be used for shutdown initiating devices.
Where two (2) pressure or temperature transmitters monitor the same parameter then local gauge need not be provided. The control transmitter installation is to include a plugged connection where a gauge can be added at future time. Instrument stands shall be designed to accommodate the future gauge. Each field and control panel instrument shall have a per­manent SS 316 nameplate bearing its tag number. Tag num­bers shall be stamped and not engraved.

2.      Instrument Accessibility

Each instrument shall be considered as a normal working location and therefore shall be properly located in order to satisfy workers safety conditions as well as efficiency. Instrument accessibility being able to induce heavy consequence on piping or complex layout, this problem shall be considered as soon as possible during the detailed engineering stage.
It shall be important to distinguish two kinds of working location:
a.     Permanent working location
b.    Non permanent working location.
A working location shall be considered as permanent when visit frequency is higher than once a week. Non permanent working location shall have visit frequency lower than once a week. For permanent type, the access shall be easy. Access platforms are to be provided where applicable and movable ladders not permitted. For non-permanent type, movable ladders shall be allowed if height is less than 3 meters.
The following instruments and accessories shall be considered as permanent working location:
Control valves, ON / OFF actuated valves, transmitters, local controllers, local converters, in-line flow meters, level gages, level switches, pressure switches, temperature elements (indication and control) with transmitters, analyzer take off point, sampling loop.
The following instruments shall be considered as non -permanent working location: orifice flanges, pressure taps, thermocouples or RTD’s, and thermo well. Permanent access at these locations is not required.

3.      Instruments Process Connections

When an instrument is connected to the process by means of flanges, those flanges shall be ANSI 150# RF rated as a minimum. The following Table-1 gives the main requirements concerning instrument taps/nozzles.
TABLE–1
 
Note:
1.     To be confirmed with TW stress calculations, 2½" flange is not allowed due to piping class constraint.
Minimum insertion length of thermo wells shall be that of 4” pipe expander/reducers as indicated on the P&ID’s.
2.     A 2 x 3” expander shall be provided.

12/2/14

PETROLEUM FIREWATER SYSTEMS DESIGN

Fire-water systems shall be installed on petroleum Plant to cover the fire-water needs of each plant. This document describes the minimum facilities and fire-water capacities required to meet the statuary requirements.
The permanent systems used for protection of equipment usually consist of a combination of deluge, water sprays and fixed monitors.
·         A water deluge system is one in which all the water is applied at the top of the vessel and allowed to run down the sides.
·         A water spray system uses many nozzles arranged in a grid pattern to distribute the water evenly over the vessel.
·         Fixed monitors are permanently connected to the fire-water grid system and directed at the protected unit.
Gas turbines/compressors/expander packages are not water protected as the units are enclosed and protected by CO2 total flooding systems.
All vessels containing hydrocarbon liquids are water protected including their supporting skirts.
Closed Drain Drum is deluged as well as the Closed Drain Pump.
Compressor discharge coolers are not water protected as those coolers are air cooler type and contain little or no liquid.
Liquid filled coolers are water protected; those with condensing liquids are not water protected.
The driver of the Emergency Diesel Generator and its feed vessel will be deluged only if fire is detected in its area. A dedicated deluge valve shall be provided for the skids.
Each LPG storage sphere shall be protected either by a water deluge system or water spray system, to protect against pool-fire exposure, supplemented by fixed monitors.
Fire-water Flow Rates
The minimum flow rates used in determining the total fire-water flow rate are shown in Table


Flow is initiated only in the zone(s) where the fire is detected. In the remaining zones, flow can be initiated manually. Fixed sprays or deluge cover equipment and critical valves. Monitors and hydrants operation is manual.

SPRAY NOZZLE SELECTION
The spray nozzle shall be effective at the minimum discharge pressure given in NFPA 20 of 40 psig. In general spray nozzles are fully effectively from 50 psig upwards (3.5 barg).
For example: D3 Protect spray Nozzle No. 21, K = 25.9 @ 3.5 barg

Q =    Flow rate, 48.5 litter/minute
P  =    Pressure, bar
K =    Nozzle constant (by vendor)
Litters / minute
Contractor shall fully design the actual fire-water network in detail engineering and all assumed parameters in this document shall be recalculated to give the optimum fire-water system.

MATERIAL AND EARTH WORK SPECIFICATION

Borrow Material Borrow material shall meet the requirement specified for satisfactory fill materials per ASTM D2487 or ASTM D...