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Local Fuel – Shoreham Oil Terminal

Gasoline Ship Import – Layers of Protection Analysis

P & I Design Ltd

DOCUMENT NO: LF364002_RPT

2 Reed Street, Thornaby, UK, TS17 7AF

ISSUE: E DATE: 30.07.15

Tel: + 44 (0)1642 617444

PAGE 19 OF 38

Fax: + 44 (0)1642 616447

www.pidesign.co.uk

5

GASOLINE IMPORT REVIEW

5.1

Storage Facility

The process involves the importation of Gasoline by pipeline to one of two gasoline

storage tanks. Import is from ship via a dedicated pipeline system. The receiving tank is

selected by the operator and only 1 tank will be selected for import.

The terminal controls the manifold route selection. The manifold has remotely operated

valves. There are two jetty loading arms with valve splits.

The complete pipeline system

runs through the confines of the terminal.

The Gasoline tanks are fitted with an automatic tank gauge (ATG), which measures the

level in the tank, by liquid height. There are prior batch fill level alerts which warn the

operator that the predicted end of transfer is approaching, these are at 5 minute intervals

from 15 minutes before the predicted transfer completion. There is a normal fill level alert

and there are high and high high alarms, these are audible alarms within the control room

and are repeated at the jetty (on an alarm panel).

There is an independent high high level alarm, from separate high high level switches, hard

wired to the dual redundancy alarm PLC in the control room and fed to the UCOS system

as well as the mimic panel. This alarm is repeated through the PLC out to the jetty alarm

panel. The independent high high jetty alarm is continually active. There is no link

between the dual redundancy alarm PLC and the valve control system and the ATG

system. No extra credit has been applied for this high alarm within the LOPA. There is also

an independent high integrity Safety Instrument System that operates by closing a common

gasoline import valve in the event of a high level in any of the gasoline storage tanks.

In the event of a power failure, the terminal operator will contact the jetty to stop transfer.

The SCADA/UCOS system and mimic panel are on a UPS system however the alarm PLC

is currently not powered through the PLC so the high high level alarms will not operate.

The level monitoring on the tanks will fail. The common gasoline import valve will fail

closed stopping any receipt of gasoline.

All tank independent alarms will be generated on the SCADA.

A local loss of power to the alarm PLC would result in a failure of the independent high

high alarms and this would not be readily apparent to the operator although all tank

independent alarms will be generated on the SCADA.