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Introduction to Fire Safety Management

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Figure 8.16 External tank facility<br />

The principles of safety relating <strong>to</strong> both chemicals<br />

and LPG are similar in many ways and it is intended <strong>to</strong><br />

consider these overall principles for each hazardous<br />

material as one, with specifi c areas of difference being<br />

highlighted.<br />

Substitution<br />

Ideally the use, s<strong>to</strong>rage, etc. of fl ammable chemicals<br />

and substances and LPG should be avoided where reasonably<br />

practicable. The same can be said for using low<br />

fl ashpoint liquids. Other chemicals, substances or liquids,<br />

which are either non-fl ammable or have a higher fl ashpoint,<br />

may provide suitable safer alternatives.<br />

It must also be noted that reactive chemicals whose<br />

properties in themselves are non-fl ammable, but may<br />

react violently even explosively when mixed <strong>to</strong>gether,<br />

should also be considered in relation <strong>to</strong> substituting<br />

them for less reactive materials.<br />

S<strong>to</strong>rage<br />

Where substitution cannot be accommodated, the provision<br />

of safe s<strong>to</strong>rage must be considered as a key element<br />

in reducing the fi re and explosion risks from the<br />

hazardous materials.<br />

Ideally, arrangements should be made for s<strong>to</strong>rage of<br />

fl ammable liquids, gases and substances <strong>to</strong> be s<strong>to</strong>red<br />

well away from other processes and general s<strong>to</strong>rage<br />

areas. This is most effectively achieved by a physical<br />

distance. An alternative approach may be <strong>to</strong> provide a<br />

physical barrier such as a wall or partition, combined<br />

with a s<strong>to</strong>rage system or container.<br />

If the s<strong>to</strong>rage facility is <strong>to</strong> be located within a<br />

building and the hazardous materials are <strong>to</strong> be handled<br />

within the area around the s<strong>to</strong>re fi re resisting separation<br />

from other areas of the building or workplace should be<br />

considered.<br />

Causes and prevention of fi re<br />

Table 8.3 Minimum separation distances<br />

Quantity s<strong>to</strong>red Distance from occupied<br />

litres building, boundary, process<br />

unit, fl ammable liquid s<strong>to</strong>rage<br />

tank or fi xed ignition source<br />

metres<br />

Up <strong>to</strong> 1 000 2<br />

1 000–100 000 4<br />

Above 100 000 7.5<br />

The arrangements for s<strong>to</strong>ring fl ammable substances<br />

and LPG will depend upon the s<strong>to</strong>rage facilities available,<br />

the amount of hazardous materials and the nature<br />

of the materials.<br />

External s<strong>to</strong>rage arrangements – when s<strong>to</strong>ring<br />

large quantities (50 litres or more) ideally an external<br />

s<strong>to</strong>rage area will be provided that will include the following<br />

considerations:<br />

➤ Segregation from other processes and s<strong>to</strong>rage<br />

(fl ammable substances should be s<strong>to</strong>red separately<br />

from other hazardous substances and materials<br />

such as oxidisers and LPG, etc.):<br />

➤ By physical distance<br />

➤ <strong>Fire</strong> wall<br />

➤ Security against unauthorised access, locking<br />

mechanisms, physical walls and fences<br />

➤ Positioned in a well-ventilated area and on impervious<br />

ground<br />

➤ Take in<strong>to</strong> account the potential heat on the containers<br />

from a fi re within or outside the premises’<br />

boundary; and a fi re within the s<strong>to</strong>rage facility on<br />

buildings, plant and people inside or outside the<br />

premises<br />

➤ Positioned away from sources of ignition (or where<br />

electrical supplies are intrinsically safe)<br />

➤ Environmental protection arrangements:<br />

➤ Bunded facility (110% of contents)<br />

➤ Intercep<strong>to</strong>rs <strong>to</strong> capture potential release<br />

The acknowledged safe separation distances are<br />

detailed in Table 8.3.<br />

The arrangements for the s<strong>to</strong>ring of larger quantities<br />

(more than 300 kg) of LPG gas cylinders are very similar<br />

<strong>to</strong> those required for fl ammable liquids.<br />

In addition <strong>to</strong> providing adequate levels of signage<br />

on site, formal systems of work will need <strong>to</strong> be<br />

151

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