austlii:sa/SAET/2025/59
General information, not legal advice.
SAET
2025-06-30
Mr P, Ms J
Original judgment source is linked above.
The first defendant, National Petroleum & Corrosion Services Pty Ltd (ABN 50 658 280 543), on 30 April 2022, at Mount Gambier in the State of South Australia, committed a Category 2 offence.
(A minor indictable offence against section 32 of the Work Health and Safety Act 2012).
(A minor indictable offence against section 32 of the Work Health and Safety Act 2012).
10. On 11 April 2022, Unigas[1] contacted NPCS via email to supply a quote to decommission the LPG tank.
11. On 13 April 2022, NPCS (via Mr Santilli) provided a quote to Unigas to decommission the LPG tank for $8,100 plus GST.
12. On 13 April 2022, Unigas accepted the quote and advised NPCS that the LPG tank contained approximately 1,280L of LPG which could not be dispensed out from the pump.
13. On 13 April 2022, NPCS advised Unigas that they did not have the resources to 'pump out' (empty) the LPG tank and would require Unigas to supply a tanker for this purpose.
14. On 14 April 2022, Unigas advised NPCS that the other contractors they engaged did the 'pump outs' themselves and that this would be an issue with most LPG tank decommissioning work moving forward.
15. On 19 April 2022, NPCS advised Unigas that they did not require a tanker and would instead empty the LPG tank by dispensing the remaining contents into 'fat boys' and then blow the remaining vapour down as per normal procedure.
On 2 May 2022, SafeWork SA was notified of the way in which the LPG tank was emptied by an email from Dr Suresh Kumar, Senior Environment Protection Officer with the EPA. On 25 May 2022, an inspector advised NPCS that it was prohibited from conducting any LPG tank decommissioning work. The direction was complied with. On 26 May 2022, the inspector issued NPCS with two notices. NPCS provided evidence of compliance with the notices on 12 July 2022.
LPG is a fuel gas which contains a flammable mixture of hydrocarbon gases specifically propane, n-butane and isobutane.
liquified petroleum gas means a liquid that is a mixture of hydrocarbons, basically consisting of butane or butenes, propane or propene, or any mixture of them, or 1 of them, and is a dangerous substance of Class 2, Dangerous Substances (General) Regulations 2017.
53. LPG is extremely flammable and reacts violently with oxidising agents.
54. LPG at atmospheric pressure and temperature is a gas which is 1.5 to 2.0 times heavier than air. As such, it would normally settle at ground level / low lying places and accumulate in depressions and may also travel to remote sources of ignition (i.e. along drainage systems).
55. LPG is colourless both in liquid and vapour phase. During leakage, the vaporisation of liquid cools the atmosphere and condenses the surrounding water vapour to form a whitish fog which makes it possible to see an escape of LPG.
56. LPG has a very low flash point and any spillage or leak is a fire and/or explosion hazard.
57. In order to prevent accidental ignition, it is imperative to eliminate all potential ignition sources (i.e. flame, spark or heat) which could trigger combustion or explosion leading to severe consequences.
58. LPG (in high concentrations) may cause asphyxiation and direct contact may cause cold burns.
59. The primary risk associated with LPG is the possibility of explosion.
60. LPG explosion requires three main elements: the presence of LPG, mixing with air and an ignition source.
61. LPG needs to mix with air in the right proportion - this specific range is called the flammable range and is between the Lower Explosive Limit (LEL) and the Upper Explosive Limit (UEL).
62. When LPG mixes with air and ignites, it undergoes an exothermic reaction - meaning it releases heat energy as a byproduct, as well as additional gaseous products of combustion (i.e. carbon dioxide and water vapour).
63. If a person is standing near an LPG leak and an ignition source is present, there is a substantial risk of death or serious injury from the resultant LPG explosion.
After taking into account weather conditions on 30 April 2022, and other relevant circumstances, Mr Satani calculated the lower explosive limit (LEL) and upper explosive limit (UEL) of the LPG release. Mr Satani calculated that the flammable limit of the released LPG was between 19 metres and 36 metres from the LPG tank. If concentration patchiness is taken into account, Mr Satani deposed that a high risk of ignition could exist between 28 metres and 55 metres. If an ignition source was present in the flammable limit, Mr Satani deposed that the most likely result would be either a flash fire or a jet fire. He deposed that a flash fire causes the vapour to burn quickly without generating significant pressure while a jet fire results from the ignition of a high velocity jet of gas and/or liquid.
I should add that the allegation of a fatal injury to the named employee is unnecessary but legally harmless. The consequence of a contravention of s 19(1) is relevant to the question of penalty, but is not an element of the offence.[12]
[1] The LPG tank was owned and maintained by Elgas Autogas Pty Ltd & Unigas Transport Fuels Pty Ltd t/a Unigas Partnership (Unigas). Unigas contracted NPCS to decommission the LPG tank.
[3] Informant's written submissions [53]-[63].
[4] Informant's written submissions [39].
[6] Affidavit affirmed on 24 March 2024, BoD 23 - 53 at 28, [25].
[12] Sections 19, 22 and 58 of the Occupational Health Safety and Welfare Act 1986 concern duties owed by employers and breaches thereof and are similar to, and have been replaced by, ss 30 to 34 of the WHS Act.
Farrell
National Petroleum & Corrosion Services Pty Ltd
(2005) 228 CLR 357
(1999) 90 IR 464
(2004) 60 NSWLR 168
(1988) 166 CLR 59