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Skystone FRP Water Tank Explosion - NACE Calgary

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<strong>NACE</strong> International<br />

<strong>NACE</strong> <strong>Calgary</strong> International Section<br />

Non-Metallics Mini Symposium<br />

November 25, 2011


Examination of <strong>Explosion</strong> Failure of<br />

Aboveground <strong>FRP</strong> <strong>Water</strong> <strong>Tank</strong><br />

Alex Tatarov, Ph.D., P. Eng., Frank Gareau, P. Eng..


Failure Site


Operating Conditions<br />

• Pumpjack oil well.<br />

• Oil emulsion consisting of sweet natural gas, oil<br />

and water.<br />

• A treater separates the three phases.<br />

• The gas phase goes to a pipeline.<br />

• The oil and water phases are stored in<br />

atmospheric tanks and trucked away periodically.


<strong>Water</strong> And Oil Were Trucked Away<br />

• Treater (100<br />

bbl)<br />

• Three oil<br />

tanks (400 bbl<br />

each)<br />

• <strong>Water</strong> tank<br />

(400 bbl)


100 bbl Treater


Automatic Discharge Valves


Conditions Prior To Failure<br />

• Pumpjack was not operating.<br />

• Well valves were not closed, so the well was<br />

flowing.<br />

• Two oil tanks were empty. Third tank<br />

contained 6 feet of oil.<br />

• <strong>Water</strong> was trucked away two days prior to<br />

failure.<br />

• <strong>Water</strong> tank was almost empty. 1.5 feet of<br />

water from the bottom=30 bbl of water.


Conditions Prior To Failure<br />

• Good weather, no storms, no precipitation within last 24 hours.<br />

• Temperature from 9C to 19C (late April).<br />

• Nobody was on site at time of failure.


Damage At Top Of <strong>Water</strong> <strong>Tank</strong><br />

• Fire<br />

damage<br />

• Mechanical<br />

damage


Fire Damage At Top Of Failed <strong>Tank</strong>


Fire Triangle<br />

Confined space additionally required for explosion


Fuel Source 1: Gas From Oil <strong>Tank</strong>s<br />

• Upper parts of<br />

tanks are<br />

connected by 3<br />

inch overflow<br />

lines at the<br />

upper part of<br />

the shell, and<br />

by a 3 inch vent<br />

line at tank<br />

tops .


Fuel Source 2: Oil Film On <strong>Water</strong>


Fuel Source 3: Gas/Hydrocarbons<br />

Discharged From Treater With <strong>Water</strong><br />

• Pumping was shut down, but the well was still flowing.<br />

• Gas-to-Oil Ratio (GOR) changed.<br />

• More gas and light hydrocarbons came to a treater.<br />

• They came in more volatile manner.<br />

• <strong>Water</strong> discharge system could be activated to discharge liquid<br />

high in hydrocarbons.


Ignition Source<br />

1. Lightning Strike – Considered to be<br />

unlikely as good weather was reported.<br />

2. Heat – Discussed later; considered to be<br />

unlikely.<br />

3. Static electricity – Discussed later; most<br />

probable source.


Air Source: Thief Hatches<br />

• <strong>Water</strong> was<br />

trucked away<br />

prior to the<br />

failure<br />

• Thief-hatches<br />

(pressure 8 oz<br />

vacuum 4 oz)<br />

allowed air to<br />

get inside the<br />

tank


Two Possible Scenarios<br />

<strong>Water</strong> Dumping Scenario<br />

• Automatic discharge<br />

triggered water dumping.<br />

• <strong>Water</strong> dumping resulted in<br />

internal pressure increase.<br />

• High internal pressure blew<br />

the lid off.<br />

• Metal parts of the lid hit the<br />

railing, which resulted in<br />

sparking.<br />

• The gas-air mixture was<br />

ignited.<br />

Fire and <strong>Explosion</strong> Scenario<br />

• <strong>Water</strong> tank contained<br />

ignitable gas-air mixture<br />

• Ignition somehow occurred.<br />

• Gas burning resulted in<br />

increasing pressure and<br />

temperature.<br />

• High internal pressure blew<br />

the lid off.


<strong>Water</strong> Dumping Scenario:<br />

Possible Metal To Metal Spark


<strong>Water</strong> Dumping Scenario - Unlikely<br />

• The pressure increase due to water dump was calculated<br />

using the worst-case scenario:<br />

• All the thief-hatches are still closed (no gas escapes).<br />

• The flare line is completely plugged.<br />

• The entire volume of the treater filled with water.<br />

• All this water is dumped into the water tank.<br />

RESULTS:<br />

• ΔP = 1psi or 7.2% of 14 psi<br />

• <strong>Water</strong> flow 2 m 3 /min; 8 minutes to fill water tank<br />

• The maximum speed of water level rising is 19 cm/min.


External Fire And <strong>Explosion</strong> Scenario<br />

• Light hydrocarbons<br />

evaporated from the<br />

tanks during hot<br />

days and then<br />

condensed inside<br />

the valve at night.<br />

• Alternatively,<br />

measuring depth of<br />

oily water could<br />

contaminate the<br />

external surface.


Properties Of Common Hydrocarbons


Internal Spark and <strong>Explosion</strong> Scenario<br />

API Standard RP 2003 Protection Against Ignitions Arising Out of Static,<br />

Lightning, and Stray Currents in paragraph A.7 Ignition by Static<br />

Electricity states:<br />

• For an electrostatic charge to be a source of ignition, the following<br />

four conditions must be met:<br />

• a) a means of generating an electrostatic charge must be present;<br />

• b) a means of accumulating an electrostatic charge capable of<br />

producing an incendive spark;<br />

• c) a means of discharging the accumulated electrostatic charge in<br />

the form of an incendive spark (that is, a spark gap) must be<br />

present;<br />

• d) an ignitable vapor-air mixture must be present in the spark<br />

gap.


Internal Spark and <strong>Explosion</strong> Scenario<br />

• The electrostatic charge could be generated during flow of the<br />

water-oil mixture through pipes from the treater to the water<br />

tank.<br />

• The electrostatic charge could be accumulated on the oil<br />

surface, which is non-conductive.<br />

• All the pipes connected to the water tank were grounded.<br />

• The pipe openings to inside the tank contained plastic outlets.<br />

• The manway lid was non-metallic.<br />

• Bolts could not store energy necessary for ignition.<br />

• The length of the grounding cable was adequate, so it did not<br />

hang over the water surface.<br />

• No foreign conductive objects inside the tank.<br />

• There were no obvious spark gaps inside the water tank.


Static Electricity Spark Promoters<br />

• Non-conductive liquid<br />

• Metallic/conductive objects<br />

• Absence of grounding


Splash Filling<br />

NFPA 77 (Recommended Practice on Static Electricity)<br />

• Flow velocity of incoming liquid should be less than 1 m/sec until the outlet<br />

is submerged either two pipe diameters or 0.6 m, whichever is less.<br />

• For tank capacity of more than 50 m 3 , the inlet flow velocity could be<br />

increased to 7 m/sec after the fill pipe is submerged.


Fill Line Is Above Liquid Level<br />

• NFPA max. velocity for the non-submerged fill line V max = 1m/s<br />

• Inlet flow velocity V flow = 7.2 m/sec or ~ 7 times higher


Bottom Of Failed <strong>Tank</strong>


Failure Scenario<br />

• Flammable gas or gas-air mixture were present in water and oil tanks.<br />

• When the truck dumped the water, this mixture was sucked into the water<br />

tank through the overflow lines and through vent lines.<br />

• Air was sucked inside the water tank through thief hatches.<br />

• Thus the ignitable gas-air mixture was created inside the water tank.<br />

• A layer of oil was present on liquid surface in the water tank.<br />

• The well was still producing and the treater was in unusual and volatile<br />

conditions.<br />

• An automatic discharge releases hydrocarbons from the treater through<br />

water line.<br />

• Fluid containing hydrocarbons was splashed over the layer of oil in water<br />

tank with high velocity.<br />

• This resulted in a static electricity spark and gas ignition.<br />

• Ignition resulted in increase of gas pressure and temperature, and the lid<br />

blew off.


Proposed Modification


RECOMMENDATIONS<br />

• Minimize the chance of sparking due to static<br />

electricity. Install a non-conductive riser on the end<br />

of the drain outlet inside the water tank.<br />

• Eliminate or significantly reduce the oxygen level<br />

inside the tanks. Use fuel or sales gas to blanket the<br />

contents of both the water tank and the oil tanks.<br />

• Upgrade the automatic discharge system to a more<br />

reliable system.


QUESTIONS


CONTACT INFORMATION<br />

Alex Tatarov, Ph.D., P. Eng<br />

403-510-4394<br />

atatarov@skystone.ca<br />

Frank Gareau, P. Eng.<br />

403-516-4234<br />

fgareau@skystone.ca

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