Boilover

A boilover is an extremely hazardous phenomenon in which a layer of water under a pool fire starts boiling, which results in a significant increase in fire intensity accompanied by violent expulsion of burning fluid to the surrounding areas. Boilover can only occur if the liquid fluid is a mixture of different chemical species with sufficiently diverse boiling points, although a so-called thin-layer ''boilover – a far less hazardous phenomenon – can arise from any water-immiscible liquid fuel. Crude oil, kerosene and some diesel oils are examples of fuels giving rise to boilover.
Boilovers at industrial scale are rare but can lead to serious plant damage. Given the sudden and not easily predictable onset of the phenomenon, fatalities can occur, especially among firefighters and bystanders that have not been made to leave the area.
Slopover and frothover'' are phenomena similar to boilover but distinct from it. A slopover occurs when pouring water over a liquid pool fire, which may result in sudden expulsion of blazing fluid as well as considerable flame growth if the fire is small, as is the case when dousing water over a chip pan fire. A frothover is a situation occurring when there is a layer of water under a layer of a viscous fuel that, although not on fire, is at higher temperature than the boiling point of water.

Features

The extreme violence of boilovers is due to the expansion of water from liquid to steam, which is by a factor of 1500 or more. In practical storage scenarios, the presence of water under the burning fluid is sometimes due to spurious accumulation during plant operation or as a consequence of attempts to extinguish the fire with water. A typical scenario for a tank fire that may eventually result in boilover is an initial confined explosion blowing off the tank roof.
Pure chemical species are not liable to boilover. In order for one to occur, the material must be a mixture of species with sufficiently diverse boiling points. Crude oil and some commercial hydrocarbon mixtures, such as kerosene and some diesel oils, are examples of such materials. The fact that these are stored in large atmospheric tanks in refineries, tank farms, power stations, etc. makes boilover a hazard of interest in terms of process safety. During a pool fire, a distillation process takes place in the fuel. Separation of light components from heavier ones occurs thanks to convective fluid motion. An intermediate fuel layer, called the hot zone or heat wave, is formed, which becomes progressively richer in higher-boiling-point species. Its temperature, as well as thickness, progressively increase. Its lower boundary moves downwards towards the fuel–water interface at a speed higher than the overall level of fuel decreases due to the fire burning it. As a result, when the hot zone reaches the water layer, a considerable amount of unburnt fuel may still be present above the water. Upon the water contacting the hot zone, some steam forms. The resulting turbulence promotes mixing of the water into the hot fuel. This can result in rapid water vaporization. The violent expansion of the steam bubbles will push out a significant part of the fuel above it, causing a violent overflow of flaming liquid. In these conditions water may be superheated, in which case part of it goes through an explosive boiling with homogeneous nucleation of steam. When this happens, the abruptness of the expansion further enhances the expulsion of blazing fuel. Typical hot-zone speeds are 0.3–0.5 meters per hour, although speeds of up to 1.2 meters per hour have been recorded.
Apart from the presence of a water layer under the fuel, other conditions must be met for a hot-zone boilover to occur:

Since the upper fuel layers, including the hot zone, are at or near their boiling temperature, it is necessary for the boiling point of the fuel to be high enough, such that the hot zone temperature is higher than the water boiling temperature. Both the effect of the static head of fuel above the water and the fact that the hot zone composition is different from that of the initial fuel have to be considered. In general, boilover is possible if the fuel mean boiling point is higher than :
As mentioned above, the composition of the fuel mixture must be sufficiently varied. It has been observed that the gap between and the higher value between and the boiling point of water at the fuel–water interface has to be higher than 60 °C :Some sources indicate that the upper range of the boiling temperature has to be above :
The fuel viscosity must be sufficiently high to oppose the upwards movement of the steam bubbles. Otherwise, these may flow through the fuel without projecting it out of the blazing tank. Low viscosity may also make it difficult for a stable heavy-components hot zone to form, thanks to more efficient natural convection. Thus, experiments on gasoline pool fires have shown that boilover does not occur. In general, fuel dynamic viscosity has to be higher at least 0.73 cSt, which is the viscosity of kerosene.

The hazards posed by a hot-zone boilover are significant for several reasons. At industrial scale, hydrocarbon tanks can contain up to hundreds of thousands of barrels of fluid. If a boilover occurs, the amount of blazing liquid erupting from the tank can therefore be huge. Ejected blazing fluids can travel at speeds up to and attain distances well in excess of the limits of secondary containment bunding, often hundreds of meters or in the order of ten tank diameters downwind. Bunding, however, remains an important measure to reduce fire spread. Moreover, since boilover inception is sometimes unpredictable —either in terms of time to onset or whether it will occur at all — the impact on the firefighters that have intervened to control the fire can be deadly. In some cases, simple bystanders were caught in the blaze and perished.
Tank fires that appear to be relatively stable may burst into massive boilovers several hours after the fire starts, as it occurred in the Tacoa disaster. Failure to appreciate the hazards posed by a water layer underneath the fuel has been a significant contributing cause to the aftermath of boilover accidents, in terms of human and material losses. Uncertainty surrounding the time to boilover onset adds unpredictability that further complicates the efforts of the firefighting services. Mathematical models for boilover have been developed that predict the time necessary for boilover to initiate, among other things.

Notable accidents

The following are some notable accidents in which a standard, or hot-zone, boilover occurred:

20 January 1968, Shell refinery, Pernis, The Netherlands – Water emulsion and hot crude oil mixed and produced frothing, vapor release and boilover. The fire spread, destroying several refinery units and 80 tanks.
26 June 1971, Czechowice-Dziedzice oil refinery, Poland – A -diameter crude oil tank was hit by lightning, which caused a roof collapse and an open-top tank fire. After extended firefighting and a decrease in the fire intensity, boilover occurred, spewing flaming liquids up to away. A nearby tank exploded due to ignition of flammable vapors inside. Thirty-three people died.
19 December 1982, Ricardo Zuloaga thermal power plant in Tacoa, Vargas, Venezuela – In the Tacoa disaster more than 150 people, including journalists and bystanders not involved in fighting the fire, died when a massive boilover developed from a fuel oil tank. It is the worst tank fire ever occurred worldwide.
30 August 1983, Amoco oil refinery, Milford Haven, Wales – An open-top tank fire occurred at a crude storage tank. Filled with more than 46,000 tons of oil, the flaming storage tank experienced multiple boilovers, spreading the fire into the containment dyke. However, the fire did not propagate further. In all, 150 firefighters and 120 fire appliances were needed to tackle the blaze. While six firefighters were injured during the two-day fire, no one was killed.
Related phenomena

Thin-layer boilover

A thin-layer boilover occurs in one of two situations:

When the fuel layer is thin, such as in the case of spillage on a wet surface. In this case the boilover onset time is very short, typically about one minute.
When, regardless of the thickness of the fuel layer, distillation does not occur and a heat wave is not formed. In such a situation, for a boilover to occur, the fuel has to burn down until its warmer top layer reaches the fuel–water interface.

In a thin-layer boilover, the size of the flames increases upon boilover onset, and a characteristic crackling sound is produced. However, due to the little amount of fuel left, this phenomenon is far less hazardous than a standard boilover. The study of thin-layer boilover is of interest in the context of in-situ burning of oil spills over water.

Slopover

A slopover is a phenomenon similar to boilover, although distinct from it. It occurs when water is poured onto the fuel while a pool fire is occurring. If the fire is small enough, the water that instantly boils in contact with the fire or with the lower layers of blazing liquid can extend the flames, especially in the upwards direction.
In industrial-scale tank fires, there is no noticeable effect when water is doused on the fire, although water sinking to the bottom of the tank may contribute to a later boilover. However, at smaller scale, slopovers pose significant hazards. Trying to extinguish a chip pan or cooking oil fire with water, for example, causes slopover, which can harm people and spread the fire in the kitchen. Serious burn incidents have also occurred during Mid-autumn Festival celebrations, where boiling candlewax and pouring water on it for entertainment has become a habit.

Frothover

A frothover occurs when a water layer is present under a layer of a viscous oil that is not on fire and whose temperature is higher than the water boiling point. An example is hot asphalt loaded into a tank car containing some water. Although nothing may happen at first, water may eventually superheat and later start to boil violently, resulting in overflow.