Knowledge (XXG)

Flixborough disaster

Source πŸ“

337:(mostly chemical engineers), the post of Works Engineer which had been occupied by a chartered mechanical engineer had been vacant since January 1974, and at the time of the accident there were no professionally qualified engineers in the works engineering department. Nypro had recognised this to be a weakness and identified a senior mechanical engineer in an NCB subsidiary as available to provide advice and support if requested. At a meeting of plant and engineering managers to discuss the failure of reactor 5, the external mechanical engineer was not present. The emphasis was upon prompt restart and – the inquiry felt – although this did not lead to the deliberate acceptance of hazards, it led to the adoption of a course of action whose hazards (and indeed engineering practicalities) were not adequately considered or understood. The major problem was thought to be getting reactor 5 moved out of the way. Only the plant engineer was concerned about restarting before the reason for the failure was understood, and the other reactors inspected. The difference in elevation between reactor 4 outlet and reactor 6 inlet was not recognised at the meeting. At a working level the offset was accommodated by a dog-leg in the bypass assembly; a section sloping downwards inserted between (and joined with by mitre welds) two horizontal lengths of 20-inch pipe abutting the existing 28-inch stubs. This bypass was supported by scaffolding fitted with supports provided to prevent the bellows having to take the weight of the pipework between them, but with no provision against other loadings. The Inquiry noted on the design of the assembly: 380:" at a high temperature while the pipe was under pressure. The metal of the pipe would have experienced hard-to-detect deformation, microscopic cracks, and structural weakness as a result, increasing the likelihood of failure. Failure had been accelerated by contact with molten zinc; there were indications that an elbow in the pipe had been at significantly higher temperature than the rest of the pipe. The hot elbow led to a non-return valve held between two pipe flanges by twelve bolts. After the disaster, two of the twelve bolts were found to be loose; the inquiry concluded that they were probably loose before the disaster. Nypro argued that the bolts had been loose, there had consequently been a slow leak of process fluid onto lagging leading eventually to a lagging fire, which had worsened the leak to the point where a flame had played undetected upon the elbow, burnt away its lagging and exposed the line to molten zinc, the line then failing with a bulk release of process fluid which extinguished the original fire, but subsequently ignited giving a small explosion which had caused failure of the bypass, a second larger release and a larger explosion. Tests failed to produce a lagging fire with leaked process fluid at process temperatures; one advocate of the 8-inch hypothesis then argued instead that there had been a gasket failure giving a leak with sufficient velocity to induce static charges whose discharge had then ignited the leak. 579:; for minor modifications a checklist-based safety assessment was to be used, indicating what aspects would be affected, and for each aspect giving a statement of the expected effect. The modification and its supporting safety assessment then had to be approved in writing by the plant manager and engineer. Where instruments or electrical equipment were involved signatures would also be needed from the relative specialist (instrument manager or electrical engineer). A Pipework Code of Practice was introduced specifying standards of design construction and maintenance for pipework – all pipework over 3"nb (DN 75 mm) handling hazardous material would have to be designed by pipework specialists in the design office. The approach was publicised outside ICI; while the Pipework Code of Practice on its own would have combatted the fault or faults that led to the Flixborough disaster, the adoption more generally of tighter controls on modifications (and the method by which this was done) were soon recognised to be prudent good practice. In the United Kingdom, the ICI approach became a 365:
setting. However theoretical modelling suggested that the expansion of the bellows as a result of this would lead to a significant amount of work being done on them by the reactor contents, and there would be considerable shock loading on the bellows when they reached the end of their travel. If the bellows were 'stiff' (resistant to deformation), the shock loading could cause the bellows to tear at pressures below the safety valve setting; it was not impossible that this could occur at pressures experienced during start-up, when pressure was less tightly controlled. (Plant pressures at the time of the accident were unknown since all relevant instruments and records had been destroyed, and all relevant operators killed). The Inquiry concluded that this ("the 20-inch hypothesis") was 'a probability' but one 'which would readily be displaced if some greater probability' could be found.
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minor modifications there was less control and this had resulted in a past history of 'near-misses' and small-scale accidents, few of which could be blamed on chemical engineers. To remedy this, not only were employees reminded of the principal points to consider when making a modification (both on the quality/compliance of the modification itself and on the effect of the modification on the rest of the plant), but new procedures and documentation were introduced to ensure adequate scrutiny. These requirements applied not only to changes to equipment, but also to process changes. All modifications were to be supported by a formal safety assessment. For major modifications this would include an
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goes wrong, are readily ignored in day-to-day work. Where management lays down safety rules, it must also ensure that they are carried out. We believe that to this end considerable formality is essential in relation to such matters as permits to work and clearance certificates to enter vessels or plant areas. In order to keep strong control in the plant, the level of authority for authorisations must be clearly defined. Similarly the level of authority for technical approval for any plant modification must also be clearly defined. To avoid the danger of systems and procedures being disregarded, there should be a requirement for a periodic form of audit of them.
279:(700mm DN), 20-inch nominal bore pipe (500mm DN) was used to fabricate the bypass pipe for linking reactor 4 outlet to reactor 6 inlet. The new configuration was tested for leak-tightness at working pressure by pressurisation with nitrogen. For two months after fitting the bypass was operated continuously at temperature and pressure and gave no trouble. At the end of May (by which time the bypass had been lagged) the reactors had to be depressurised and allowed to cool in order to deal with leaks elsewhere. The leaks having been dealt with, early on 1 June attempts began to bring the plant back up to pressure and temperature. 22: 98: 481:
overlook obvious defects which in other circumstances they would not have failed to realise'. Of one proponent the report noted gratuitously that his examination by the court 'was directed to ensuring that we had correctly appreciated the main steps in the hypothesis some of which appeared to us in conflict with facts which were beyond dispute'. The report thanked him for his work in assembling eyewitness evidence but said his use of it showed 'an approach to the evidence which is wholly unsound'.
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design or operational procedures or both". The company would have to show that "it possesses the appropriate management system, safety philosophy, and competent people, that it has effective methods of identifying and evaluating hazards, that it has designed and operates the installation in accordance with appropriate regulations, standards and codes of practice, that it has adequate procedures for dealing with emergencies, and that it makes use of independent checks where appropriate"
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build a nuclear power plant, the electricity industry must provide a detailed safety evaluation to the Nuclear Inspectorate before it receives a licence. On the other hand, permission for highly hazardous process plants only involves satisfying a technically unqualified local planning committee, which lacks even the most rudimentary powers once the plant goes on stream. ... The Factory Inspectorate has standing only where it has promulgated specific regulations
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mitre joints. No calculations were done to ascertain whether the bellows or pipe would withstand these strains; no reference was made to the relevant British Standard, or any other accepted standard; no reference was made to the designer's guide issued by the manufacturers of the bellows; no drawing of the pipe was made, other than in chalk on the workshop floor; no pressure testing either of the pipe or the complete assembly was made before it was fitted.
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pressure tests showed the bellows did not develop tears until well above the safety valve pressure. This hypothesis has however been revived, with the tears being caused by fatigue failure at the top of the reactor 4 outlet bellows because of flow-induced vibration of the unsupported bypass line. Finite element analysis has been carried out (and suitable eyewitness evidence adduced) to support this hypothesis.
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created any unacceptable risk. The disaster was caused wholly by the coincidence of a number of unlikely errors in the design and installation of a modification. Such a combination of errors is very unlikely ever to be repeated. Our recommendations should ensure that no similar combination occurs again and that even if it should do so, the errors would be detected before any serious consequences ensued.
208:(HSE) planning permission for storage of 1,200 te LPG at Flixborough was initially granted subject to HSE approval, but HSE objected); as a result of a subsequent collapse in the price of nylon it closed down a few years later. The site was demolished in 1981, although the administration block still remains. The site today is home to the Flixborough Industrial Estate, occupied by various businesses and 49:, England, on Saturday, 1 June 1974. It killed 28 and seriously injured 36 of the 72 people on site at the time. The casualty figures could have been much higher if the explosion had occurred on a weekday, when the main office area would have been occupied. A contemporary campaigner on process safety wrote "the shock waves rattled the confidence of every chemical engineer in the country". 389:
inquiry identified difficulties at various stages of the accident development in the 8-inch hypothesis, their cumulative effect being considered to be such that the report concluded that overall the 20-inch hypothesis involving 'a single event of low probability' was more credible than the 8-inch hypothesis depending upon 'a succession of events, most of which are improbable'.
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gas or liquid on the plant was not usually large. Now pipe-lines are much larger and the amount of gas or liquid that can leak out is much greater. Several serious incidents in the last three years have shown that we dare not risk breaking into lines that are not properly isolated. As plants have got larger we have moved ... into a new world where new methods are needed.
248:. The reactors were constructed from mild steel with a stainless steel lining; when operating they held in total about 145 tonnes of flammable liquid at a working pressure of 8.6 bar gauge (0.86 MPa gauge; 125 psig). In each of the reactors, compressed air was passed through the cyclohexane, causing a small percentage of the cyclohexane to oxidise and produce 449:
that plants at which there is a risk of instant as opposed to escalating disaster be identified. Once identified measures should be taken both to prevent such a disaster so far as is possible and to minimise its consequences should it occur despite all precautions.' There should be coordination between planning authorities and the
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and there was no route for excess pressure to escape; pressure was kept within acceptable limits (slightly wider than those achieved under automatic control) by operator intervention (manual operation of vent valves). A pressure-relief valve acting at 11 kgf/cm (11 bar; 156 psi) gauge was also fitted.
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postulated that there had been bulk water in reactor 4 and a disruptive boiling event had occurred when the interface between it and the reaction mixture reached operating temperature. Abnormal pressures and liquor displacement resulting from this (it was argued) could have triggered failure of the 20-inch bypass.
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come up with a 'shopping list' of about 30 recommendations on plant design, many of which had not been adopted (and a few explicitly rejected) by the Inquiry Report; the HSE inspector who acted as secretary to the inquiry spoke afterwards of making sure that the real lessons were acted upon. More fundamentally,
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reached a state of technological development where it is not sufficient in areas of high risk for employers merely to demonstrate to themselves that all is well. They should now be required to demonstrate to the community as a whole that their plants are properly designed, well constructed and safely operated.
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and after the accident only two possible sites for leaks before the explosion were identified: "the 20 inch bypass assembly with the bellows at both ends torn asunder was found jack-knifed on the plinth beneath" and there was a 50-inch long split in nearby 8-inch nominal bore stainless steel pipework".
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e.g. for one pipe work mod "the plant engineer had not considered it necessary to consult the piping experts, as the pipe was straight, without any bends... As at Flixborough there was a failure to recognise the circumstances in which expert advice should have been sought" – the problem being spotted
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problems: he notes that post-inquiry work on behalf of HSE showed that nitrate stress corrosion cracking only occurs in mild steel in areas subject to abnormal stress; the failure of reactor 5 therefore required not only the presence of nitrate in the cooling water, but some inadequacy in the reactor
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Press reporting of both has included the suggestion that the new hypothesis clears the dead operators of the slur of having caused the accident; in fact none of the competing theories makes that claim – unless it is felt that the inquiry report's explicit refusal to blame 'pilot error' by the dead is
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ICI Petrochemicals Safety Newsletter 60 (January 1974) summarised a published 1973 conference paper as follows: Unconfined vapour cloud explosions had been experienced since the 1930s; by the early 1970s there had been about 100 known incidents, with about 5 more every year. Significant overpressures
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In its first report (issued as a basis for consultation and comment in March 1976), the ACMH noted that hazard could not be quantified in the abstract, and that a precise definition of 'major hazard' was therefore impossible. Instead installations with an inventory of flammable fluids above a certain
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If the UK public were largely reassured to be told the accident was a one-off and should never happen again, some UK process safety practitioners were less confident. Critics felt that the Flixborough explosion was not the result of multiple basic engineering design errors unlikely to coincide again;
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The plant design had assumed that the worst consequence of a major leak would be a plant fire and to protect against this a fire detection system had been installed. Tests by the Fire Research Establishment had shown this to be less effective than intended. Moreover, fire detection only worked if the
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he Court's commitment for the 20-inch hypothesis led them to present their conclusions in a way that does not help the reader to assess contrary evidence. The Court could still be right that a single unsatisfactory modification caused the disaster but this is no reason for complacency. There are many
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No-one appreciated that the pressurised assembly would be subject to a turning moment imposing shear forces on the bellows for which they are not designed. Nor did anyone appreciate that the hydraulic thrust on the bellows (some 38 tonnes at working pressure) would tend to make the pipe buckle at the
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At about 16:53 on 1 June 1974, there was a massive release of hot cyclohexane in the area of the missing reactor 5, followed shortly by ignition of the resulting huge cloud of flammable vapour and a massive explosion in the plant. The explosion virtually demolished the site. As it was a weekend there
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was stripped from it, a crack extending about 6 feet (1.8 m) was visible in the mild steel shell of the reactor. It was decided to install a temporary pipe to bypass the leaking reactor to allow continued operation of the plant while repairs were made. In the absence of 28-inch nominal bore pipe
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The change in scale was real and much larger than anything experienced since (in 1956 a typical ethylene plant might have a capacity of 30, 000 tpa; in 1974 ICI and BP planned an ethylene plant with a capacity of 500, 000 tpa; as of 2014 an 830,000 tpa unit is still one of the largest in Europe) but
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was the best-fit estimate of – the gist of their paper is given in the Second Report of the Advisory Committee on Major Hazards. TNT equivalence is now thought less useful than more modern approaches to characterisation of vapour cloud explosions and there are no directly comparable estimates of TNT
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HSE could then choose to – in some cases (generally involving high risk or novel technology) – require submission of a more elaborate assessment, covering (as appropriate) "design, manufacture, construction, commissioning, operation and maintenance, as well as subsequent modifications whether of the
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In accordance with this view, post-Flixborough (and without waiting for the Inquiry Report), ICI Petrochemicals instituted a review of how it controlled modifications. It found that major projects requiring financial sanction at a high level were generally well-controlled, but for more (financially)
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The proponent of the 8-inch gasket failure hypothesis responded by arguing that the 20-inch hypothesis had its share of defects which the inquiry report had chosen to overlook, that the 8-inch hypothesis had more in its favour than the report suggested, and that there were important lessons that the
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The claim argued by experts retained by Nypro and their insurers was that the disaster's cause was that the 20-inch bypass was not what would have been produced or accepted by a more considered process. Controversy developed (and became acrimonious) as to whether its failure was the initiating fault
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The Secretary of State for Employment set up a Court of Inquiry to establish the causes and circumstances of the disaster and identify any immediate lessons to be learned, and also an expert committee to identify major hazard sites and advise on appropriate measures of control for them. The inquiry,
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The occupants of the works laboratory had seen the release and evacuated the building before the release ignited; most survived. None of the 18 occupants of the plant control room survived, nor did any records of plant readings. The explosion appeared to have been in the general area of the reactors
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Although the operating pressure was maintained by an automatically controlled bleed valve once the plant had reached steady state, the valve could not be used during start-up, when there was no air feed, the plant being pressurised with nitrogen. During start-up the bleed valve was normally isolated
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We would not contest that the best run companies achieve high standards of safety, but we believe this is because they have .... achieved what is perhaps best described as technical discipline in all that they do. We believe that the best practices must be followed by all companies and that we have
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The rarity of major disasters tends to breed complacency and even a contempt for written instructions. We believe that rules relevant to safety must be everyday working rules and be seen as an essential part of day-to-day work practice. Rules, designed to protect those who drew them up if something
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The ACMH's terms of reference were to identify types of (non-nuclear) installations posing a major hazard, and advise on appropriate controls on their establishment, siting, layout, design, operation, maintenance and development (including overall development in their vicinity). Unlike the Court of
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standard for high-risk plant (partly because the new (1974) Health and Safety at Work Act went beyond specific requirements on employers to state general duties to keep risks to workers as low as reasonably practicable and to avoid risk to the public so far as reasonably practicable; under this new
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managed for 45 years without them. During those 45 years there were no doubt many occasions when fitters broke into equipment and found it had not been isolated, or broke into the wrong line because it had not been identified positively. But pipe-lines were mostly small, and the amount of flammable
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but ICI felt that saying that most accidents were caused by human error was no more useful than saying that most falls are caused by gravity. ICI had not simply reminded operators to be more careful, but issued explicit instructions on the required quality of isolations, and the required quality of
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There are now probably more than a dozen British petrochemical plants with a similar devastation-potential to the Nypro works at Flixborough. Neither when they were first built, nor now that they are in operation, has any local or government agency exercised effective control over their safety. To
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approval by the local council; while "an interdepartmental procedure enabled planning authorities to call upon the advice of Her Majesty's Factory Inspectorate when considering applications for new developments which might involve a major hazard" (there was no requirement for them to do so), since
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Nypro's advisers had put considerable effort into the 8-inch hypothesis, and the inquiry report put considerable effort into discounting it. The critique of the hypothesis spilled over into criticism of its advocates: 'the enthusiasm for the 8-inch hypothesis felt by its proponents has led them to
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The Inquiry noted further that "there was no overall control or planning of the design, construction, testing or fitting of the assembly nor was any check made that the operations had been properly carried out". After the assembly was fitted, the plant was tested for leak-tightness by pressurising
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Disasters on the scale of last Saturday's tragic explosion ... at Flixborough tend to provoke a brief wave of statements that such things must never happen again. With the passage of time these sentiments are diluted into bland reports about human error and everything being well under control – as
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so that liquid entered the reactors at a low level; the exiting liquid flowed over a weir whose crest was somewhat higher than the top of the outlet pipe. The mixture exiting reactor 6 was processed to remove reaction products, and the unreacted cyclohexane (only about 6% was reacted in each pass)
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therefore could be destroyed by a single failure and had a much greater risk of killing workers than the designers had intended. Critics of the inquiry report therefore found it hard to accept its characterisation of the plant as 'well-designed'. The HSE (through the Department of Employment) had
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We believe, however, that if the steps we recommend are carried out, the risk of any similar disaster, already remote, will be lessened. We use the phrase "already remote" advisedly for we wish to make it plain that we found nothing to suggest that the plant as originally designed and constructed
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No one concerned in the design or construction of the plant envisaged the possibility of a major disaster happening instantaneously. It was now apparent that such a possibility exists where large amounts of potentially explosive material are processed or stored. It was 'of the greatest importance
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The 8-inch hypothesis was claimed to be supported by eyewitness accounts and by the apparently anomalous position of some debris post-disaster. The inquiry report took the view that explosions frequently throw debris in unexpected directions and eyewitnesses often have confused recollections. The
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Experimental work carried out for HSE in 2000 confirmed that the vapour pressure of cyclohexane at 155Β°C is well below plant operating pressure; likewise that of water, but the vapour pressure of immiscible liquids is nearly additive and at operating temperature the sum of vapour pressures would
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Safety documents were needed both for design and operation. The management of major hazard installations must show that it possessed and used a selection of appropriate hazard recognition techniques, had a proper system for audit of critical safety features, and used independent assessment where
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but not necessarily best practice: some adopters of the approach have felt -or been made to feel- a danger of a group mindset where no off-plant personnel are involved (and the safety culture is not that of ICI) and therefore added a requirement for approval by a responsible person off-plant to
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The ACMH's second report (1979) rejected criticisms that since accidents causing multiple fatalities were associated with extensive and expensive plant damage the operators of major hazard sites had every incentive to avoid such accidents and so it was excessive to require major hazard sites to
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Tests on replica bypass assemblies showed that deformation of the bellows could occur at pressures below the safety valve setting, but that this deformation did not lead to a leak (either from damage to the bellows or from damage to the pipe at the mitre welds) until well above the safety valve
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design leading to high local stress. (The crack skirted a 28" branch, and King is reported elsewhere to have claimed an HSE source had told him that the reactors had been designed against a 9 t thrust upon these branches, not the 38t thrust the inquiry noted the bypass 'design' to have ignored)
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For most 'notifiable installations' no further explicit controls should be needed; HSE could advise and if need be enforce improvements under the general powers given it by the 1974 Health and Safety at Work Act (HASAWA), but for a very few sites explicit licensing by HSE might be appropriate;
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The enquiry noted the existence of a small tear in a bellows fragment, and therefore considered the possibility of a small leak from the bypass having led to an explosion bringing the bypass down. It noted this to be not inconsistent with eyewitness evidence, but ruled out the scenario because
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The inquiry report identified 'lessons to be learned' which it presented under various headings; 'General observation' (relating to cultural issues underlying the disaster), 'specific lessons' (directly relevant to the disaster, but of general applicability) are reported below; there were also
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The reactors were normally mechanically stirred but reactor 4 had operated without a working stirrer since November 1973; free phase water could have settled out in unstirred reactor 4 and the bottom of reactor 4 would reach operating temperature more slowly than the stirred reactors. It was
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site (including one in which cyclohexane was oxidised to cyclohexanone and cyclohexanol). Historically good process safety performance at Wilton had been marred in the late 1960s by a spate of fatal fires caused by faulty isolations/handovers for maintenance work. Their immediate cause was
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The HSE website as of 2014 said that "During the late afternoon on 1 June 1974 a 20 inch bypass system ruptured, which may have been caused by a fire on a nearby 8-inch pipe". In the absence of a strong consensus for either hypothesis other possible immediate causes have been suggested.
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A leak had developed on the air feed to the reactor, and a water spray had been put on it as a prudent precaution against hot cyclohexane reaching the leak site. The water spray had been nitrate dosed and after the crack was discovered DSM advised that nitrates were known to promote
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also being produced. Each reactor was slightly (approximately 14 inches, 350 mm) lower than the previous one, so that the reaction mixture flowed from one to the next by gravity through nominal 28-inch bore (700mm DN) stub pipes with inset bellows. The inlet to each reactor was
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equivalence for the Buncefield event. However, gives a graphical presentation of the raw data (overpressure inferred from damage vs distance from explosion source) for Flixborough (Fig 3.1.2) (in which the data is bounded by TNT equivalent curves for 11.2 t and 60t) and for the
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The foundations of properties severely damaged by the blast and subsequently demolished can be found on land between the estate and the village, on the route known as Stather Road. A memorial to those who died was erected in front of offices at the rebuilt site in 1977. Cast in
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The regulation by company procedures of safety matters (such as: identification of hazards, control of maintenance (through clearance certificates, permits to work etc.), control of modifications which might affect plant integrity, emergency operating procedures, access
535:– instead processes and plant were selected on other grounds then safety systems bolted on to a design with avoidable hazards and unnecessarily high inventory. 'We keep a lion and build a strong cage to keep it in. But before we do so we should ask if a lamb might do.' 133:
was partially oxidised by compressed air. The plant was intended to produce 70,000 tons per annum (tpa) of caprolactam but was reaching a rate of only 47,000 tpa in early 1974. Government controls on the price of caprolactam put further financial pressure on the plant.
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in the same year, it led to (and is often quoted in justification of) a more systematic approach to process safety in UK process industries. UK government regulation of plant processing or storing large inventories of hazardous materials is currently under the
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Although this is not commented upon in the reference, the basic physics would suggest that interfacial boiling could be triggered not only by increasing temperature with pressure steady but also by -with temperature steady – reducing pressure e.g. by manual
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other lessons. It is to be hoped that the respect normally accorded to the findings of a Court of Inquiry will not inhibit chemical engineers in looking beyond the report in their endeavours to improve the already good safety record of the chemical industry.
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in the disaster (the 20-inch hypothesis, argued by the plant designers (DSM) and the plant constructors; and favoured by the court's technical advisers), or had been triggered by an external explosion resulting from a previous failure of the 8-inch line.
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The terms of reference of the Court of Inquiry did not include any requirement to comment on the regulatory regime under which the plant had been built and operated, but it was clear that it was not satisfactory. Construction of the plant had required
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were relatively few people on site: of the 72 people on-site at the time, 28 were killed and 36 injured. Fires burned on-site for more than ten days. Off-site there were no fatalities, but 50 injuries were reported and about 2,000 properties damaged.
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QC, sat for 70 days in the period September 1974 – February 1975, and took evidence from over 170 witnesses. In parallel, an Advisory Committee on Major Hazards was set up to look at the longer-term issues associated with hazardous process plants.
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regime the presumption was that recognised good practice would inherently be 'reasonably practicable' and hence should be adopted, partly because key passages in reports of the Advisory Committee on Major Hazards were clearly supportive).
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All gasket materials in the area had been destroyed by the fire, so there was no direct evidence for or against a preceding gasket fault; the plant was known to have suffered leaks elsewhere because the wrong type of gasket had been
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Feedback within the management structure should ensure that top management understand the responsibilities of individuals and can ensure that their workload, capacity and competence allow them to effectively deal with those
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the errors were rather multiple instances of one underlying cause: a complete breakdown of plant safety procedures (exacerbated by a lack of relevant engineering expertise, but that lack was also a procedural shortcoming).
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When the bypass was installed, there was no works engineer in post and company senior personnel (all chemical engineers) were incapable of recognising the existence of a simple engineering problem, let alone solving it
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with nitrogen to 9 kg/cm; i.e. roughly operating pressure, but below the pressure at which the system relief valve would lift and below the 30% above design pressure called for by the relevant British Standard.
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in his cab. Fires started on-site which were still burning ten days later. Around 1,000 buildings within a 1-mile (1.6 km) radius of the site (in Flixborough itself and in the neighbouring villages of
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It was a failure of the cyclohexane plant that led to the disaster. A major leak of liquid from the reactor circuit caused the rapid formation of a large cloud of flammable hydrocarbon. When this met an
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expertise. Mechanical engineering issues with the modification were overlooked by the managers who approved it, and the severity of potential consequences due to its failure were not taken into account.
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commented presciently on the normal official response to such events, but hoped that the opportunity would be taken to introduce effective government regulation of hazardous process plants.
453:, so that planning authorities could be advised on safety issues before granting planning permission; similarly the emergency services should have information to draw up a disaster plan. 651:
HASAWA already required companies to have a safety policy, and a comprehensive plan to implement it. ACMH felt that for major hazard installations the plan should be formal and include
1596:. Unpublished: presented at American Institute of Chemical Engineers 2013 Spring Meeting 9th Global Congress on Process Safety San Antonio, Texas 28 April – 1 May 2013. Archived from 622:
Inquiry, its personnel (and that of its associated working groups) had significant representation of safety professionals, drawn largely from the nuclear industry and ICI (or ex-ICI)
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exceed operating pressure – the work was not on a large enough scale to resolve whether disruptive boiling by this mechanism would have created forces large enough to fail the bypass
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leak ignited at the leak site; it gave no protection against a major leak with delayed ignition, and the disaster had shown this could lead to multiple worker fatalities. The plant
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1984, the sculpture was stolen. It has never been recovered but the plinth it stood on, with a plaque listing all those who died that day, can still be found outside the church.
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When an important post is vacant, special care should be taken when decisions have to be taken which would normally be taken by or on the advice of the holder of the vacant post
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The plant was re-built but cyclohexanone was now produced by hydrogenation of phenol (Nypro proposed to produce the hydrogen from LPG; in the absence of timely advice from the
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Plant should be designed and run to minimise the rate at which critical management decisions arise (particularly those in which production and safety conflict).
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Sudee, C; Samuels, D E; O'Brien, T P (1976–1977). "The characteristics of the explosion of cyclohexane at the Nypro (UK) Flixborough plant on 1st June 1974".
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modelling of the release showing the upper and lower flammable limit envelopes can be found in for both the inquiry's favoured failure scenario and Venart's
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The report of the court of inquiry was critical of the installation of the bypass pipework on a number of counts: although plant and senior management were
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Lees' Loss Prevention in the Process Industries: Hazard Identification, Assessment and Control (3rd Edition) ed Sam Mannan, Butterworth-Heinemann, 2004
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The disaster involved (and may well have been caused by) a hasty equipment modification. Although virtually all of the plant management personnel had
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alighting on water. When the plant was closed, the statue was moved to the pond at the parish church in Flixborough. During the early hours of
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in northern Italy in July 1976, 'major hazard plants' became an EU-wide issue and the UK approach became subsumed in EU-wide initiatives (the
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Plant – where possible – should be designed so that failure does not lead to disaster on a timescale too short to permit corrective action.
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Why do we need the rules on the isolation and identification of equipment for maintenance? They were introduced about two years ago, but
2172: 113:(NCB)) had originally produced fertiliser from by-products of the coke ovens of a nearby steelworks. Since 1967, it had instead produced 1872:– the same thought but with the lower-risk animal a cat had appeared immediately post-Flixborough in Safety Newsletter No 67 (July 1974) 942:
pre-use by the traditional informal safeguard of a senior engineer walking the plant to have a look at what his subordinates were doing
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The disaster was caused by 'a well designed and constructed plant' undergoing a modification that destroyed its mechanical integrity.
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saw the plant as symptomatic of a general failure to consider safety early enough in process plant design, so that designs were
689:
The approach advocated by the ACMH was largely followed in subsequent UK legislation and regulatory action, but following the
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the conclusion of the official Inquiry, but this has been queried, given the pattern of deposition of soot from the explosion
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could be developed where the release was large, and ignition delayed: at Pernis in 1968 pipebridges had been blown down
2251: 730: 450: 205: 1768: 1591:"Effects of the Primary Explosion Site (PES) and Bulk Cloud in VCE Prediction: A Comparison with Historical Accident" 824:
of mild steel. There had been no similar air leaks (and consequently no similar water sprays) on the other reactors.
1386: 244:
In the DSM process, cyclohexane was heated to about 155 Β°C (311 Β°F) before passing into a series of six
821: 775:
i.e. the fatal modification did not introduce the bellows (a point not always appreciated by popular retellings)
427:
Modifications should be designed, constructed, tested and maintained to the same standards as the original plant
2216: 1556: 833:
and the pipework lifted about 6 mm at plant operating temperature because of thermal expansion of the reactors
1658: 2261: 2014:– reprinted, with slight modifications in Chemical Engineering Progress, Vol 2, No 11, November 1976, p. 48 1961: 1905: 857: 662:
Training for safety, measures to foster awareness of safety, and feedback of information on safety matters
258: 209: 154:
collapsed, killing all 18 occupants. Nine other site workers were killed, and a delivery driver died of a
57: 2086: 2001: 1859: 1680: 1380:"Safety: too important a matter to be left to the engineers? Inaugural lecture given on 22 February 1979" 603:
the council had not recognised the hazardous nature of the plant they had not called for advice. As the
155: 643:
responsibility for safety of the installation remaining however always and totally with the licensee.
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Clear safety roles (for e.g. the design and development team, production management, safety officers)
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The cyclohexane oxidation process is still operated in much the same plant design in the Far East.
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it subsequently transpired that Billingham had had similar rules, but they had fallen into disuse
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All engineers should learn at least the elements of branches of engineering other than their own
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threshold or of toxic materials above a certain 'chlorine equivalent' threshold should be '
245: 274:
Two months prior to the explosion, the number 5 reactor was discovered to be leaking. When
807: 725: 690: 532: 312: 78: 1799: 1742: 1273:"Catastrophic explosion of a cyclohexane cloud June 1, 1974 Flixborough United Kingdom" 129:, but in 1972 additional capacity was added, built to a DSM design in which hot liquid 65: 38: 1715: 2205: 1786:
Snee, T J (2001). "Interaction Between Water and Hot Cyclohexane in Closed Vessels".
713: 302: 249: 195: 122: 106: 1345: 952:
ensure that the interests of production are not allowed to override those of safety
801:
The explosion was estimated to be equivalent to 15–45 t TNT at the Inquiry. 16Β±2 t
705:
in 1996). A third and final report was issued when the ACMH was disbanded in 1983.
670:
The ACMH also called for tight discipline in the operation of major hazard plants:
528: 253: 171:
3 miles (4.8 km) away; the blast was heard over 35 miles (56 km) away in
151: 1303: 2111: 810:(Fig 3.4.1). Flixborough gives a higher estimated over-pressure than Buncefield. 557: 551:(ICI) operated many plants with large inventories of flammable chemicals at its 201:
who had been covering the Appleby-Frodingham Gala in Scunthorpe that afternoon.
130: 114: 42: 1998:
Imperial Chemical Industries Limited Petrochemicals Division Safety Newsletter
1856:
Imperial Chemical Industries Limited Petrochemicals Division Safety Newsletter
1807: 1750: 377: 168: 139: 2187: 2174: 1319: 561:
its documentation. The more onerous requirements were justified as follows:
198: 180: 34: 2155: 961:
this from para 61, where the examples given included 'operability studies'
143: 2030: 1702:
Strehlow, R A (1973). "Unconfined vapor-cloud explosionsβ€”An overview".
221: 172: 164: 118: 694: 217: 126: 373:
Detailed analysis suggested that the 8-inch pipe had failed due to "
2165:
Flixborough: 20 years on, Loss Prevention Bulletin issue 117, 1994
1825:(3rd ed.). Oxford: Butterworth-Heinemann. pp. 2/1–2/17 ( 1248:"Flixborough (Nypro UK) Explosion 1st June 1974: Accident Summary" 922:
An earlier organisation that became ICI's Petrochemicals Division.
96: 20: 2159: 499:
Post-enquiry forensic engineering – two-stage rupture of bypass
105:
The chemical works, owned by Nypro UK (a joint venture between
2146:
The Flixborough Disaster, Report of the Court of Inquiry, 1975
979:
The Flixborough Disaster, Report of the Court of Inquiry, 1975
680:
demonstrate their safety to a government body in such detail:
188: 1906:"14/8 Why Do We Need New Rules For Preparing For Maintenance" 736:
List of disasters in Great Britain and Ireland by death toll
1673:"60/6 Explosion of Clouds of Gas or Vapour in the Open Air" 908:
In addition, King takes the crack on reactor 5 to indicate
1278:. French Ministry of the Environment – DPPR / SEI / BARPI. 508:
Post-enquiry forensic engineering – the 'water hypothesis'
56:
qualifications, there was no on-site senior manager with
16:
Industrial accident in North Lincolnshire, England (1974)
856:, but a long-held belief of the inquiry's vice-chairman 517:
Dissatisfaction with other aspects of the Inquiry Report
1729:
Venart, J E S (2007). "Flixborough: A final footnote".
2277:
Industrial fires and explosions in the United Kingdom
77:(COMAH). In Europe, the Flixborough disaster and the 2024:
HC Deb 3 June 1974 vol 874 cc 867-77 (3 June 1974).
1731:
Journal of Loss Prevention in the Process Industries
2112:"Watch Days of Fury (1979) on the Internet Archive" 125:. This was originally produced by hydrogenation of 64:Flixborough led to a widespread public outcry over 1558:Advisory Committee on Major Hazards: Second Report 1354:. Oxford U.K.: Gulf Professional. pp. 103–9. 712:(1979), directed by Fred Warshofsky and hosted by 75:Control of Major Accident Hazards Regulations 1999 2151:Summary of the official inquiry into the accident 2069:Advisory Committee on Major Hazards FIRST REPORT 1886:By Accident – a life preventing them in industry 879:really an implicit invitation to others to do so 461:The inquiry summarised its findings as follows: 444:Matters to be referred to the Advisory Committee 262:then returned to the start of the reactor loop. 682: 672: 647:Ensuring safety of 'major hazard' installations 609: 593:Dissatisfaction with existing regulatory regime 563: 487: 463: 339: 308: 1994:"Must Plant Modifications Lead to Accidents?" 1966:ICI Petrochemicals Division Safety Newsletter 1910:ICI Petrochemicals Division Safety Newsletter 1823:Lees' Loss Prevention in the Process Industry 1677:ICI Petrochemicals Division Safety Newsletter 708:Footage of the incident appeared in the film 8: 1880: 1878: 1506:"Flixborough The Disaster and Its Aftermath" 1297: 1295: 1293: 1291: 1289: 1287: 1285: 2227:Buildings and structures demolished in 1981 2051:: CS1 maint: numeric names: authors list ( 1788:Process Safety and Environmental Protection 1402:(minor updating when posted on web in 2013) 1987: 1985: 1983: 1499: 1497: 1495: 1340: 1338: 1336: 753:Various authors have compared it with the 25:Memorial to those who died in the disaster 1622: 1620: 1618: 1448:"Flixborough Chemical Plant (Rebuilding)" 646: 607:commented within a week of the disaster: 187:were soon shown on television, filmed by 1550: 1548: 1302:Kinnersley, Patrick (27 February 1975). 117:, a chemical used in the manufacture of 2066:Health & Safety Commission (1976). 1936:"Your guide to the Fife Ethylene Plant" 1762: 1760: 1704:Symposium (International) on Combustion 1555:Health & Safety Commission (1979). 1474:"Liquefied Gas Storage (Canvey Island)" 1421:"Flixborough – Some Additional Lessons" 1373: 1371: 1236: 984: 746: 142:source (probably a furnace at a nearby 2282:June 1974 events in the United Kingdom 2044: 1659:"Sir Joseph Pope, Engineering Pioneer" 1589:Bauwens, C Regis; Dorofeev, Sergey B. 1304:"What really happened at Flixborough?" 1267: 1265: 1242: 1240: 167:) were damaged, as were nearly 800 in 146:production plant) there was a massive 2237:Chemical plants of the United Kingdom 1629:"Comment: Flixborough and the Future" 1437:(updated version of original article) 1414: 1412: 1410: 1408: 7: 2212:1974 disasters in the United Kingdom 1852:"Supplement to Safety Newsletter 75" 1351:Learning from Accidents, 3rd edition 121:. The caprolactam was produced from 588:Advisory Committee on Major Hazards 68:. Together with the passage of the 1679:(60). January 1974. Archived from 852:More a long-term solution than an 693:by a runaway chemical reaction at 81:in 1976 led to development of the 14: 2287:1970s fires in the United Kingdom 1539:Journal of Occupational Accidents 476:Controversy as to immediate cause 1454:. 959 cc179-90. 27 November 1978 617:Terms of Reference and personnel 485:inquiry had failed to identify: 300:Immediately after the accident, 70:UK Health and Safety at Work Act 2031:Parliamentary Debates (Hansard) 1767:King, Ralph (15 January 2000). 547:The Petrochemicals Division of 507: 270:Reactor 5 leaks and is bypassed 1992:Kletz, Trevor (January 1976). 626:Suggested regulatory framework 1: 1716:10.1016/S0082-0784(73)80107-9 1480:. 965 cc417-30. 27 March 1979 1250:. Health and Safety Executive 784:or of that part of it within 329:Circumstances of the disaster 2222:20th century in Lincolnshire 1962:"15/7 COMMENTS FROM READERS" 1850:Kletz, Trevor (April 1975). 549:Imperial Chemical Industries 101:Another view of the memorial 1661:. University of Nottingham. 1627:Tinker, Jon (6 June 1974). 731:Health and Safety Executive 701:in 1982, superseded by the 543:ICI Petrochemicals response 451:Health and Safety Executive 206:Health and Safety Executive 2315: 973:Report of Court of Inquiry 803:at 45 m above ground level 471:Response to Inquiry Report 2242:Disasters in Lincolnshire 2232:Chemical plant explosions 2026:"Flixborough (Explosion)" 1821:Mannan, Sam, ed. (2005). 1808:10.1205/09575820151095166 1769:"Flixborough 25 years on" 1751:10.1016/j.jlp.2007.05.009 822:stress corrosion cracking 633:notifiable installations 41:close to the village of 2267:History of Lincolnshire 1827:Appendix 2: Flixborough 1378:Booth, Richard (1979). 691:release of chlordioxins 757:in one aspect or other 687: 677: 614: 572: 492: 468: 384:The inquiry conclusion 360:The 20-inch hypothesis 344: 317: 210:Glanford Power Station 109:(DSM) and the British 102: 58:mechanical engineering 26: 2297:1970s in Lincolnshire 2257:Explosions in England 1425:The Chemical Engineer 1419:Cox, J I (May 1976). 393:Lessons to be learned 369:The 8-inch hypothesis 351:Cause of the disaster 100: 24: 2247:Engineering failures 2156:Flixborough memories 2000:(83). Archived from 1858:(75). Archived from 1099:Appendix II pp 46–49 788:. Visualisations of 193:Yorkshire Television 87:Directive 2012/18/EU 54:chemical engineering 31:Flixborough disaster 2184: /  1800:2001PSEP...79...81S 1773:Process Engineering 1743:2007JLPPI..20..621V 786:flammability limits 755:Tay Bridge disaster 703:Seveso II Directive 600:planning permission 577:'operability study' 402:General observation 335:chartered engineers 161:Burton upon Stather 111:National Coal Board 85:in 1982 (currently 2252:Explosions in 1974 1884:Kletz, T., (2000) 1126:para 226, pp 37–38 311:happened with the 148:fuel-air explosion 103: 47:North Lincolnshire 27: 1941:. Esso UK Limited 1888:PVF Publications 1710:(14): 1189–1200. 1683:on 4 October 2020 1361:978-0-7506-4883-7 1054:paras 54–59 pp7–8 1036:Appendix III p 50 910:mechanical design 107:Dutch State Mines 89:issued in 2012). 2304: 2199: 2198: 2196: 2195: 2194: 2189: 2185: 2182: 2181: 2180: 2177: 2116: 2115: 2108: 2102: 2101: 2099: 2097: 2091: 2085:. Archived from 2075:. London: HMSO. 2074: 2063: 2057: 2056: 2050: 2042: 2040: 2038: 2021: 2015: 2013: 2011: 2009: 1989: 1978: 1977: 1975: 1973: 1957: 1951: 1950: 1948: 1946: 1940: 1932: 1926: 1925: 1923: 1921: 1902: 1896: 1882: 1873: 1871: 1869: 1867: 1847: 1841: 1840: 1818: 1812: 1811: 1783: 1777: 1776: 1764: 1755: 1754: 1726: 1720: 1719: 1699: 1693: 1692: 1690: 1688: 1669: 1663: 1662: 1655: 1649: 1648: 1646: 1644: 1624: 1613: 1612: 1610: 1608: 1602: 1595: 1586: 1580: 1579: 1577: 1575: 1561:. London: HMSO. 1552: 1543: 1542: 1534: 1528: 1527: 1525: 1523: 1517: 1511:. Archived from 1510: 1501: 1490: 1489: 1487: 1485: 1470: 1464: 1463: 1461: 1459: 1444: 1438: 1436: 1434: 1432: 1416: 1403: 1401: 1399: 1397: 1391: 1385:. Archived from 1384: 1375: 1366: 1365: 1346:Kletz, Trevor A. 1342: 1331: 1330: 1328: 1326: 1314:(938): 520–522. 1299: 1280: 1279: 1277: 1269: 1260: 1259: 1257: 1255: 1244: 1232:Other references 1226: 1223: 1217: 1214: 1208: 1205: 1199: 1196: 1190: 1187: 1181: 1178: 1172: 1169: 1163: 1160: 1154: 1151: 1145: 1142: 1136: 1133: 1127: 1124: 1118: 1115: 1109: 1106: 1100: 1097: 1091: 1088: 1082: 1079: 1073: 1070: 1064: 1061: 1055: 1052: 1046: 1043: 1037: 1034: 1028: 1025: 1019: 1016: 1010: 1009:para 89 pp 13–14 1007: 1001: 998: 992: 989: 962: 959: 953: 949: 943: 939: 933: 929: 923: 920: 914: 906: 900: 896: 890: 886: 880: 876: 870: 866: 860: 854:immediate lesson 850: 844: 840: 834: 831: 825: 817: 811: 799: 793: 782: 776: 773: 767: 764: 758: 751: 699:Seveso Directive 419:Specific lessons 414:responsibilities 296:Court of Inquiry 183:. Images of the 83:Seveso Directive 2314: 2313: 2307: 2306: 2305: 2303: 2302: 2301: 2217:1974 in England 2202: 2201: 2192: 2190: 2186: 2183: 2178: 2175: 2173: 2171: 2170: 2142: 2135:, 9780750675550 2124: 2122:Further reading 2119: 2110: 2109: 2105: 2095: 2093: 2092:on 14 July 2014 2089: 2083: 2072: 2065: 2064: 2060: 2043: 2036: 2034: 2023: 2022: 2018: 2007: 2005: 2004:on 14 July 2014 1991: 1990: 1981: 1971: 1969: 1960:Kletz, Trevor. 1959: 1958: 1954: 1944: 1942: 1938: 1934: 1933: 1929: 1919: 1917: 1916:. 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The plant 136: 104: 63: 51: 30: 28: 18: 2191: / 858:Joseph Pope 558:human error 524:as designed 320:chaired by 131:cyclohexane 115:caprolactam 43:Flixborough 2292:1974 fires 2272:Humberside 2206:Categories 2133:0750675551 1639:(901): 590 1541:: 203–235. 1216:paras 58-9 1018:para 1 p 1 968:References 567:Billingham 457:Conclusion 378:cavitation 199:news crews 169:Scunthorpe 1320:0262-4079 240:The plant 196:filmstock 181:Saltfleet 35:explosion 2047:cite web 1348:(2001). 720:See also 656:control) 581:de facto 246:reactors 222:mallards 185:disaster 144:hydrogen 140:ignition 93:Overview 2176:53Β°37β€²N 2114:. 1979. 1972:10 July 1920:10 July 1866:27 June 1796:Bibcode 1739:Bibcode 1687:27 June 1607:26 June 1522:25 June 1484:10 July 1458:10 July 1431:26 June 1396:27 June 1254:25 June 1225:para 63 1207:para 35 1198:para 31 1189:para 29 1171:Plate 7 1081:pp18-19 889:venting 843:fitted. 276:lagging 259:baffled 252:, some 173:Grimsby 165:Amcotts 119:nylon 6 33:was an 2179:0Β°42β€²W 2131:  2096:9 July 2079:  2037:8 July 2008:1 July 1945:8 July 1892:  1833:  1643:8 July 1574:7 July 1565:  1358:  1325:7 July 1318:  695:Seveso 553:Wilton 218:bronze 127:phenol 2090:(PDF) 2073:(PDF) 1939:(PDF) 1601:(PDF) 1594:(PDF) 1516:(PDF) 1509:(PDF) 1390:(PDF) 1383:(PDF) 1276:(PDF) 742:Notes 375:creep 37:at a 2160:h2g2 2129:ISBN 2098:2014 2077:ISBN 2053:link 2039:2014 2010:2014 1974:2014 1968:(15) 1947:2014 1922:2014 1890:ISBN 1868:2014 1831:ISBN 1689:2014 1645:2014 1609:2014 1576:2014 1563:ISBN 1524:2014 1486:2014 1460:2014 1433:2014 1398:2014 1356:ISBN 1327:2014 1316:ISSN 1256:2014 1108:p 32 1027:p 14 191:and 179:and 177:Hull 163:and 29:The 2158:on 1829:). 1804:doi 1747:doi 1712:doi 1162:p15 1090:p18 1063:p 9 1045:p 4 1000:p 3 991:p 2 790:CFD 189:BBC 2208:: 2049:}} 2045:{{ 2028:. 1996:. 1982:^ 1964:. 1914:14 1912:. 1908:. 1877:^ 1854:. 1802:. 1792:79 1790:. 1771:. 1759:^ 1745:. 1735:20 1733:. 1708:14 1706:. 1675:. 1637:62 1635:. 1631:. 1617:^ 1547:^ 1494:^ 1476:. 1450:. 1423:. 1407:^ 1370:^ 1335:^ 1312:65 1310:. 1306:. 1284:^ 1264:^ 1239:^ 716:. 212:. 175:, 45:, 2100:. 2055:) 2041:. 2012:. 1976:. 1949:. 1924:. 1870:. 1839:. 1810:. 1806:: 1798:: 1775:. 1753:. 1749:: 1741:: 1718:. 1714:: 1691:. 1647:. 1611:. 1578:. 1526:. 1488:. 1462:. 1435:. 1400:. 1364:. 1329:. 1258:.

Index


explosion
chemical plant
Flixborough
North Lincolnshire
chemical engineering
mechanical engineering
process safety
UK Health and Safety at Work Act
Control of Major Accident Hazards Regulations 1999
Seveso disaster
Seveso Directive
Directive 2012/18/EU

Dutch State Mines
National Coal Board
caprolactam
nylon 6
cyclohexanone
phenol
cyclohexane
ignition
hydrogen
fuel-air explosion
control room
heart attack
Burton upon Stather
Amcotts
Scunthorpe
Grimsby

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