Process safety is an interdisciplinary engineering domain focusing on the study, prevention, and management of large-scale fires , explosions and chemical accidents (such as toxic gas clouds) in process plants or other facilities dealing with hazardous materials , such as refineries and oil and gas ( onshore and offshore ) production installations. Thus, process safety is generally concerned with the prevention of, control of, mitigation of and recovery from unintentional hazardous materials releases that can have a serious effect to people (onsite and offsite), plant and/or the environment.
30-423: (Redirected from Perrys ) Perry's or Perrys may refer to: Arts, entertainment, and media [ edit ] Perry's Chemical Engineers' Handbook , a reference book The Perrys , a Southern Gospel quartet Brands and enterprises [ edit ] Perry's Ice Cream , an American company Perrys Motor Sales , British company Perry's Nut House ,
60-460: A limited number of workers (usually one or two per event), have consequences limited to well within the work site boundaries, and do not necessarily involve unintended contact with a hazardous material. Thus, for example, a gasoline storage tank loss of containment resulting in a fire is a process safety event, while a fall from height occurring while inspecting the tank is an OSH event. Although they may result in far higher impact to people, assets and
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120-533: Is analyzed and managed with tools typical of process safety. Process safety is usually associated with fixed onshore process and storage facilities, as well as fixed and floating offshore production and/or storage installations. However, process safety tools can and often are used (although to varying degrees) to analyze and manage bulk transportation of hazardous materials, such as by road tankers , rail tank cars , sea-going tankers , and onshore and offshore pipelines . Industrial domains that share similarities with
150-471: Is concerned. In the domain of offshore oil and gas extraction, production, and subsea pipelines, the discipline of process safety is sometimes understood to extend to major accidents not directly associated with hazardous materials processing, storage, or transport. In this context, the potential for accidents such as ship collisions against oil platforms, loss of FPSO hull stability, or crew transportation accidents (such as from helicopter or boating events),
180-542: Is primarily concerned with events which involve hazardous materials and are or have the potential to escalate to major accidents. A major accident is usually defined as an event causing multiple fatalities, extensive environmental impact, and/or significant financial consequences. The consequences of major accidents, while typically limited to the work site, can overcome the plant or installation boundaries, thus causing significant offsite impact. In contrast to this, occupational safety and health focuses on events that cause harm to
210-582: Is the CCPS scheme for risk-based process safety, which can be reconciled with most other established PSM schemes: While originally designed eminently for plants in their operations phase, elements of PSM can and should be implemented through the entire lifecycle of a project, wherever applicable. This includes design (from front-end loading to detailed design), procurement of equipment, commissioning , operations, material and organizational changes , and decommissioning. A common model used to represent and explain
240-542: The American Institute of Chemical Engineers (AIChE) gives the following: A discipline that focuses on the prevention of fires, explosions, and accidental chemical releases at chemical process facilities. Process safety scope is usually contrasted with occupational safety and health (OSH). While both domains deal with dangerous conditions and hazardous events occurring at work sites and/or while carrying out one's job duties, they differ at several levels. Process safety
270-447: The 1960s, failure mode and effects analysis (FMEA), checklists and what-if reviews . These were mostly qualitative techniques for identifying the hazards of a process. Quantitative analysis techniques, such as fault tree analysis (FTA, which had been in use by the nuclear industry ), quantified risk assessment (QRA, also referred to as Quantitative Risk Analysis), and layer-of-protection analysis (LOPA) also began to be used in
300-463: The HAZOP technique. In time, it absorbed a range of elements from other disciplines (such as chemistry and physics for mathematical modelling of releases, fires and explosions, instrumentation engineering , asset management , human factors and ergonomics , reliability engineering , etc.), thus becoming a relatively interdisciplinary engineering domain, although at its core it remains strongly connected with
330-648: The chemical process industries, and to which process safety concepts often apply, are nuclear power , fossil fuel power production , mining , steelmaking , foundries , etc. Some of these industries, notably nuclear power, follow an approach very similar to process safety's, which is usually referred to as system safety . In the early chemical industry, processes were relatively simple and societal expectations regarding safety were low by today’s standards. As chemical technology evolved and increased in complexity, and, simultaneously, societal expectations for safety in industrial activities increased, it became clear that there
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#1732881249284360-426: The environment, process safety accidents are significantly less frequent than OSH events, with the latter account for the majority of workplace fatalities. However, the impact of a single major process safety event on such aspects as regional environmental resources, company reputation, or the societal perception of the chemical and process industries, can be very considerable and is usually given prominent visibility in
390-454: The handbook's editor-in-chief, holds a B.S. in petroleum engineering from the University of Tulsa, and M.S. and PhD. Degrees in chemical engineering from the University of Oklahoma. He is Editor of the 6th, 7th and 8th Editions of Perry's. On the other hand, Marylee Southard, the associate editor, holds B.S., M.S. and PhD Degrees in chemical engineering from the University of Kansas. She is new to
420-520: The link to point directly to the intended article. Retrieved from " https://en.wikipedia.org/w/index.php?title=Perry%27s&oldid=1001694302 " Category : Disambiguation pages Hidden categories: Short description is different from Wikidata All article disambiguation pages All disambiguation pages Perry%27s Chemical Engineers%27 Handbook Perry's Chemical Engineers' Handbook (also known as Perry's Handbook , Perry's , or The Chemical Engineer's Bible )
450-585: The loss of control in the handling of hazardous materials at industrial scale. Strictly related to process safety, although for historical reasons usually not considered to belong to its domain, is the design of the following systems (note however that their selection is often the responsibility of a specialized process safety engineer): Companies whose business heavily relies on the extraction, processing, storage, and/or transport of hazardous materials, usually integrate elements of process safety management (PSM) within their health and safety management system. PSM
480-680: The media. The pivotal step in a process safety accident, around which a chain of accident causation and escalation can be built (including preventative and control/mitigative safety barriers), is generally the loss of containment of a hazardous material. It is this occurrence that frees the chemical energy available for the harmful consequences to materialize. Inadequate isolation, overflow, runaway or unplanned chemical reaction , defective equipment, human error , procedural violation, inadequate procedures, blockage, corrosion , degradation of material properties, excessive mechanical stress, fatigue , vibration , overpressure, and incorrect installation are
510-487: The prevention and control of events that have the potential to release hazardous materials or energy. Such events can cause toxic effects, fire or explosion and could ultimately result in serious injuries, property damage, lost production, and environmental impact. The same definition is given by the International Association of Oil & Gas Producers (IOGP). The Center for Chemical Process Safety (CCPS) of
540-443: The previous year. Lessons learnt from past events have been key in determining advances in process safety. Some of the major accidents that shaped it as an engineering discipline are: The following is a list of topics covered in process safety. There are some overlaps with equivalent domains from other disciplines, especially occupational safety and health (OSH), although the focus in process safety will always be specifically on
570-449: The process industries in the 1970s, 1980s and 1990s. Modeling techniques were developed for analyzing the consequences of spills and releases, explosions, and toxic exposure. The expression "process safety" began to be used increasingly to define this engineering field of study. It was generally understood to be a branch of chemical engineering , as it primarily relied on the understanding of industrial chemical processes, as exemplified in
600-453: The publication of Perry's, but has done significant work in inorganic chemicals production including process engineering, design and product development. Process safety The American Petroleum Institute defines process safety as follows: A disciplined framework for managing the integrity of hazardous operating systems and processes by applying good design principles, engineering, and operating and maintenance practices. It deals with
630-402: The released chemical is a toxic gas or a liquid whose vapors are toxic, then a toxic gas cloud occurs, which may harm or kill people locally at the release source or remotely, if its size and the atmospheric conditions do not immediately result in its dilution to below hazardous concentration thresholds. Fires, explosions, and toxic clouds are the main types of accidents with which process safety
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#1732881249284660-623: The term in its current sense is the Process Safety Guide by the Dow Chemical Company . By the mid to late 1970s, process safety was a recognized technical specialty. The American Institute of Chemical Engineers (AIChE) formed its Safety and Health Division in 1979. In 1985, AIChE established the Center for Chemical Process Safety (CCPS), partly in response to the Bhopal tragedy occurred
690-468: The understanding of industrial process chemical technology. "Process safety" gradually prevailed over alternative terms; for example, Frank P. Lees in his monumental work Loss Prevention in the Process Industries either used the titular expression or "safety and loss prevention", and so did Trevor Kletz , a central figure in the development of this discipline. One of the first publications to use
720-506: The usual proximate causes for such loss of containment. If the material is flammable and encounters a source of ignition, a fire will take place. Under particular conditions, such as local congestion (e.g., arising from structures and piping in the area where the release occurred or the flammable gas cloud migrated), the flame front of a flammable gas cloud can accelerate and transition to an explosion , which can cause overpressure damage to nearby equipment and structures and harm to people. If
750-403: The various different but connected systems related to achieving process safety is described by James T. Reason 's Swiss cheese model . In this model, barriers that prevent, detect, control and mitigate a major accident are depicted as slices, each having a number of holes. The holes represent imperfections in the barrier, which can be defined as specific performance standards. The better managed
780-434: Was a need for increasingly specialized expertise and knowledge in safety and loss prevention for the chemical industry. Organizations in the process industries originally had safety reviews for processes that relied on the experience and expertise of the people in the review. In the mid 20th century, more formal review techniques began to appear. These included the hazard and operability (HAZOP) review, developed by ICI in
810-452: Was edited by John H. Perry who was a PhD physical chemist and chemical engineer for E. I. du Pont de Nemours & Co. W. S. Calcott (ChE) of DuPont was his assistant editor. It was published in 1934. The second edition was published in 1941. The third edition was edited by John H. Perry and published in 1950 The fourth edition was edited by Robert H. Perry , Cecil H. Chilton, and Sidney D. Kirkpatrick and published in 1963. The fifth edition
840-462: Was edited by Robert H. Perry and published in 1973. The sixth edition ("50th Anniversary Edition") was published in 1984 and edited by Robert H. Perry and Donald W. Green. The 1997 seventh edition was edited by Robert H. Perry and Donald W. Green. The 2640 page 2007–2008 eighth edition was edited by Don W. Green and Robert H. Perry. and published October 2007. The 2018–2019 ninth edition was edited by Don W. Green and Marylee W. Southard Don Green,
870-990: Was first published in 1934 and the most current ninth edition was published in July 2018. It has been a source of chemical engineering knowledge for chemical engineers , and a wide variety of other engineers and scientists, through eight previous editions spanning more than 80 years. The subjects covered in the book include: physical properties of chemicals and other materials; mathematics ; thermodynamics ; heat transfer ; mass transfer ; fluid dynamics ; chemical reactors and chemical reaction kinetics ; transport and storage of fluid; heat transfer equipment; psychrometry and evaporative cooling ; distillation ; gas absorption ; liquid-liquid extraction ; adsorption and ion exchange ; gas–solid, liquid–solid and solid–solid operations; biochemical engineering ; waste management , materials of construction, process economics and cost estimation ; process safety and many others. The first edition
900-627: Was notably regulated by the United States' OSHA in 1992. The OSHA model for PSM is still widely used, not only in the US but also internationally. Other equivalent models and regulations have become available since, notably by the EPA , the Center for Chemical Process Safety (CCPS), and the UK's Energy Institute . PSM schemes are organized in 'elements'. Different schemes are based on different lists of elements. This
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