2012Unpublished venueRequires access

Hazard and Operability Studies (HAZOP) -- Best Practices Adopted by BAPCO (Bahrain Petroleum Company)

Ram K. Goyal, Suren Kugan

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Abstract

Abstract In 2007 BAPCO won the prestigious Robert W Campbell award for integrating safety into its primary business processes. The team who reviewed BAPCO processes on behalf of the Awarding agency made specific reference to the excellent quality of HAZOPs that BAPCO had conducted and reported. Such commendation for BAPCO HAZOPs did not come by chance. BAPCO has a very strong and rich tradition in this field; arguably the pioneers in this region. Bert Lawley, inventor of the HAZOP process, published his first paper on the topic in 1976; BAPCO conducted their first HAZOP meeting in as early as 1981! The traditional P&ID (Piping and Instrument Diagram) line-by-line guideword-based HAZOP remains a very powerful tool in the armory of modern designers and engineers in minimizing hazard and operability related concerns from process plants in continuous as well as batch operations. Nonetheless, BAPCO have strengthened its effectiveness through developing some best practices of our own and adopting some recommended by other well-known authorities such as the American Institute of Chemical Engineers’ Center for Chemical Process Safety (CCPS). One noteworthy best practice developed by BAPCO is the adoption of a comprehensive list of "Global Parameters." This is generally referred to as the last Node in HAZOPs and it addresses unit-wide or plant-wide concerns related to civil and structural integrity, instrumentation philosophy, fire water system, fireproofing, environmental concerns, reliability, emergency shutdown systems … the list goes on (currently there are 50 items under Global Parameters that BAPCO HAZOPs take into account). In addition to the Global Parameters mentioned above, this paper describes the following best practices that we apply to our HAZOPs: use of specific checklists which will captures all the items that are not covered under Global Parameters, review of emergency inventory isolation block valves, modeling of gas blow-by scenarios, and overpressure protection. HAZOP is a continually improving and evolving process in BAPCO. Our recent contacts with reputable engineering consultants have given us feedback regarding current best practices with EPC companies. We in BAPCO are committed to striving for excellence.

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Abstract In 2007 BAPCO won the prestigious Robert W Campbell award for integrating safety into its primary business processes. The team who reviewed BAPCO processes on behalf of the Awarding agency made specific reference to the excellent quality of HAZOPs that BAPCO had conducted and reported. Such commendation for BAPCO HAZOPs did not come by chance. BAPCO has a very strong and rich tradition in this field; arguably the pioneers in this region. Bert Lawley, inventor of the HAZOP process, published his first paper on the topic in 1976; BAPCO conducted their first HAZOP meeting in as early as 1981! The traditional P&ID (Piping and Instrument Diagram) line-by-line guideword-based HAZOP remains a very powerful tool in the armory of modern designers and engineers in minimizing hazard and operability related concerns from process plants in continuous as well as batch operations. Nonetheless, BAPCO have strengthened its effectiveness through developing some best practices of our own and adopting some recommended by other well-known authorities such as the American Institute of Chemical Engineers’ Center for Chemical Process Safety (CCPS). One noteworthy best practice developed by BAPCO is the adoption of a comprehensive list of "Global Parameters." This is generally referred to as the last Node in HAZOPs and it addresses unit-wide or plant-wide concerns related to civil and structural integrity, instrumentation philosophy, fire water system, fireproofing, environmental concerns, reliability, emergency shutdown systems … the list goes on (currently there are 50 items under Global Parameters that BAPCO HAZOPs take into account). In addition to the Global Parameters mentioned above, this paper describes the following best practices that we apply to our HAZOPs: use of specific checklists which will captures all the items that are not covered under Global Parameters, review of emergency inventory isolation block valves, modeling of gas blow-by scenarios, and overpressure protection. HAZOP is a continually improving and evolving process in BAPCO. Our recent contacts with reputable engineering consultants have given us feedback regarding current best practices with EPC companies. We in BAPCO are committed to striving for excellence.

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Available abstract

Abstract In 2007 BAPCO won the prestigious Robert W Campbell award for integrating safety into its primary business processes. The team who reviewed BAPCO processes on behalf of the Awarding agency made specific reference to the excellent quality of HAZOPs that BAPCO had conducted and reported. Such commendation for BAPCO HAZOPs did not come by chance. BAPCO has a very strong and rich tradition in this field; arguably the pioneers in this region. Bert Lawley, inventor of the HAZOP process, published his first paper on the topic in 1976; BAPCO conducted their first HAZOP meeting in as early as 1981! The traditional P&ID (Piping and Instrument Diagram) line-by-line guideword-based HAZOP remains a very powerful tool in the armory of modern designers and engineers in minimizing hazard and operability related concerns from process plants in continuous as well as batch operations. Nonetheless, BAPCO have strengthened its effectiveness through developing some best practices of our own and adopting some recommended by other well-known authorities such as the American Institute of Chemical Engineers’ Center for Chemical Process Safety (CCPS). One noteworthy best practice developed by BAPCO is the adoption of a comprehensive list of "Global Parameters." This is generally referred to as the last Node in HAZOPs and it addresses unit-wide or plant-wide concerns related to civil and structural integrity, instrumentation philosophy, fire water system, fireproofing, environmental concerns, reliability, emergency shutdown systems … the list goes on (currently there are 50 items under Global Parameters that BAPCO HAZOPs take into account). In addition to the Global Parameters mentioned above, this paper describes the following best practices that we apply to our HAZOPs: use of specific checklists which will captures all the items that are not covered under Global Parameters, review of emergency inventory isolation block valves, modeling of gas blow-by scenarios, and overpressure protection. HAZOP is a continually improving and evolving process in BAPCO. Our recent contacts with reputable engineering consultants have given us feedback regarding current best practices with EPC companies. We in BAPCO are committed to striving for excellence.

Key concepts: Hazard and operability study, Process safety, Process safety management, Operability, Engineering, Process (computing), Hazard, Vetting

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