02415oam 2200469 450 991083058380332120230629235608.01-119-52921-21-5231-3825-41-119-52918-21-119-52917-4(CKB)4100000011689703(MiAaPQ)EBC6437586(EXLCZ)99410000001168970320210608d2021 uy 0engurcnu||||||||txtrdacontentcrdamediacrrdacarrierGuidelines for process safety during the transient operating mode managing risks during process start-ups and shut-downs /Center for Chemical Process Safety of the American Institute of Chemical EngineersHoboken, New Jersey :Wiley,2021.1 online resource (289 pages)1-119-52915-8 Includes bibliographical references and index."Process industries bring vast benefits to our daily lives, but we do not live in a risk-free environment and mistakes are made. The timing for the highest risk period for most facilities occurs during start-up and shutdowns - also known as "transient" operations. Since transient operations, in general, for continuous chemical processes are performed less frequently, they have increased operational risks. This increased risk is due, in part, to an increased likelihood for procedural errors and the special hazards associated with the start-up or shutdown, especially since the process is not running under normal, steady state conditions. In addition, it may not be possible to address the many temporary and potentially hazardous conditions which could occur during the start-up or shutdown of these complex processes"--Provided by publisher.Chemical engineeringSafety measuresChemical process controlChemical plantsSafety measuresPlant shutdownsChemical engineeringSafety measures.Chemical process control.Chemical plantsSafety measures.Plant shutdowns.660.2804MiAaPQMiAaPQUtOrBLWBOOK9910830583803321Guidelines for process safety during the transient operating mode4086120UNINA