LEADER 02415oam 2200469 450 001 9910830583803321 005 20230629235608.0 010 $a1-119-52921-2 010 $a1-5231-3825-4 010 $a1-119-52918-2 010 $a1-119-52917-4 035 $a(CKB)4100000011689703 035 $a(MiAaPQ)EBC6437586 035 $a(EXLCZ)994100000011689703 100 $a20210608d2021 uy 0 101 0 $aeng 135 $aurcnu|||||||| 181 $ctxt$2rdacontent 182 $cc$2rdamedia 183 $acr$2rdacarrier 200 10$aGuidelines for process safety during the transient operating mode $emanaging risks during process start-ups and shut-downs /$fCenter for Chemical Process Safety of the American Institute of Chemical Engineers 210 1$aHoboken, New Jersey :$cWiley,$d2021. 215 $a1 online resource (289 pages) 311 $a1-119-52915-8 320 $aIncludes bibliographical references and index. 330 $a"Process industries bring vast benefits to our daily lives, but we do not live in a risk-free environment and mistakes are made. The timing for the highest risk period for most facilities occurs during start-up and shutdowns - also known as "transient" operations. Since transient operations, in general, for continuous chemical processes are performed less frequently, they have increased operational risks. This increased risk is due, in part, to an increased likelihood for procedural errors and the special hazards associated with the start-up or shutdown, especially since the process is not running under normal, steady state conditions. In addition, it may not be possible to address the many temporary and potentially hazardous conditions which could occur during the start-up or shutdown of these complex processes"--$cProvided by publisher. 606 $aChemical engineering$xSafety measures 606 $aChemical process control 606 $aChemical plants$xSafety measures 606 $aPlant shutdowns 615 0$aChemical engineering$xSafety measures. 615 0$aChemical process control. 615 0$aChemical plants$xSafety measures. 615 0$aPlant shutdowns. 676 $a660.2804 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bUtOrBLW 906 $aBOOK 912 $a9910830583803321 996 $aGuidelines for process safety during the transient operating mode$94086120 997 $aUNINA