Table Of Content

Index to Volume 18 Authors Abbasi, S.A. Keeports, G Amyotte, P.R. Khan, Faisal I. .... Atherton, John G. Khan, Faisall. .... Klein, | vn Rite RECORDS 25 od. doo es ce es Koch, Wolfgang Bodman, Glenn T. Brown, Anthony Bie. ooo .s ws edie eee Leverenz, Jr., Fred L. ESRGRE eA oe i het ok SG Rw BR Buchier, P.M. . . M Maranghides, Alexander Marszal, Edward M. Chadwell, G. Bradley Mashuga, Chad V. Chatrathi, K. McConnell, R.A. Chervin, Sima Modigell, M. Cohen, Wayne Crowl, Daniel A. Dastidar, A.G. Davis, Lloyd Dieken, Dominique Ogle, Russell A. ...... Dowel AGM s2.00 9.0% eee Osborn, Lucas . . Evon, Skip E Paquet Jr., D.A. Pequeno, Catela Perlmutter, Barry A. .... Fisher, Harold G. Pratt, Thomas H. Foisselon, Pierre Prugh, Richard W. ...... Fuller, Brad A. Rose, Susan E Going, J. Rofskothen, Hanns-Jiirgen . Gruhn, Paul Scheier, Ephraim Hansen, Olav Roald Scheuermann, Klaus P. Schmidt, Jochen Hansen, Don Hendershot, D.C. Severin, Manfred Hobbs, Douglas H. Shah, Jatin N. Holman, Michael Sheinson, Ronald S. Sutherland, Lester E. Jamerson, Scott ¢ Tamanini, Francesco Process Safety Progress (Vol.18, No.4) Winter 1999 247 Tang, MJ. Williams, Gerald P. Torres, Anthony J. Woodward, John I Worthington, David R.E. Valiulis, John V. van Wingerden, Kees Zalosh, Robert G. A Wilhelm, S. Mark Application of ISA $84.01 to SIS in the Willey, RonaldJ . Chemical and Petrochemical Industries. . .. .22 Titles Application of Pressure Nutsche Filtration Flammability Zone Prediction Using Calculated and Drying Technology for Toxic Chemicals Adiabatic Flame Temperatures Avoiding Exposure to Mercury During Flammable Liquid Storerooms: Fire Protection Inspection and Maintenance Operations in without Halon 1301 Oil and Gas Processing B Hazard Identification Analysis of a Batch Purge Caused by Confusing Control System Hydrogen Plant Displays Inspection, Testing and Maintenance of Fire Can Solvent Choices Enhance Both Process Safety Protection Systems at Industrial Plants and Efficiency? Comparison of EPA Guidelines Tables With a L Commercial Model Layer of Protection Analysis and Inherently Comparison of Safety Integrity Level Selection Safer Processes Methods and Utilization of Risk Based Approached Constraints on Inherently Safer Design New Set of Blast Curves From and Other Innovations Vapor Cloud Explosion, A Contribution of Human Factors to Incidents in the Petroleum Refining Industry O D Oxychem Y2K Contingency Planning Developing Screening Risk Evaluation Criteria for Facility Siting Vapor Cloud P Explosion Hazards Predicting Blast Overpressures Caused by Vapor Cloud Explosions in the Vicinity of Control Rooms Pressure Relief Valve Piping Failures and Fire: Effects of Explosive Blast on Structures Ammonia Synthesis Loop and Personnel .... R Risk Analysis: An Investment in Engineering Polymerization Processes Risk Management Plans for Existing Experiences with Heavy Fuel-Oil Firing Control Rooms in a Steam Reformer Experiments on the Propagation of Vented Dust Explosions to Connected Equipment SACHE Case Histories and Training Modules ... . Explosion Hazard Analysis for an Enclosure SACHE Essay - Process Safety in Education Partially Filled With a Flammable Gas Safety Instrumented System Design: Lessons Learned r Safety Performance in Ammonia Flammability Limits of Dusts: Minimum Plants: Survey VI Inerting Concentrations 248 Winter 1999 Process Safety Progress (Vol.18, No.4) U W Ise of Aerosol Fire Extinguishing Generators at Rotogravure Fed Presses When You Cut Down a Tree, Keep an iser Friendly System for Eye on the Forest Probabilistic Fault Tree Analysis Why DIERS Technology Should be Used in Risk Ising Constant Slip Ratios to Model Assessment: Call for a 1999 Worldwide Non-Flashing (Frozen) Two-Phase Flow Benchmarking Survey on Various Risk Through Nozzles . . Reduction Methods Used Ising Quantitative Risk Assessment World's Worst Industrial Accident of the 1990's to Develop a Cost Effective Spill - What Happened and What Have Been: Prevention Program A Quantitative Study . Subjects A Fuel-oil-firing in a steam reformer Acrylic polymerization processes Aerosol fire extinguishing generators, use of G Ammonia Gas plants, safety performance in hazard analysis for flammable synthesis loop, valve piping failures and fire . . processing Batch purge Halon 1301, fire protection without . . Blast(s) Hazard(s) curves from vapor cloud explosion classification system for liquids effect of identification analysis vapor cloud explosion G I Calculated adiabatic flame temperatures Industrial accident, a quantitative study Chemical operations, electrostatic ignitions in Inherently Safer Control system, confusing displays design, constraints on processes D DIERS technology in risk assessment L Dust(s) Liquids, fire hazard classification system for explosions, vented flammability limits of M Maintenance of fire protection systems Mercury, avoiding exposure to Electrostatic ignitions \ Emergency relief Explosive(s) Nozzles, non-flashing (frozen) blast, effects of Oil and gas processing Filtration and drying technology Flame temperatures, calculated adiabatic Petroleum refining industry Fire Plants extinguishing generators ammonia, safety performance in hazard classification system fire protection systems at pressure relief valve piping failures and Pressure refief valve piping failures protection Production analysis, layer of Flammable PROFAT (probabilistic fault tree analysis) gas, explosion hazard analysis liquid storerooms Q Flammability zone prediction Quantitative risk assessment Process Safety Progress (Vol.18, No.4) Winter 1999 249 R SIS (safety instrumented systems) Risk Solvent choices to enhance process safety ARMM 555.« aio oeltea.ps8s ae Di Spill prevention program assessment a: Steam reformer, fuel-oil-firing in based approaches evaluation criteria for facility siting 5 T management plans Toxic chemicals, filtration/drying technology for . reduction methods Two-phase flow through non-flashing nozzles Rotogravure fed presses : Training methods (SACHE) SACHE case histories Valve, pressure relief Safety Vapor cloud explosion and efficiency Vented dust explosions instrumented systems design integrity level selection methods performance in ammonia plants Y2K contingency planning |S tatement of Ownership, Management, and Circulation (required by 39 U.S.C. 3685) of September 1, 1999, for Process Safety Progress Publication No. 689-410, issued quarterly for an annual subscription price of $225 from 3 Park Avenue, New York, NY 10016-5901, which is the location of its publication and business offices. The name and address of the Publisher, Editor, and Managing Editor are: Publisher, Stephen R. Smith, 3 Park Avenue, New York, N.Y. 10016-5901; Editor, T.A. Ventrone, 3 Park Avenue, New York, N.Y. 10016-5901; Managing Editor, Maura Mullen, 3 Park Avenue, New York, N.Y. 10016- 5901. The owner is: American Institute of Chemical Engineers, 3 Park Avenue, New York, N.Y. 10016-5901. The known bondholders, mortgagees, and other security holders owning or holding one percent or more of the total amount of bonds, mortgages, or other securities are: None. The purpose, function, and nonprofit status of this organization, and the exempt status for federal income tax purpose have not changed during the preceding 12 months. The following figures describe the nature and extent of the circulation of the Fall 1999 issue. In each category the first number (in italics) is the average number of copies of each issue during the preceding 12 months. The number next to it, within parentheses (), is the actual number of copies of the single issue published nearest to the filing date. Total number of copies printed (net press run): (2750) 2500. 1. Paid/requested outside-county mail subscriptions stated on form 3541: (2066) 1987. 2. Paid in-county subscriptions: None. 3. Sales through dealers and carriers, street vendors, counter sales, and other non-USPS paid distribution: None. 4. Other classes mailed through the USPS: None. Total paid and/or requested circulation: (2066) 1987. Free distribution outside the mail: None. Total free distribution: (15) 15. Total Distribution: (2081) 2002. Copies not distributed: (669) 498. Total: (2750) 2500. Percent paid and/or requested circulation: (99.28%) 99.25%. 1 certify that the statements made by me are correct and complete. Stephen R. Smith, Senior Director, Publications. Winter 1999 Process Safety Progress (Vol.18, No.4)