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Guidelines for design solutions for process equipment failures.
While there is no "perfect" solution or absolute zero risk, engineering design can significantly reduce risk potential in the CPI. In Guidelines for Design Solutions to Process Equipment Failures, industry experts offer their broad experience in identifying numerous solutions to the more c...
| Clasificación: | Libro Electrónico |
|---|---|
| Autor Corporativo: | |
| Formato: | Electrónico eBook |
| Idioma: | Inglés |
| Publicado: |
New York, N.Y. :
Center for Chemical Process Safety of the American Institute of Chemical Engineers,
[1998]
|
| Temas: | |
| Acceso en línea: | Texto completo |
MARC
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| 245 | 0 | 0 | |a Guidelines for design solutions for process equipment failures. |
| 246 | 3 | 0 | |a Design solutions for process equipment failures |
| 264 | 1 | |a New York, N.Y. : |b Center for Chemical Process Safety of the American Institute of Chemical Engineers, |c [1998] | |
| 264 | 4 | |c ©1998 | |
| 300 | |a 1 online resource (xviii, 252 pages) : |b illustrations | ||
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| 504 | |a Includes bibliographical references and index. | ||
| 588 | 0 | |a Print version record. | |
| 505 | 0 | |a Guidelines for Design Solutions for Process Equipment Failures; CONTENTS; Foreword; Preface; Acknowledgments; 1 Introduction; 2 Technique for Selecting the Design Bases for Process Safety Systems; 3 VESSELS; 4 REACTORS; 5 Mass Transfer Equipment; 6 HEAT TRANSFER EQUIPMENT; 7 DRYERS; 8 FLUID TRANSFER EQUIPMENT; 9 Solid-Fluid Separators; 10 Solids Handling and Processing Equipment; 11 FIRED EQUIPMENT; 12 Piping and Piping Components; APPENDIX A Example Problem: Batch Chemical Reactor; B Example Problem: Distillation System; Glossary; Acronyms and Abbreviations; Index. | |
| 520 | |a While there is no "perfect" solution or absolute zero risk, engineering design can significantly reduce risk potential in the CPI. In Guidelines for Design Solutions to Process Equipment Failures, industry experts offer their broad experience in identifying numerous solutions to the more common process equipment failures including inherent safer/passive, active, and procedural solutions, in decreasing order of robustness and reliability. The book challenges the engineer to identify opportunities for inherent and passive safety features early, and use a risk-based approach to process | ||
| 506 | |3 Use copy |f Restrictions unspecified |2 star |5 MiAaHDL | ||
| 533 | |a Electronic reproduction. |b [Place of publication not identified] : |c HathiTrust Digital Library, |d 2010. |5 MiAaHDL | ||
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| 710 | 2 | |a American Institute of Chemical Engineers. |b Center for Chemical Process Safety. | |
| 776 | 0 | 8 | |i Print version: |t Guidelines for design solutions for process equipment failures. |d New York, N.Y. : Center for Chemical Process Safety of the American Institute of Chemical Engineers, ©1998 |z 081690684X |w (DLC) 97020538 |w (OCoLC)36900950 |
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