| 81 |
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Features - SAFETY - Benefit from the Three-Zone National Electrical Code - The NEC allows a three-Zone classification for hazardous (classified) locations in addition to the well-known two-Division approach. Use of this other scheme can reduce the cost of electrical equipment in these areas./
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LeBlanc, John A
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American Institute of Chemical Engineers
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2000
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| 82 |
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Features - SAFETY - Electrical Enclosures: Making an Informed Decision - In addition to the NEMA type and materials of construction, also take into account mounting, security, plus various other options./
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Dodds, Joe
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American Institute of Chemical Engineers
|
2001
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| 83 |
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Features - SAFETY - Expanded-Metal Networks: A Safety Net to Thwart Gas Explosions - Prevent gas explosions passively -- Insert a metal foil directly into the vessel to absorb the heat of reaction and put a limit on DT./
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Fauske, Hans K
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American Institute of Chemical Engineers
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2001
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| 84 |
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Features - SAFETY - Map Your Way to Strategic Investments in Process Safety - Many CPI firms are looking at safety costs as investments, rather than expenses, and are reaping wide-range benefits. Here's a roadmap of how best to accomplish this./
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Stavrianidis, Paris
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American Institute of Chemical Engineers
|
2001
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| 85 |
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Features - SAFETY - Reduce Thermal Risk in Industrial Synthesis - Knowing the safe operating conditions for a reaction allows us to select appropriate safety measures and thereby lower both the likelihood and the severity of a thermal runaway./
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Wedlich, Richard C
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American Institute of Chemical Engineers
|
2001
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| 86 |
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Features - SAFETY - Screen Reactive Chemical Hazards Early in Process Development - Using two tools can lead to selecting an inherently safer chemistry, identifying potential hazards and, thus, mitigating them, and saving money by providing safety layers for these hazards early on, avoiding rework./
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Mosley, David W
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American Institute of Chemical Engineers
|
2000
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| 87 |
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Features - SAFETY - Use a Comprehensive Database to Better Manage Process Safety - Find out if your database is large enough to be meaningful and whether it is being used to its fullest extent./
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Kelly, Brian D
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American Institute of Chemical Engineers
|
2001
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| 88 |
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Features - SAFETY - Use Importance Measures To Reduce Residual Risks - These measures help to prioritize time and money spent for mechanical integrity and risk reduction activities when resources are limited, as they always are. The method is risk-based/
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Bradley, G
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American Institute of Chemical Engineers
|
2000
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| 89 |
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Features - SAFETY - Use Maximum-Credible Accident Scenarios for Realistic and Reliable Risk Assessment - Posing various possible incidents -- Rather than just the worst-case one -- Illuminates those that are really important and those that are most likely to occur./
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Khan, Faisal I
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American Institute of Chemical Engineers
|
2001
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| 90 |
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Features - SALARY SURVEY HIGHLIGHTS - ChE Salaries Continue to Beat Inflation - The median salary among chemical engineers is (USD)77,200 and annual raises are averaging 4.4%/
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Feehan, Betty
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American Institute of Chemical Engineers
|
2000
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| 91 |
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Features - SIMULATING REALITY - Uncovering the Realities of Simulation, Part 2 - Simulation software is a commonly used design tool, thanks mainly to its availability on the desktop. However, one has to understand thermodynamic basics before accepting the desktop's final answer./
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Agarwal, Rajeev
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American Institute of Chemical Engineers
|
2001
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| 92 |
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Features - SOLIDS/FLUIDS HANDLING - Take Another Look at Steam Traps - Think twice before installing a steam trap. In the case of superheated lines, steam traps may prove to be a waste of time, effort, and money./
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Chari, S Raghava
|
American Institute of Chemical Engineers
|
2001
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| 93 |
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Features - SURVEY RESULTS - The Net Makes a Mark - Chemical engineers are finding that the Internet and intranets help them do their jobs more effectively. The impact has been modest so far, but promises to become much more profound./
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Rosenzweig, Mark D
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American Institute of Chemical Engineers
|
2000
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| 94 |
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Feedback Regularization and Control of Nonlinear Differential-Algebraic-Equation Systems
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Kumar, A
|
American Institute of Chemical Engineers]
|
1980
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| 95 |
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Fickian Diffusion in Binary Mixtures That Form Two Liquid Phases
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Pertler, M
|
American Institute of Chemical Engineers]
|
1980
|
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| 96 |
|
Film Profiles Behind Liquid Slugs in Gas-Liquid Pipe Flow
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Cook, M
|
American Institute of Chemical Engineers]
|
1980
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| 97 |
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Filter Medium Clogging During Cake Filtration (R&D Note)
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Lee, D. J
|
American Institute of Chemical Engineers]
|
1980
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| 98 |
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Finite-Element Scheme for Solution of the Dynamic Population Balance Equation/
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Rigopoulos, S
|
American Institute of Chemical Engineers]
|
2003
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| 99 |
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Finite-Element Simulation of Mixing: 1. Two-Dimensional Flow in PeriodicGeometry
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Avalosse, T
|
American Institute of Chemical Engineers]
|
1980
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|
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| 100 |
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Finite-Element Simulation of Mixing: 2. Three-Dimensional Flow Through aKenics Mixer
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Avalosse, T
|
American Institute of Chemical Engineers]
|
1980
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