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Chemical
plant safety, environmental protection, sustainability, government regulations
This color indicates a
link available via Clarkson University (off-campus
access)
Sustainability, energy
efficiency, green chemistry
U.S. government agencies, regulations and laws
As in other fields, use of
the acronyms in parentheses below tends to identify you as someone who knows
about these important matters
·
Integrated Risk Information Service (IRIS)
·
Toxic Substances Control Act
(TSCA)
·
Emergency Planning and
Public Right to Know Act (EPCRA)
·
Superfund Amendments and
Reauthorization Act (SARA)
·
Resource Conservation and
Recovery Act (RCRA)
·
Clean Air Act (CAA)
·
National Ambient
Air Quality Standards (NAAQS)
·
National Emission Standards
for Hazardous Air Pollutants (NESHAP)
·
Clean Water Act (CWA)
·
Occupational
Safety and Health Act (same acronym)
·
Process
Safety Management of Highly Hazardous Chemicals (PSM)
·
OSHA
and EPA Process Safety Management Requirements: A Practical Guide for
Compliance
·
The Whistleblower Protection
Program
·
Chemical Facility
Anti-Terrorism Standards (CFATS)
·
Current
Good Manufacturing Practices (cGMP) Rules for manufacturing
pharmaceuticals, from the Food and Drug Administration (FDA)
Non-U.S.
regulations
With global commerce,
companies often must also follow laws and regulations established by non-U.S.
governments and organizations. For
example:
Non-governmental
safety codes and standards
Often recognized in
governmental regulations
Pollution control and environmental protection
Design for Safety
Operate for Safety
·
52 on-line publications (search “Center for Chemical Process Safety”)
·
Process Safety Progress On-line journal with excellent research
papers.
HAZOP (HAZard
and OPerability) and Risk Assessment studies
Software, training, consulting and facilitation are available
commercially and can be found on-line.
Simulators such as HYSYS,
particularly in the dynamics mode (varying with time), can be quite useful in
determining the influence of deviations from specified flow rates,
compositions, temperatures, pressures, etc.
They can also be used to test the effectiveness of control systems to
automatically compensate for these deviations without relying on the
intervention of a human operator.
Fires,
explosions, chemical reaction hazards, toxicity
·
Avoid:
·
A mixture containing a combustible material and oxygen between the
upper and lower flammability limits (see below), taking into account pressure,
temperature, and oxygen concentration.
·
A
combustible stream from a condenser at a temperature above its flash point .
·
Formation
of a pyrophoric reaction product, such as iron maleate from the reaction of
maleic acid with iron.
·
Perry's pp 26-51 to
26-72.
·
Fire
Protection Guide to Hazardous Materials Complete and up-to-date source of
the fire hazard properties of flammable liquids, gases and volatile solids in
air at 1 atm. National Fire Protection
Association (NFPA), 2001 (ISBN 0877654735; $125)
·
Handbook
of Chemistry and Physics (CRC): page 16-13 and following
in the 87th edition.
·
“Flammability Characteristics of Combustible Gases and Vapors,” by
Michael G. Zabetakis, Bulletin 627, Bureau of Mines, US
Department of the Interior (1965).
Excellent (but old) book on flammability of combustible gases and vapor:
Extensive collection of data on flammability limits, including plots of
influence of oxygen-nitrogen ratio, pressure, temperature. Here is Appendix A, which contains limits of
flammability and autoignition temperature for many compounds in air at 1
atm.
·
“Limits of Flammability of Gases and Vapors,” by H.F. Coward and
G.W. Jones, Bulletin 503, Bureau of Mines (1952). A report preceding the above
that also tabulates flammability limits
in oxygen and nitrogen oxides, as well as the oxygen percentages below
which no mixture is flammable using nitrogen or carbon dioxide as
diluents.
·
Extended Le Chatelier's formula for mixtures (includes influence of
dilution with an inert gas such as carbon dioxide).
·
Review of methods for mixtures
·
Prediction of the flash point of single components and
mixtures
·
Appendices in Understanding Explosions
·
T-dependence of LFL Tables of LFL for
this paper
·
"Fire Hazards in Industry," Norman Thomson,
Oxford: Butterworth-Heinemann, ISBN 141750563X (2002) ebook
·
Selection of flame
arrestors
·
Handling Flammable
Liquids (control of electrostatic hazards)
·
Improved
safety of LNG terminal by dynamics modeling with HYSYS
·
Explosion Hazards in the Process Industries
·
Avoiding Static Ignition Hazards in Chemical Operations (from the AIChE Center for Chemical Process Safety)
·
Power Point
presentation on methods to avoid explosions
·
Deflagration and Detonation Arresters
·
Emergency Relief System Design Using DIERS Technology -
The Design Institute for Emergency Relief Systems (DIERS) Project Manual
·
High Integrity Pressure
Protection Systems
·
Using Instrumented
Systems for Overpressure Protection
·
Hazard of relief
valve and rupture disk in series ; Relief valves ; Relief valves for
supercritical fluids
·
Dust Explosions in the Process Industries
·
Avoiding explosions in dust collectors
·
Minimum Inerting Concentration for Dusts
·
Hazard
Analysis for Dust-Handling Operations
·
On-line chemical
reaction predictor for mixtures of more than 6,000 common
hazardous chemicals.
·
Essential Practices for Managing Chemical Reactivity
Hazards
·
How
to handle reactive materials
·
Bretherick's Handbook of Reactive Chemical Hazards Ref 660.2804 B844h4
·
Screening for
Chemical Reactivity Hazards
·
Evaluation
of reactive chemical hazards
·
Patty's Industrial Hygiene and Toxicology
·
Sax's Dangerous Properties of Industrial Materials Ref 604.7
S272d9
·
Sittig's Handbook of Toxic and Hazardous Chemicals and Carcinogens
·
Toxic properties of chemicals
·
Toxicity of chemicals in air
·
DoT Office of Hazardous
Materials Safety
·
Registry of Toxic Effects of
Chemical Substances
·
NIOSH Databases and
Other Resources
·
DDT and malaria. A
New Home for DDT. The
Case for DDT
Disclaimer: The
material on these pages is intended for instructional purposes by Clarkson
University students only. Neither
Clarkson University nor Professor Wilcox are responsible for problems caused by
using this information.
Last updated
September 5, 2012. Comments and
corrections should be sent to Professor William R. Wilcox
Wilcox
home × ChE design home × Professional × General × Properties × Equipment × Separation × HYSYS &
UniSim × Costs × Safety × Case studies × Excel
× MATLAB × Data Analysis