Information chemical engineering

Allen-Bradley—www.ab.com Foxboro—ww W .foxboro.com Chemical Engineering Information Chemical Engineering—... 

Kirschner, E. Running on information. Chemical Engineering News 75, 15-19 (1997)... 

Center for Chemical Process Safety. In 1985, the American Institute of Chemical Engineers estabHshed the Center for Chemical Process Safety (CCPS) (New York). The objective of the CCPS was to help prevent catastrophic chemical accidents by compiling information on the latest scientific and engineering practices, safety programs, and adininistrative procedures of the larger members of the chemical industry, so that they can be shared with other (and particularly the smaller) members of the chemical and petrochemical industries. 

For certain types of stochastic or random-variable problems, the sequence of events may be of particular importance. Statistical information about expected values or moments obtained from plant experimental data alone may not be sufficient to describe the process completely. In these cases, computet simulations with known statistical iaputs may be the only satisfactory way of providing the necessary information. These problems ate more likely to arise with discrete manufactuting systems or solids-handling systems rather than the continuous fluid-flow systems usually encountered ia chemical engineering studies. However, there ate numerous situations for such stochastic events or data ia process iadustries (7—10). 

Rutan, The SPACE Predictor for Infinite Dilution Activity Coefficients, unpubhshed, presented at AlChE 1992 Annual Meeting, Nov. 3, Miami Beach, Fla. For information, write to Chades. A. Eckert, School of Chemical Engineering, Georgia Institute of Technology, Adanta, Ga. 30332-0100. 

Hsue-peng Loh, Ph.D., P.E., Federal Energy Technology Center (Morgantown), U.S. Department of Energy Member, American Institute of Chemical Engineers, American Society of Information Sciences (Section 27, Energy Resources, Conversion, and Utihzation)... 

Table 9-42 presents information on some cost indices for the United States. Engineering News-Record updates its construction-cost index in March, June, September, and December. The Oil and Gas Journal gives the Nelson-Farrar refinery indices in the first issue of each quarter. The Chemical Engineering plant-cost index and Marshall and Swift equipment-cost index are given in each issue of the pubhcation Chemical Engineering. Derivation of the base values is referred to in the respective publications. 

Vessel Codes Other Than ASME Different design and construction rules are used in other countries. Chemical engineers concerned with pressure vessels outside the United States must become familiar with local pressure-vessel laws and regulations. Boilers and Pressure Vessels, an international survey of design and approval requirements published by the British Standards Institution, May-lands Avenue, Hemel Hempstead, Hertfordshire, England, in 1975, gives pertinent information for 76 political jurisdic tions. 

Engineering, McGraw-Hill, New York, 1955. Standiford, Chem. Eng., 70, 158-176 (Dec. 9, 1963). Testing Frocedure for Evaporators, American Institute of Chemical Engineers, 1979. Upgrading Evaporators to Reduce Energy Consumption, ERDA Technical Information Center, Oak Ridge, Tenn., 1977. 

When the kinetics are unknown, still-useful information can be obtained by finding equilibrium compositions at fixed temperature or adiabatically, or at some specified approach to the adiabatic temperature, say within 25°C (45°F) of it. Such calculations require only an input of the components of the feed and produc ts and their thermodynamic properties, not their stoichiometric relations, and are based on Gibbs energy minimization. Computer programs appear, for instance, in Smith and Missen Chemical Reaction Equilibrium Analysis Theory and Algorithms, Wiley, 1982), but the problem often is laborious enough to warrant use of one of the several available commercial services and their data banks. Several simpler cases with specified stoichiometries are solved by Walas Phase Equilibiia in Chemical Engineering, Butterworths, 1985). 

It is sincerely hoped that the information presented in this document will lead to an even more impressive record for the entire industry however, the American Institute of Chemical Engineers, its consultants, CCPS Subcommittee members, their employers, their employers officers and directors, and Arthur D. Little, Inc., disclaim making or giving any warranties or representations, express or implied, including with respect to fitness, intended purpose, use or merchantability and/or correctness or accuracy of the content of the information presented in this document. As between (1) American Institute of Chemical Engineers, its consultants, CCPS Subcommittee members, their employers, their employers officers and directors, and Arthur D. Little, Inc., and (2) the user of this document, the user accepts any legal liability or responsibility whatsoever for the consequence of its use or misuse. 

The American Institute of Chemical Engineers (AIChE) has a 30-year history of involvement with process safety for chemical processing plants. Through its strong ties with process designers, builders, operators, safety professionals and academia, the AIChE has enhanced communication and fostered improvement in the high safety standards of the industry. AIChE publications and symposia have become an information resource for the chemical engineering profession on the causes of accidents and means of prevention. 

QRA is fundamentally different from many other chemical engineering activities (e.g., chemistry, heat transfer, reaction kinetics) whose basic property data are theoretically deterministic. For example, the physical properties of a substance for a specific application can often be established experimentally. But some of the basic property data used to calculate risk estimates are probabilistic variables with no fixed values. Some of the key elements of risk, such as the statistically expected frequency of an accident and the statistically expected consequences of exposure to a toxic gas, must be determined using these probabilistic variables. QRA is an approach for estimating the risk of chemical operations using the probabilistic information. And it is a fundamentally different approach from those used in many other engineering activities because interpreting the results of a QRA requires an increased sensitivity to uncertainties that arise primarily from the probabilistic character of the data. 

Chemical Engineering URL s Directory— www.ciw.uni-karlsruhe.de/chem-eng.html Engineering Information—www.ei.org Chemical Information... 

Kletz, T.A. (1984) Cheaper, Safer Plants or Wealth and Safety at Work Notes on Inherently Safer and Simpler Plants, Institution of Chemical Engineers Loss Prevention Information Exchange Scheme - Hazard Workshop Module. 

More extensive data can be found in standard references such as Perry s Chemical Engineering Handbook or the CRC Handbook of Chemistry and Physics. The following table, however will provide some basic information for many common calculations that the process engineer can easily run on his or her PC. 

For over 30 years the American Institute of Chemical Engineers (AIChE) has been involved with process safety and loss control issues in the chemical, petrochemical, hydrocarbon process and related industries and facilities. AIChE publications and symposia are information resources for the chemical engineering and other professions on the causes of process incidents and the means of preventing their occurrences and mitigating their consequences. 

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