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Industrial chemical system

One of the assumptions underlying the use of a Latin Square is that there should be no interaction between the factors. Since the existence of interaction in industrial chemical systems appears to be common, the Latin Square may not be of wide applicability in this field. [Pg.122]

Exotic chemical systems, mostly oscillatory reactions, but also systems exhibiting multistationarity and chaotic effects, have extensively been investigated. Phenomena in chemical, biological and industrial chemical systems are the experimental basis of the theoretical studies. [Pg.11]

Besway Chemical Systems Ecco Chemicals Greater Southwest Chemicals Panther Industries CD Products Crown Paint Co. [Pg.554]

Identification of Piping Systems, American National Standards Institute, New York, A13.1,1981 Chemical Plant and Refiney Piping, B31.3,1990 Precautionay Eabeling of Ha rdous Industrial Chemicals, Z129.1,1988. [Pg.105]

Evaporation. In most chemical industry evaporation systems, the objective is product recovery, although occasionally the objective is concentration of an organic waste from an aqueous solution, to facihtate incineration. Similar equipment is used extensively for desalination of salt or brackish water (see also Water, supply and desalination). [Pg.230]

Industrial refrigeration - New industrial refrigeration systems that are used by the chemical, petrochemical, pharmaceutical, oil and gas, and metallurgical industries, as well for industrial ice making and for sports and leisure facilities, can use ammonia and hydrocarbons as the refrigerant. Although the product base concerned is small, existing CFC equipment can be retrofitted to use HCFC-22, HFCs and HFC blends, and hydrocarbons. [Pg.36]

Trichloroethane 0.003 0.005 Liver, kidney, or immune system problems Discharge from industrial chemical factories... [Pg.23]

This directory contains the USEPA Pesticide and Industrial Chemical Risk Analysis and Hazard Assessment system. Documentation for PIRANHA is contained in a MANUALS subdirectory enter PIRANHA C where C is a hard disk to receive the output files to run the sy stem. For efficient operation of PIRANHA, transfer the files from the CD-ROM to your hard disk, (it requires 28 MB). Data files are accessed from the CD-ROM when running PIRANHA. [Pg.371]

Several reported chemical systems of gas-liquid precipitation are first reviewed from the viewpoints of both experimental study and industrial application. The characteristic feature of gas-liquid mass transfer in terms of its effects on the crystallization process is then discussed theoretically together with a summary of experimental results. The secondary processes of particle agglomeration and disruption are then modelled and discussed in respect of the effect of reactor fluid dynamics. Finally, different types of gas-liquid contacting reactor and their respective design considerations are overviewed for application to controlled precipitate particle formation. [Pg.232]

Bums and Hazzan demonstrated tlie use of event tree and fault tree analysis in tlie study of a potential accident sequence leading to a toxic vapor release at an industrial chemical process plant. The initiator of tlie accident sequence studied is event P, the failure of a plant programmable automatic controller. Tliis event, in conjunction willi the success or failure of a process water system (a glycol cooling system) mid an operator-manual shutdown of tlie distillation system produced minor, moderate, or major release of toxic material as indicated in Fig. 21.4.1. The symbols W, G, O represent tlie events listed ... [Pg.618]

For more than 50 years, magnetic devices and other devices have been regularly tested and compared with other water treatment methods, notably chemicals. Although irrefutable, documented evidence of their beneficial effect in industrial water systems still seems sadly lacking, they have enjoyed a profitable share of the water treatment market. [Pg.333]

Bason CW, Colbom T. 1998. U.S. application and distribution of pesticides and industrial chemicals capable of disrupting endocrine and immune systems. J Clean Technol Environ Toxicol Occup Med 7 147-156. [Pg.194]

This chapter reviews the reported effects of different types of energy on chemical processing. Many of them are already known for a long time, but were, until recently, mostly used in nonreactive systems such as separation or drying. The focus here is on the (assumed) mechanism, reported effects, and known industrial applications of reactive chemical systems. [Pg.289]

STABREX Stabilized Liquid Bromine9 is far more stable than liquid chlorine bleach. For example, several tons of the new product were shipped to India and stored for one year above 90 °F. The product remained within specification (less than 10% degraded) for the entire year, after which it was successfully used to control fouling in an industrial water system. Chlorine would have completely degraded in this time under these conditions. Chemical wastage was eliminated. Accident risk in transporting oxidant was reduced because less volume was necessary. Table 2 shows the stability of the new product compared to industrial strength chlorine bleach in well-controlled laboratory tests. [Pg.57]

The benefits of replacing chlorine with STABREX are in reducing environmental toxicity (because it is less toxic to aquatic wildlife), in reducing accident risk (because it is less hazardous and easier to handle), and in reducing chemical waste (because it works better, is more stable in transport/storage, is less volatile and less reactive). Environmental toxicity and accident risk have been substantially reduced in more than 2,500 industrial water systems worldwide. [Pg.59]

An industrial treatment system may require some chemical pretreatment before biological treatment even some physical treatment may be desirable. Also, smce the concentrations of the pollutants are usually greater and more predictable than those in municipal wastes, the engineer can design a more specific system than is possible for municipal treatment plants.64 In this case all possibilities must be carefully evaluated by the process engineer. [Pg.452]

Van Vliet, E., Derksen, J. J., and Van den Akker, H. E. A., Modelling of Parallel Competitive Reactions in Isotropic Homogeneous Turbulence Using a Filtered Density Function Approach for Large Eddy Simulations . Proc. PVP01 3rd Int. Symp. on Comput. Techn. for Fluid/Thermal/Chemical Systems with Industrial Appl., Atlanta, GE, USA (2001). [Pg.228]


See other pages where Industrial chemical system is mentioned: [Pg.510]    [Pg.348]    [Pg.228]    [Pg.272]    [Pg.535]    [Pg.263]    [Pg.458]    [Pg.459]    [Pg.1894]    [Pg.35]    [Pg.252]    [Pg.20]    [Pg.483]    [Pg.894]    [Pg.1047]    [Pg.271]    [Pg.323]    [Pg.163]    [Pg.37]    [Pg.104]    [Pg.350]    [Pg.1]    [Pg.19]    [Pg.437]    [Pg.21]    [Pg.173]    [Pg.169]    [Pg.118]    [Pg.17]    [Pg.232]    [Pg.761]   
See also in sourсe #XX -- [ Pg.11 ]




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