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Process equipment centrifuges

Fig. 1. Fine chemicals plant design showing successive additions of processing equipment, where A represents the reaction vessel with agitator B, centrifuge C, dryer D, crystaUi2ation vessel E, raw material feed tanks F, centrifuge which may have an automatic discharge G, mother Hquor tank H,... Fig. 1. Fine chemicals plant design showing successive additions of processing equipment, where A represents the reaction vessel with agitator B, centrifuge C, dryer D, crystaUi2ation vessel E, raw material feed tanks F, centrifuge which may have an automatic discharge G, mother Hquor tank H,...
The compressor or blower installation in a typical refinery or chemical process unit is not out-of-doors completely. Some form of shelter often is provided, ranging from only a roof to a completely closed building. When process equipment such as a centrifugal gas compressor, which is not hazardous in normal operation, is present in the shelter, the hazard classification depends on the extent to that which the shelter restricts ventilation. The extent of the shelter provided determines the area classification and the type of motor enclosure that should be applied. [Pg.275]

The application of force to a stationary or moving system can be described in static, kinematic, or dynamic terms that define the mechanical similarity of processing equipment and the solids or liquids within their confines. Static similarity relates the deformation under constant stress of one body or structure to that of another it exists when geometric similarity is maintained even as elastic or plastic deformation of stressed structural components occurs [53], In contrast, kinematic similarity encompasses the additional dimension of time, while dynamic similarity involves the forces (e.g., pressure, gravitational, centrifugal) that accelerate or retard moving masses in dynamic systems. The inclusion of tune as another dimension necessitates the consideration of corresponding times, t and t, for which the time scale ratio t, defined as t = t It, is a constant. [Pg.80]

Centrifugal, motor-driven pumps are the only type of process equipment that is relatively cheap. [Pg.301]

Processing equipment (dryers, mills, filters, mixers, centrifuges, etc.). [Pg.183]

All the major process equipment, such as vessels, reactors, columns, furnaces, heat exchangers, coolers, pumps, compressors, motors, fans, turbines, filters, centrifuges, dryers, etc., including field fabrication and testing if necessary ... [Pg.299]

The basic raw materials required include starting culture E. coli cells), nutrients (glucose and salts), tryptophan, water, ammonia and air. The process equipment includes fermentor, mixing tank, continuous heat sterilizer, centrifugal compressor, air filter and storage tank. [Pg.426]

Timothy C. Frank, Ph.D. Research Scientist and Sr. Technical Leader, The Dow Chemical Company Member, American Institute of Chemical Engineers (Section Editor, Introduction and Overview, Thermodynamic Basis for Liquid-Liquid Extraction, Solvent Screening Methods, Liquid-Liquid Diversion Fundamentals, Process Fundamentals and Basic Calculation Methods, Dual-Solvent Fractional Extraction, Extractor Selection, Packed Columns, Agitated Extraction Columns, Mixer-Settler Equipment, Centrifugal Extractors, Process Control Considerations, Liquid-Liquid Phase Separation Equipment, Emerging Developments)... [Pg.1687]

FIG. 15-59 CINC centrifugal separator. Courtesy of CINC Processing Equipment, Inc.)... [Pg.1778]

The ability to separate a mixture of two liquid phases is critical to the successful operatiou of mauy chemical aud petrochemical processes. Besides its obvious importauce to liquid-liquid extractiou aud washing operations, liquid-liquid phase separation can be a critical factor in other operations including two-liquid-phase reaction, azeotropic distillation, and industrial wastewater treatment. Sometimes the required phase separation can be accomplished within the main process equipment, such as in using an extraction column or a batch-wise, stirred-tank reactor but in many cases a stand-alone separator is used. These include many types of gravity decanters, filter-type coalescers, coalescers filled with granular media, centrifuges, and hydrocyclones. [Pg.1782]


See other pages where Process equipment centrifuges is mentioned: [Pg.43]    [Pg.438]    [Pg.529]    [Pg.27]    [Pg.83]    [Pg.1737]    [Pg.24]    [Pg.773]    [Pg.37]    [Pg.223]    [Pg.579]    [Pg.553]    [Pg.90]    [Pg.61]    [Pg.43]    [Pg.595]    [Pg.603]    [Pg.48]    [Pg.150]    [Pg.172]    [Pg.1332]    [Pg.94]    [Pg.43]    [Pg.59]    [Pg.979]    [Pg.2651]    [Pg.1777]    [Pg.1778]    [Pg.1457]    [Pg.1097]    [Pg.91]    [Pg.92]    [Pg.264]    [Pg.1771]    [Pg.1772]   
See also in sourсe #XX -- [ Pg.149 ]




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