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Process approach

Another continuous pasteurization process, known as ultrahigh temperature (UHT), employs a shorter time (2 s) and a higher temperature (minimum 138°C). The UHT process approaches aseptic processiag (Fig. 3). [Pg.354]

Second Law of Thermodynamics. The entropy change of any system together with its surroundings is positive for a real process, approaching zero as the process approaches reversibiUty ... [Pg.481]

Andersson, P. A. 1996 Process Approach to Robust Design in Early Engineering Design Phases. PhD Thesis Department of Machine Design, Lund Institute of Technology, Lund, Sweden. [Pg.381]

Dieter, G. E. 1986 Engineering Design a materials and processing approach, 1st Metric Edition. NY McGraw-Hill. [Pg.384]

Many organizations will not be reaching for ISO/TS 16949 without having put in place either an ISO 9000 compliant quality system or a quality systems that meets QS-9000, VDA 6.1, AVSQ 94, or EAQF 94. The few that may be motivated to use ISO/TS 16949 1999 rather than wait for ISO 16949 2001 should start out by adopting the process approach and resist any temptation to build an element-based quality system ... [Pg.61]

SCRIMP process This Seeman Composites Resin Infusion Process (SCRIMP) is described as a gas-assist resin transfer molding process. As an example glass fiber fabrics/ thermoset vinyl ester polyester plastic and polyurethane foam panels (for insulation) are placed in a segmented tool. A vacuum is pulled with a bag so that a huge amount of plastic can be drawn into the mold (Marco process approach). Its curved roof is made separately and bonded to the box with mechanical and adhesive fastening. It is similar to various reinforced plastics molding processes. [Pg.522]

For quasi-reversible systems (with 10 1 > k" > 10 5 cm s1) the current is controlled by both the charge transfer and mass transport. The shape of the cyclic voltammogram is a function of k°/ JnaD (where a = nFv/RT). As k"/s/naD increases, the process approaches the reversible case. For small values of k°/+JnaD (i.e., at very fast i>) the system exhibits an irreversible behavior. Overall, the voltaimnograms of a quasi-reversible system are more drawn-out and exhibit a larger separation in peak potentials compared to those of a reversible system (Figure 2-5, curve B). [Pg.33]

The closer two particles pass, the greater is their interaction. Still, AJ/J may turn out to be less than 1 even in the case of face to face collision. In this limit collisions are weak, y 1 and the model of the correlated process fits the situation well. If close impacts produce a strong effect, then the influence of more distant paths is negligible, and the process approaches the non-correlated limit y 0. [Pg.19]

We recently demonstrated that photocatalyzed destruction rates of low quantum efficiency contaminant compoimds in air can be promoted substantially by addition of a high quantum efficiency contaminant, trichloroethylene (TCE), in a single pass fixed bed illuminated catalyst, using a residence time of several milliseconds [1-3]. Perchloroethylene (PCE) and trichloropropene (TCP) were also shown to promote contaminant conversion [2]. These results establish a novel potential process approach to cost-effective photocatalytic air treatment for contaminant removal. [Pg.435]

Figure 5.28, effect 4). This process approaches an equilibrium called adsorptive saturation. [Pg.126]

As exergy efficiency approaches 100%, the environmental impact associated with process operation approaches zero, since exergy is only converted from one form to another without loss. Also sustainability approaches infinity because the process approaches reversibility. [Pg.33]

It has to be assumed that these processes are occurring on the boundary between SN1(P) and SN2(P) mechanisms in whose transition states considerable P—0(—Ar) bond cleavage takes place. The lifetime of the resulting, more or less free metaphosphate anion 102 then depends upon the nucleophilicity of the surrounding solvent. With pyridine, for example, a very fast reaction occurs so that the overall process approaches an SN2 reaction. Acceleration of the reaction by amines such as 2,6-lutidine, which are disqualified from acting as nucleophiles by steric hindrance, or by solvents such as dioxane, whiche are presumably too... [Pg.98]

The concentration profiles are shown in Figure 6. As time approaches infinity, the term involving the exponential vanishes and the diffusion process approaches the steady state Eqs. (87) and (88) are then reduced to the steady concentration profile, Eq. (38), and flux, Eq. (39). [Pg.59]

Martin, R. E. (1999), Taphonomy, a Process Approach, Cambridge Univ. Press, Cambridge, UK. [Pg.596]

Founded in San Diego in 1999, Aviva has been fully engaged in the development and application of technologies for drug discovery and healthcare. The major limitations of current sample processing approaches are the inability to isolate reliably cells/molecules... [Pg.258]

Madsen, C. K. Zhao, J. H., Optical Filter Design and Analysis A Signal Processing Approach, Wiley Interscience Publications, New York, NY, 1999, and references therein. [Pg.334]

Wet-weather processes have, in general, been excluded in the text, because they are based on a different concept and perform differently. Microbial and physicochemical processes are contrary to the physical processes dominating in sewers during dry-weather transport of the wastewater. When dealing with combined sewer networks in terms of pollutant loads during overflow events, dry-weather solids deposition and erosion and solids transport during high-flow events are, in addition to the rainfall/runoff hydraulic and sewer solids characteristics, the central physical in-sewer processes. Quite different process approaches are, therefore, required to describe dry-weather and wet-weather sewer performance. [Pg.223]

C. Jakowatz, D. Wahl, P. Eichel, D. Ghiglia, P. Thompson. Spotlight-Mode Synthetic Aperture Radar A Signal Processing Approach, Kluwer Academic Publishers, 1996. [Pg.338]

Heat recovery efficiency is a consideration of major importance in the conversion of coal to secondary fuels. This parameter is defined as the percent of the heating value of the coal used which is recovered as heating value in the desired secondary fuel. Heat recovery efficiency which can be attained in a coal conversion process depends firstly on the theoretical chemical and thermodynamic requirements of the process, and secondly on the practical realization of the process. The first factor determines the theoretical maximum heat recovery efficiency that can be obtained under ideal circumstances. The second factor determines the extent to which the practical process approaches the theoretical ideal. [Pg.302]

The pK of tyrosine explains the absence of measurable excited-state proton transfer in water. The pK is the negative logarithm of the ratio of the deprotonation and the bimolecular reprotonation rates. Since reprotonation is diffusion-controlled, this rate will be the same for tyrosine and 2-naphthol. The difference of nearly two in their respective pK values means that the excited-state deprotonation rate of tyrosine is nearly two orders of magnitude slower than that of 2-naphthol.(26) This means that the rate of excited-state proton transfer by tyrosine to water is on the order of 105s 1. With a fluorescence lifetime near 3 ns for tyrosine, the combined rates for radiative and nonradiative processes approach 109s-1. Thus, the proton transfer reaction is too slow to compete effectively with the other deactivation pathways. [Pg.8]

This new terminology is proposed jointly in the present publication and in Pitard Pierre Gy s Theory of Sampling and C.O. IngamelTs Poisson Process Approach — Pathways to Representative SampUng and Appropriate Industrial Standards . Doctoral thesis, Aalborg University, campus Esbjerg (2009). ISBN 978-87-7606-032-9. [Pg.44]

The databases of NMR data that are the basis of chemometric model development for on-line process control can be developed via several different processing approaches. [Pg.318]

If an infinite number of intercoolers, compressors, reheaters, and turbines are added to a basic ideal Brayton cycle, the intercooling and multicompression processes approach an isothermal process. Similarly, the reheat and multiexpansion processes approach another isothermal process. This limiting Brayton cycle becomes an Ericsson cycle. [Pg.214]

Measirement analysis and improvement The process approach Documented quality management system Objective evidence of the conformance of the laboratory activities to the requirements... [Pg.70]


See other pages where Process approach is mentioned: [Pg.352]    [Pg.367]    [Pg.94]    [Pg.117]    [Pg.247]    [Pg.990]    [Pg.356]    [Pg.206]    [Pg.235]    [Pg.70]    [Pg.722]    [Pg.22]    [Pg.11]    [Pg.211]    [Pg.19]    [Pg.40]    [Pg.136]    [Pg.206]    [Pg.348]    [Pg.234]    [Pg.246]    [Pg.273]    [Pg.288]    [Pg.46]   
See also in sourсe #XX -- [ Pg.46 ]




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Processing approach

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