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Step 4 Process analysis

Having designed the additional processes, you need to examine existing processes and establish the extent to which they are compliant with the relevant requirements of ISO/TS 16949. Remember that the requirements are a framework. They are not exhaustive. Your processes should possess characteristics that are compliant but are likely to possess many other characteristics that are not addressed by the requirements. [Pg.64]


The explorative analysis of data sets by visual data mining applications takes place in a three-step process During the first step (overview), the user can obtain an overview of the data and maybe can identify some basic relationships between specific data points. In the second step (filtering), dynamic and interactive navigation, selection, and query tools will be used to reorganize and filter the data set. Each interaction by the user will lead to an immediate update of the data scene and will reveal the hidden patterns and relationships. Finally, the patterns or data points can be analyzed in detail with specific detail tools. [Pg.476]

Measurements of product gas evolution, mass loss or evolved gas analysis may all be used to study the kinetics of a solid—solid interaction provided that there is strict adherence to the condition that gas evolution occurs concurrently with the solid state process. Clearly this approach is only applicable if there is direct experimental support for a single step process. For example, carbon dioxide release is identified [410] as being... [Pg.37]

When the most likely bottleneck stage and limiting resource have been identified, choosing the best management action may well then require lower-level DES that acts behind the scenes to calculate maximum throughput at each relevant step within the bottlenecked research stage. Such a two-step process of analysis is much more efficient than a bottom-up attempt to map the R D universe before asking critical questions about constraints. [Pg.266]

Once soil samples have been received and properly logged in by the laboratory, there is a multi-step process required to isolate agrochemical residues from the sample matrix so that sensitive, reproducible analysis can occur. Residue methods for agrochemicals in soil involve the basic steps shown in Figure 8. [Pg.872]

Separations in hydrophobic interaction chromatography have been modeled as a function of the ionic strength of the buffer and of the hydrophobicity of the column, and tested using the elution of lysozyme and ovalbumin from octyl-, butyl- and phenyl-Sepharose phases.2 The theoretical framework used preferential interaction analysis, a theory competitive to solvophobic theory. Solvophobic theory views protein-surface interaction as a two-step process. In this model, the protein appears in a cavity in the water formed above the adsorption site and then adsorbs to the phase, with the free energy change... [Pg.129]

The north polar region of Mars consists of variously layered sediments, the upper layer consisting of water ice and thus having a high albedo. More detailed pictures ( 30 cm per pixel) were obtained from the High Resolution Imaging Science Experiment (HiRISE) on board the Mars Reconnaissance Orbiter (MRO). The sediment layers in this region are only about 10 cm thick but seem to be covered with a layer of dust. A detailed analysis of the HiRISE pictures of the north pole deposits indicate that complex, multi-step processes must have occurred at the polar icecaps (Herkenhoff et al., 2007). [Pg.286]

Fig. 9. Pulse microreactor system for use with 13C-labeled hydrocarbons. D, E, and J are microreactors J contains the catalyst to be used for hydrocarbon skeletal reaction D and E are used, when necessary, to generate the required reactant hydrocarbon from a non-hydrocarbon precursor (e.g., alcohol dehydration in D and olefin hydrogenation in E) reactant injected at C. F is a trap which allows the accumulation of products from several reaction pulses before analysis G is a G.P.C. column, K a katharometer. Traps H collect fractions separated on G for subsequent mass spectrometric study. When generating reactant hydrocarbon in D and E, a two-step process is preferable in which, with J below reaction temperature, the purified reactant hydrocarbon is collected in H, and this is recycled as reactant with D and E below reaction temperature but with J at reaction temperature. After C. Corolleur, S. Corolleur, and F. G. Gault, J. Catal. 24, 385 (1972). Fig. 9. Pulse microreactor system for use with 13C-labeled hydrocarbons. D, E, and J are microreactors J contains the catalyst to be used for hydrocarbon skeletal reaction D and E are used, when necessary, to generate the required reactant hydrocarbon from a non-hydrocarbon precursor (e.g., alcohol dehydration in D and olefin hydrogenation in E) reactant injected at C. F is a trap which allows the accumulation of products from several reaction pulses before analysis G is a G.P.C. column, K a katharometer. Traps H collect fractions separated on G for subsequent mass spectrometric study. When generating reactant hydrocarbon in D and E, a two-step process is preferable in which, with J below reaction temperature, the purified reactant hydrocarbon is collected in H, and this is recycled as reactant with D and E below reaction temperature but with J at reaction temperature. After C. Corolleur, S. Corolleur, and F. G. Gault, J. Catal. 24, 385 (1972).
Referring first of all to the reactions over 0.2% platinum/alumina (Table V) the major features of the product distributions may be explained by a simple reaction via an adsorbed C5 cyclic intermediate. For instance, if reaction had proceeded entirely by this path, 2-methylpentane-2-13C would have yielded 3-methylpentane labeled 100% in the 3-position (instead of 73.4%) and would have yielded n-hexane labeled 100% in the 2-position (instead of 90.2%). Similarly, 3-methylpentane-2-I3C would have yielded a 2-methylpentane labeled 50% in the methyl substituent (instead of 42.6%), and would have yielded n-hexane labeled 50% in the 1- and 3-positions (instead of 43.8 and 49% respectively). The other expectations are very easily assessed in a similar manner. On the whole, the data of Table V lead to the conclusion that some 80% or so of the reacting hydrocarbon reacts via a simple one step process via an adsorbed C5 cyclic intermediate. The departures from the distribution expected for this simple process are accounted for by the occurrence of bond shift processes. It is necessary to propose that more than one process (adsorbed C6 cyclic intermediate or bond shift) may occur within a single overall residence period on the catalyst Gault s analysis leads to the need for a maximum of three. The number of possible combinations is large, but limitations are imposed by the nature of the observed product distributions. If we designate a bond shift process by B, and passage via an adsorbed Cs cyclic intermediate by C, the required reaction paths are... [Pg.39]

Stripping voltammetry or stripping analysis has a special place in electrochemistry because of its extensive application in trace metal analysis. Stripping voltammetry (SV) is a two-step process as shown schematically in Fig. 18b. 12. In the first step, the metal ion is reduced to metal on a mercury electrode (thin mercury film on glassy carbon or a HMDE) as amalgam. [Pg.686]

A possible economically attractive alternative would be the production of acrylic acid in a single step process starting from the cheaper base material propane. In the nineteen nineties the Mitsubishi Chemical cooperation published a MoVTeNb-oxide, which could directly oxidise propane to acrylic acid in one step [6], Own preparations of this material yielded a highly crystalline substance. Careful analysis of single crystal electron diffraction patterns revealed that the MoVTeNb-oxide consists of two crystalline phases- a hexagonal so called K-Phase and an orthorhombic I-phase, which is the actual active catalyst phase, as could be shown by preparing the pure phases and testing them separately. [Pg.404]

This analysis corresponds to a comparison of different two-step processes characterized by identical kinetics of the first redox step and different kinetics of the second one. For log(o)i) = -3.5 (curve 1 in Fig. 2.66), 0)2 exhibits no influence on the net peak current, whereas for log(o)i) = -1 (curve 2 in Fig. 2.66) the effect is very week. Over the interval log(o)i) < -3.5 limiting conditions are reached and kinetics of the overall reaction is solely controlled by the first redox step, which is slow and electrochemically irreversible. [Pg.94]

The Swedish Chemical Inspectorate (KEMI) has used substitution analysis to assess biocides with the goal of promoting sustainable agriculture. KEMI uses a seven-step process that evaluates not only the intrinsic... [Pg.8]

Finally, a step away from H NMR in some applications may open up other areas of process analysis. In the current configuration the only nuclei that are really feasible are F, P, Al, and Na. Sodium content of liquid foodstuffs is an obvious area for Na NMR. P NMR has been targeted as a way to identify biological and chemical warfare agents in the held. A portable version of the 60 MHz NMR analyzer could be mounted in a van and driven to scenes of inquiry. [Pg.331]

The nunber of observations that can be tested as seedpoints is limited by the size of the initial set of observations chosen from the data. Because of time constraints, less than 10> of the data set is commonly included in the initial set. To avoid this limitation, the seedpoints are chosen in a two-step process. A trial set of seedpoints is found in the first round and then used for cluster analysis. The unassigned observations from the first round are then sampled for an additional set of seedpoints. The two sets are then combined. This allows many more of the observations in the data set to be sampled as possible seedpoints. In each of the two rounds the seedpoints can be chosen by one of the seven methods listed above. [Pg.122]

The phenomenological analysis (6) of the increase of the helix amount X, shows a two step process the first step is exponential, the second one is logarithmic with time. These two steps can be considered either independent or related to each other, a- If the two steps are independent, then we may write ... [Pg.214]


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