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Production in practice

The segregation of safety from work practice and productivity enables the development of relationships between them that can be traced back to these earliest of arguments safety readily becomes involved in confrontational and negative relationships with the processes of production. [Pg.116]

The case against safety is often based on this type of [Pg.116]

The segregated entity of safety has no place within practice, and for this operative it even has the power to stop production. Safety has become the practice of just safety itself, and is firmly and clearly positioned as a hindrance to his work. The workforce is on site to work - and to work efficiently - not to work under the restrictions that safety can place on construction tasks, be they work methods designed to reduce risks, PPE to protect, or planning measures that require preparation in the form of records, discussions and signatures. This reveals one of the fundamental shared understandings of the construction industry itself, as suggested by the considerations of the site context made in Chapter 2, that of the fundamental truths of construction site context is quite simply that production is king. [Pg.116]

Although safety practices such as risk assessments are arguably not too onerous when considered practically within the scope of site work and the potential dangers found there, they are still not production. As found in Chapter 5, risk is often devalued within the shared understandings of safety, and is often accorded the [Pg.116]

Evaluations are made of this relationship between the practice of work and the practice of safety, and value judgements not dissimilar to those the Victorian mill owners made between outputs and workforce welfare. Within this comment above, efforts to practice safety are even positioned as more onerous than the work itself, and its negative role alongside that of production is clearly established. This shared understanding of safety will resonate readily for those involved in safety management at the site level. For example, the time it takes to follow safe working procedures is often used to justify violations, and as a site manager, the number of times I heard  [Pg.117]


It is possible to produce adipic acid by a variety of methods from such diverse starting points as benzene, acetylene and waste agricultural products. In practice, however, benzene is the favoured starting point and some of the more important routes for this material are illustrated in Figure 18.4... [Pg.480]

Blumann and Zeitschel have obtained these degradation products in practically equal amounts from both geraniol and nerol, so that there no longer exists the slightest doubt as to the constitution of nerol. [Pg.113]

The substitution reaction of toluene with Br2 can, in principle, lead to the formation of three isomeric bromotoluene products. In practice, however, only o- and jp-bromotoluene are formed in substantial amounts. The meta isomer is not formed. Draw the structures of the three possible carbocation intermediates (Problem 15.48), and explain why ortho and para products predominate over meta. [Pg.546]

A reactivity index which accurately predicts the site selectivity of the photoisomerization of cycloheptatrienes to their bicyclic valence tautomers fails with 1//-azepines.237 For example, for methyl 2-methyl-1//-azepine-l-carboxyIatc (14), the 1-methyl isomer 16 is the predicted major product in practice the reverse is true. [Pg.177]

You should have identified that the acyl moiety, phenylacetic add, is the second product arising from the hydrolysis of penicillin G. This could be recovered from the reaction mixture and reused as a precursor for penicillin G production. In practice, an integrated process is used. We can represent this in the following way ... [Pg.173]

Bieber reported that the reaction of bromoacetates is greatly enhanced by catalytic amounts of benzoyl peroxide or peracids and gives satisfactory yields with aromatic aldehydes. A radical chain mechanism, initiated by electron abstraction from the organometallic Reformatsky reagent, is proposed (Scheme 8.27).233 However, an alternative process of reacting aldehydes with 2,3-dichloro-l-propene and indium in water followed by ozonolysis provided the Reformatsky product in practical yields.234 An electrochemical Reformatsky reaction in an aqueous medium and in the absence of metal mediator has also been reported.235... [Pg.266]

Although the crystals are likely to be pure, the mass of crystals will retain some liquid when the solid crystals are separated from the residual liquid. If the adhering liquid is dried on the crystals, this will contaminate the product. In practice, the crystals will be separated from the residual liquid by filtration or centrifuging. Large uniform crystals separated from a low-viscosity liquid will retain the smallest proportion of liquid. Nonuniform crystals separated from a viscous liquid will retain a higher proportion of liquid. It is common practice to wash the crystals in the filter or centrifuge. This might be with fresh solvent, or in the case of melt crystallization, with a portion of melted product. [Pg.205]

Polejes, J. D Nylon and polyester production - in practice, Presentation given at the Fundamentals of Melt Spinning and Yam Production Conference, Clemson University, Clemson, SC, February 26-27, 1992. [Pg.395]

Chemical reactions are in principle equilibria between one or two educts and products. In practice, the preferred preparative reactions proceed irreversibly. Syntheses of products from three or more educts are usually sequences of preparative steps, where after each reaction step its intermediate or hnal product must be isolated and purihed while the yield decreases. Exceptions can be the reactions of three components on solid surfaces and also some MCRs with a-additions of intermediate cations and anions onto the isocyanides. [Pg.4]

Ciystallization from solution is an important separation and purification process in a wide variety of industries. These range from basic materials such as sucrose, sodium chloride and fertilizer chemicals to pharmaceuticals, catalysts and specialty chemicals. The major purpose of crystallization processes is the production of a pure product. In practice however, a number of additional product specifications are often made. They may include such properties as the ciystd size distribution (or average size), bulk density, filterability, slurry viscosity, and dry solids flow properties. These properties depend on the crystal size distribution and crystal shape. The goal of crystallization research therefore, is to develop theories and techniques to allow control of purity, size distribution and shape of crystals. [Pg.2]

The final example of the intramolecular 1,3-dipolar cycloadditions of nitrile oxides is the formation of the norbornadiene-derived tetracyclic adducts 146, described by Tam and co-workers (240,241). The nitrile oxide 145, formed from 144 by dehydration, can in principle give rise to four different cycloaddition products (three [2,3]-cycloaddition products). In practice, only diastereomer 146 was obtained. The reaction was used on substrates with a variety of different substituents (R=H, Me, hexyl. Cl, Br, C02Me, CH20Me), and in these cases, yields ranging between 66-89% were obtained (Scheme 12.48). [Pg.849]

An alternative and more costly approach is to actually follow the reaction from transition state to both the reactants and (independently) the products. In practice, this involves optimization subject to a fixed position along the reaction coordinate. A number of schemes for doing this have been proposed, and these are collectively termed Intrinsic Reaction Coordinate methods. Note, that no scheme is unique while the reactants, products and transition state are well defined points on the overall potential energy surface, there are an infinite number of pathways linking them together, just like there are an infinite number of pathways leading over a mountain pass. [Pg.420]

Contrary to the optical resolutions described in Sections 2.1.1.-2.1.3., which depend on the solubility or chromatographic properties ( Thermodynamic resolution ), the kinetic resolution rests on rate differences shown by the enantiomers when reacted with an optically active reagent. In the ideal case, only one enantiomer is converted into the envisaged product and the other enantiomer is unchanged. In this way, optical resolution is reduced to the more simple separation of two different reaction products. In practice, only two methods of kinetic resolution are reasonably general and reliable the Sharpless epoxidation of allylic alcohols and the enzymatic transesterification of racemic alcohols or carboxylic acids. [Pg.95]

Thus, on a chemical basis, it is possible to define the hydrodesulfurization process in terms of the feedstock type and the required products. In practice, it may actually be difficult, if not impossible, to carry out nondestructive hydrogenation and completely eliminate carbon-carbon bond scission as in the case of the desulfurization of naphtha. For heavy oils and residua, it is usually preferable to promote hydrocracking as an integral part of the desulfurization process. [Pg.183]

Steam plants usually operate on the Rankine cycle [9,10], as shown in Figure 9.9. This figure shows the ideal Rankine cycle in the sense that the pump and turbine operate isentropically, that is, reversibly or without entropy production. In practice, these will operate with entropy production. [Pg.116]

Adhesive and sealant manufacturers employ rheological additives for thickening and to prevent sag of their products. In practice, rheological additives may provide benefits in addition to viscosity or flow control. When properly formulated into adhesives and sealants, rheological additives can... [Pg.162]

The following points are to be noted. First of all, complexes 5.1, 5.3, 5.5, and 5.7 are 18-electron complexes, while the rest are 16-electron ones. Second, conversions of 5.3 to 5.4 and 5.5 to 5.6 are the two insertion steps. The selectivity towards n-butyraldehyde is determined in the conversion of 5.3 to 5.4. It is possible that a rhodium-isopropyl rather than rhodium-propyl complex is formed. In such a situation on completion of the catalytic cycle isobutyral-dehyde will be the product. In practice both the n-propyl and the /-propyl complexes of rhodium are formed, and a mixture of n-butyraldehyde and /-butyraldehyde is obtained. This aspect is discussed in greater detail in the following section. Third, the catalyst precursor 5.1 undergoes ligand dissocia-... [Pg.86]

Monomer casting is effective for the fabrication of shaped products in practically all sizes and thicknesses. It also provides economic advantages in low or high volume manufacture. Cast parts can be either produced to size or they can be cast and then machined to strict tolerances as required in accordance with end-use needs. Monomers of the lactam family are used to make cast nylon. They will polymerize under various conditions. [Pg.403]

Phenolic adhesives continue to be the most significant adhesives for the production of weather-resistant wood products. The energy crisis of the seventies, the cost of phenol, and the inevitable decline in petroleum reserves have caused the wood industry to focus attention on obtaining adhesive self-sufficiency (1). This concern arises primarily from the questionable longterm availability of resins and secondarily from the economics of adhesive resin use. Ready availability of adhesive resins is critical to the manufacture of bonded wood products. In practical terms, this means that new adhesive systems are needed in which part, or perhaps all, of the petroleum-derived phenolic component is replaced... [Pg.352]

The definition of LSF is theoretically based (Section 2.3.3), and in the form given above applies to clinkers if corrected by subtracting O.7SO3 from CaO, it may be applied to cements. It largely governs the ratio of alite to belite and also shows whether the clinker is likely to contain an unacceptable proportion of free lime, a value of 1.0 or above indicating that the latter will be present at equilibrium at the clinkering temperature and thus liable to persist in the product. In practice, values up to 1.02 may be acceptable typical values for modern clinkers are 0.92-0.98. Other parameters similar in... [Pg.61]


See other pages where Production in practice is mentioned: [Pg.502]    [Pg.250]    [Pg.517]    [Pg.696]    [Pg.291]    [Pg.315]    [Pg.1000]    [Pg.359]    [Pg.75]    [Pg.114]    [Pg.1]    [Pg.149]    [Pg.243]    [Pg.291]    [Pg.527]    [Pg.291]    [Pg.46]    [Pg.97]    [Pg.515]    [Pg.528]    [Pg.768]    [Pg.502]    [Pg.435]    [Pg.293]    [Pg.155]    [Pg.82]    [Pg.12]    [Pg.26]    [Pg.94]    [Pg.139]   
See also in sourсe #XX -- [ Pg.116 , Pg.117 , Pg.118 , Pg.119 ]




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