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Whole process

Raw materials efficiency. In choosing the reactor, the overriding consideration is usually raw materials efficiency (bearing in mind materials of construction, safety, etc.). Raw material costs are usually the most important costs in the whole process. Also, any inefficiency in raw materials use is likely to create waste streams that become an environmental problem. The reactor creates inefficiency in the use of raw materials in the following ways ... [Pg.60]

Figure 13.8 The grand composite curve for the whole process apparently requires only high-pressure steam generation from boiler feedwater. Figure 13.8 The grand composite curve for the whole process apparently requires only high-pressure steam generation from boiler feedwater.
From the probability distributions for each of the variables on the right hand side, the values of K, p, o can be calculated. Assuming that the variables are independent, they can now be combined using the above rules to calculate K, p, o for ultimate recovery. Assuming the distribution for UR is Log-Normal, the value of UR for any confidence level can be calculated. This whole process can be performed on paper, or quickly written on a spreadsheet. The results are often within 10% of those generated by Monte Carlo simulation. [Pg.169]

If high wellhead pressures are available over long periods, cooling can be achieved by expanding gas through a valve, a process known as Joule Thomson (JT) throttling. The valve is normally used in combination with a liquid gas separator and a heat exchanger, and inhibition measures must be taken to avoid hydrate formation. The whole process is often termed low temperature separation (LTS). [Pg.251]

Covalent immobilization of proteins on nricrostmctured gold surfaces was studied in [226]. On Arese substrates, which were prepared by pCP aird etching. Are immobilization sites of proteins could be spatially controlled using air amino-reactive SAM. The whole process, i.e. production of Are micropattemed substrate including SAM exchairge aird protein immobilization, took a reasonably small amount of time ( 24 h), providing some flexibility in the experimental work. [Pg.2628]

A white gelatinous precipitate of aluminium hydroxide is obtained when an alkali is added to an aqueous solution of an aluminium salt. Addition of an excess of caustic alkali causes the precipitate to redissolve, the whole process being reversed by the addition of a strong acid the actual substance present at any time depending on... [Pg.150]

After selection of descriptors/NN training, the best networks were applied to the prediction of 259 chemical shifts from 31 molecules (prediction set), which were not used for training. The mean absolute error obtained for the whole prediction set was 0.25 ppm, and for 90% of the cases the mean absolute error was 0.19 ppm. Some stereochemical effects could be correctly predicted. In terms of speed, the neural network method is very fast - the whole process to predict the NMR shifts of 30 protons in a molecule with 56 atoms, starting from an MDL Molfile, took less than 2 s on a common workstation. [Pg.527]

Fractional Distillation under Reduced Pressure. One great disadvantage of the simple vacuum-distillation apparatus shown in Fig. 12(a) is that, if more than one fraction distils, the whole process has to be stopped after collecting each consecutive fraction, in order to change the receiver F. This may be overcome by replacing the simple receiving flask F by a pig (Fig. 13) which collects consecutive... [Pg.30]

The whole process is then repeated exactly as described above. The absorption tubes are then weighed and attached to the apparatus ffull details will be given below when a complete combustion is described), and the above process repeated. The absorption tubes are detached and reweighed. They should not have gained in weight by more than o i... [Pg.474]

The chief disadvantage of the simple vacuum distillation set up shown in Fig. 11,19, 1 is that, if more than one fraction is to be collected, the whole process must be stopped in order to change the receiver B. It is of value, however, for the distillation of solids of low melting point the distillate can easily be removed from the receiver by melting and pouring out. For routine work, involving the collection of several fractious under reduced pressure, the most convenient receiver is the so-called Perkin triangle the complete apparatus for vacuum distillation is depicted in F g. 11,20, 1. The Claisen fla.sk A is fitted to a. short water... [Pg.108]

All these intermediate complexes undergo various transformations such as insertion, transmetallation, and trapping with nucleophiles, and Pd(0) is regenerated at the end in every case. The regenerated Pd(0) starts the catalytic cycle again, making the whole process catalytic. These reactions catalyzed by Pd(0) are treated in Chapter 4. [Pg.16]

TT-Aliylpalladium chloride reacts with a soft carbon nucleophile such as mal-onate and acetoacetate in DMSO as a coordinating solvent, and facile carbon-carbon bond formation takes place[l2,265], This reaction constitutes the basis of both stoichiometric and catalytic 7r-allylpalladium chemistry. Depending on the way in which 7r-allylpalladium complexes are prepared, the reaction becomes stoichiometric or catalytic. Preparation of the 7r-allylpalladium complexes 298 by the oxidative addition of Pd(0) to various allylic compounds (esters, carbonates etc.), and their reactions with nucleophiles, are catalytic, because Pd(0) is regenerated after the reaction with the nucleophile, and reacts again with allylic compounds. These catalytic reactions are treated in Chapter 4, Section 2. On the other hand, the preparation of the 7r-allyl complexes 299 from alkenes requires Pd(II) salts. The subsequent reaction with the nucleophile forms Pd(0). The whole process consumes Pd(ll), and ends as a stoichiometric process, because the in situ reoxidation of Pd(0) is hardly attainable. These stoichiometric reactions are treated in this section. [Pg.61]

Subsequent commercial development utilized 4,4 -diaminodiphenylamine as the starting material, and the whole process may be carried out in situ on the fabric. [Pg.197]

Precise kinetic electroanalytical data permit to describe quantitatively the kinetics of the whole process with a precision that has never been achieved before by patch-clamp techniques or spectroscopic near-field methods. This enables to investigate finely these events and to identify the exact physicochemical nature of all the individual physicochemical and biological factors which concur to produce vesicular release. [Pg.10]

The recoiler is driven by motor M - that adjusts its speed and tension as calculated for the whole process line. It is this drive and the bridles that maintain the required tension throughout the process and make the pay-off reel drives operate as regenerative units. [Pg.144]

Step 7 Write an Overall Material Balance. Remember that the P2 audit focuses on a unit process, but that there are individual unit operations that make up this process. The team will need to develop a series of material balances for each unit operation, and an overall material balance about the entire unit process, to bring closure to a solution of parameters of interest. The individual or component material balances developed may be summed to give a balance for the whole process, production area, or factory. [Pg.371]

The team is now at the point where it can prepare a material balance at a scale appropriate to the level of detail required in the assessment. For example, you may require a material balance for each unit operation, or one for a whole process may be sufficient. Decide on various levels of detail that may be needed. [Pg.376]

After recording the information for one process variable, another process variable is selected, as shown in Figure 3.3.4-1, and the process is repeated until all important process variables have been considered for an operating mode then another operating mode is selected and the whole process is repeated. [Pg.91]

A critical assembly is a split bed on which fissionable material used to mock up up a separated reactor core that is stacked half on each half. One half is on roller guides so that the two halves may be quickly pulled apart if the neutron multiplication gets too high. Use the Preliminary Hazards Analysis method described in section 3,2.1 to identify the possible accidents that may occur and the qualitative probabilities and consequences. List the initiators in a matrix to systematically investigate the whole process. Don t forget human error. [Pg.243]


See other pages where Whole process is mentioned: [Pg.97]    [Pg.1895]    [Pg.298]    [Pg.475]    [Pg.527]    [Pg.1044]    [Pg.264]    [Pg.321]    [Pg.328]    [Pg.328]    [Pg.340]    [Pg.28]    [Pg.5]    [Pg.271]    [Pg.75]    [Pg.26]    [Pg.83]    [Pg.14]    [Pg.643]    [Pg.100]    [Pg.138]    [Pg.157]    [Pg.298]    [Pg.455]    [Pg.91]    [Pg.90]    [Pg.239]    [Pg.245]    [Pg.690]    [Pg.318]    [Pg.11]   
See also in sourсe #XX -- [ Pg.1419 ]




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