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Products, salient features

A salient feature of the fluidized bed reactor is that it operates at nearly constant temperature and is, therefore, easy to control. Also, there is no opportunity for hot spots (a condition where a small increase in the wall temperature causes the temperature in a certain region of the reactor to increase rapidly, resulting in uncontrollable reactions) to develop as in the case of the fixed bed reactor. However, the fluidized bed is not as flexible as the fixed bed in adding or removing heat. The loss of catalyst due to carryover with the gas stream from the reactor and regenerator may cause problems. In this case, particle attrition reduces their size to such an extent where they are no longer fluidized, but instead flow with the gas stream. If this occurs, cyclone separators placed in the effluent lines from the reactor and the regenerator can recover the fine particles. These cyclones remove the majority of the entrained equilibrium size catalyst particles and smaller fines. The catalyst fines are attrition products caused by... [Pg.234]

NO Reactions. The most informative derivitization reaction of oxidized polyolefins that we have found for product identification is that with NO. The details of NO reactions with alcohols and hydroperoxides to give nitrites and nitrates respectively have been reported previously, and only the salient features are discussed here (23). The IR absorption bands of primary, secondary and tertiary nitrites and nitrates are shown in Table I. After NO treatment, y-oxidized LLDPE shows a sharp sym.-nitrate stretch at 1276 cm-1 and an antisym. stretch at 1631 cm-1 (Fig. 1), consistent with the IR spectra of model secondary nitrates. Only a small secondary or primary nitrite peak was formed at 778 cm-1. NO treatment of y-oxidized LLDPE which had been treated by iodometry (all -OOH converted to -OH) showed strong secondary nitrite absorptions, but only traces of primary nitrite, from primary alcohol groups (distinctive 1657 cm-1 absorption). However, primary products were more prominent in LLDPE after photo-oxidation. [Pg.383]

Part—I has three chapters that exclusively deal with General Aspects of pharmaceutical analysis. Chapter 1 focuses on the pharmaceutical chemicals and their respective purity and management. Critical information with regard to description of the finished product, sampling procedures, bioavailability, identification tests, physical constants and miscellaneous characteristics, such as ash values, loss on drying, clarity and color of solution, specific tests, limit tests of metallic and non-metallic impurities, limits of moisture content, volatile and non-volatile matter and lastly residue on ignition have also been dealt with. Each section provides adequate procedural details supported by ample typical examples from the Official Compendia. Chapter 2 embraces the theory and technique of quantitative analysis with specific emphasis on volumetric analysis, volumetric apparatus, their specifications, standardization and utility. It also includes biomedical analytical chemistry, colorimetric assays, theory and assay of biochemicals, such as urea, bilirubin, cholesterol and enzymatic assays, such as alkaline phosphatase, lactate dehydrogenase, salient features of radioimmunoassay and automated methods of chemical analysis. Chapter 3 provides special emphasis on errors in pharmaceutical analysis and their statistical validation. The first aspect is related to errors in pharmaceutical analysis and embodies classification of errors, accuracy, precision and makes... [Pg.539]

The following composition illustrates the use of steel hlings for wire sparklers (the salient features of spark production having been discussed during the considerations in the preceding chapter). [Pg.95]

Table V shows the salient features of several Fischer-Tropsch processes. Two of these—the powdered catalyst-oil slurry and the granular catalyst-hot gas recycle—have not been developed to a satisfactory level of operability. They are included to indicate the progress that has been made in process development. Such progress has been quite marked in increase of space-time yield (kilograms of C3+ per cubic meter of reaction space per hour) and concomitant simplification of reactor design. The increase in specific yield (grams of C3+ per cubic meter of inert-free synthesis gas) has been less striking, as only one operable process—the granular catalyst-internally cooled (by oil circulation) process—has exceeded the best specific yield of the Ruhrchemie cobalt catalyst, end-gas recycle process. The importance of a high specific yield when coal is used as raw material for synthesis-gas production is shown by the estimate that 60 to 70% of the total cost of the product is the cost of purified synthesis gas. Table V shows the salient features of several Fischer-Tropsch processes. Two of these—the powdered catalyst-oil slurry and the granular catalyst-hot gas recycle—have not been developed to a satisfactory level of operability. They are included to indicate the progress that has been made in process development. Such progress has been quite marked in increase of space-time yield (kilograms of C3+ per cubic meter of reaction space per hour) and concomitant simplification of reactor design. The increase in specific yield (grams of C3+ per cubic meter of inert-free synthesis gas) has been less striking, as only one operable process—the granular catalyst-internally cooled (by oil circulation) process—has exceeded the best specific yield of the Ruhrchemie cobalt catalyst, end-gas recycle process. The importance of a high specific yield when coal is used as raw material for synthesis-gas production is shown by the estimate that 60 to 70% of the total cost of the product is the cost of purified synthesis gas.
Salient features of the cationic pathway, which was introduced independently by Cabri [8] and Hayashi [9], are presented in Scheme 8G.20. Thus, subsequent to oxidative addition, a vacant coordination site is generated either by triflate dissociation or by halide abstraction by the Ag(I) salt in intermediate 20,4. This vacant coordination site facilitates double-bond coordination to form cationic intermediate 20.5, which ultimately forms the Heck product. [Pg.692]

The salient feature of le as a chiral phase-transfer catalyst is its ability to catalyze the asymmetric alkylation of glycine methyl and ethyl ester derivatives 4 and 5 with excellent enantioselectivities. Since methyl and ethyl esters are certainly more susceptible towards nucleophilic additions than tert-butyl ester, the synthetic advantage of this process is clear, and highlighted by the facile transformation of the alkylation products (Scheme 5.3) [8],... [Pg.74]

The same authors have demonstrated that 1,3-diynes behave in predictable yet distinctive manners compared to simple enynes under electrophilic transition metal-mediated reaction conditions. This characteristic behaviour of 1,3-diynes is presumably caused by the slightly electron-withdrawing nature of the alkynyl substituent, which not only renders preferentially the formation of 5-exotype alkylidenes but also allows for the subsequent [l,3]-metallotropic shift. Several salient features of reactions with this functionality include the following (a) an acetate is more reactive than the tethered alkene as an initiator, generating [l,2]-acetate migrated alkylidene intermediate, whereas an alkene is a better terminator than an acetate/bromide to generate the cyclopropane moiety (b) allene products are not formed at all under current reaction conditions (c) 5-exo/6-endo-type alkylidene formation depends on the heteroatom substituent in the tether (d) facile metallotropic [1,3]-shift of the intermediate alkylidenes occurred whenever possible. [Pg.487]

Since the pioneering work of Siddall, /V./V-dialkyl amides have been evaluated extensively as alternative extractants to TBP (200, 201). The salient features of amides as extractants are (i) low volume of secondary waste generated (completely incinerable), (ii) innocuous nature of chemical and radiolytic degradation products (better decontamination from fission products andregeneration/clean up easier), (iii) low aqueous-phase solubility, (iv) final U and Pu products streams are free of P contamination, and (v) ease of synthesis. However, LOC values of U and Pu as well as viscosity are... [Pg.93]

The initial analysis is frequently represented in chart form to highlight salient features such as growth versus size, where segments may be represented by circles and with each product s market share shown within (see Figure 3.6). [Pg.40]

The second section of the book details application of instrumentation and numerical analysis to spectroscopic analyses in a number of fields. The applications cover fields such as materials science (Chapters 5-8), biomedical science (Chapters 9-11) and agricultural and food sciences (Chapters 12 and 13). Chapter 5 details the application of mid-IR FUR spectroscopic imaging to multicomponent polymeric systems, salient features of data analysis for these systems, and a number of examples. Chapter 6 describes the utility of multichannel detectors to catalyst development and provides examples to demonstrate the translation of laboratory concepts to viable industrial catalysis. Chapter 7 provides an overview, and examples, of the application of near-IR imaging systems to the real world in real time . Issues in the industrial design and analysis of several commercial products are detailed in Chapter 8. [Pg.326]

Supported liquid-phase catalysts (SLPCs) combine the salient features of both homogeneous and heterogeneous catalysis for enhanced catalytic and/or process efficiency (337). SLPC catalysts, in which a liquid-phase (homogeneous) catalyst is dispersed within a porous support, have been used in Wacker-type ethylene oxidation for acetaldehyde and vinyl acetate production (337, 338). In the former case, a traditional homogeneous Wacker catalyst (vide supra) consisting of a chlorinated solution of Pd and Cu chlorides retained on a support with monomodal pore size distribution... [Pg.61]

A detailed study on the binding of Pt uracil blue to closed and nicked circular DNA, reported in 1978 [38], confirmed some of the salient features of the earlier study. However, it was also shown that presumably low-mo-lecular-weight Pt entities not carrying a uracil nucleobase had formed covalent adducts with DNA. Whether or not these Pt species were solvolysis products of the blue used or simply part of the complex mixture, was not obvious. Hints for a hydrolytic decomposition of another blue obtained from 1-methyluracil rather than uracil during reaction with DNA were later found [39], but there appears to be no consensus about the nature of the DNA-binding Pt species. [Pg.386]

Product separation and catalyst recovery at the end of the homogeneous catalyzed reactions, as explained, are in most cases carried out by crystallization, filtration, distillation liquid-liquid extraction, or gas-liquid absorption. These unit operations can be performed in batch or continuous mode. The salient features of these operations are described in the following. [Pg.47]

Radioactivity is significant in the study of environmental phenomena due to its possible effects on living organisms. One finds it for example in the atmosphere (e.g., radon and its decay products), in water near uranium-production sites, in wastes from warfare and nuclear operations, and dispersed as a result of accidents (e.g., the Chernobyl accident, 1986). We will now review some salient features of radioactivity and key radiation properties. [Pg.63]

The academic and patent literature of hydrocarbon pyrolysis is very large. An extensive exposition of various aspects of pyrolysis is given by Albright et al to which the reader is referred for greater detail of many aspects of the industrial uses of pyrolysis. This chapter gives the salient features of the chemistry of hydrocarbon pyrolysis as it applies to describing the key points of the technology and economics of production of olefins. [Pg.33]


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See also in sourсe #XX -- [ Pg.28 , Pg.324 ]




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Product features

Salient Features

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