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Process industrial

Hydrodenitrogenation (HDN) processes in current industry are not separated from the other hydrotreatments, viz, HDS, HDO, and HDM. A clear description of the HDS processes for conventional petroleum distillation was [Pg.129]

The important fact about HDN from an industrial point of view is the higher consumption of H2 compared to the classical HDS treatment of [Pg.131]

Refinery Autoproduction (reforming) in 103m3/day Extra production (natural gas) in 103m3/day [Pg.131]

Katzer, and G. C. A. Schuit, Chemistry of Catalytic Processes , McGraw-Hill Series in Chemical Engineering , McGraw-Hill Inc., New York, 1979. [Pg.131]

Jacobsen, Preprint of Nato Advanced Study Institute Series on Surface properties and Catalysis by Non-metals oxides, sulfides. , Lille, France, Sept. 1982. [Pg.131]

Separations by chromatography are carried out in the pharmaceutical and food industiy, for instance, the isolation of specific polysaccharides. As an example a mixture of glucose and fractose is separated by elution chromatography. The differences of the physical properties of isomers are often very small with the consequence that most of the known separation processes cannot be economically used. Here chromatography is an excellent tool. This is true for racemic mixtures. Enantiomers are separated by the apphcation of chiral stationary phases. Sometimes ten-side micellar solutions or mixtures of solvents are used as the mobile phase. [Pg.551]

Anions attached on anion exchange resins can be replaced by other anions (OH, COj , SO4, Cr,etc.) [Pg.551]

Besides polymeric resins also zeolites Z are used for the exchange of ions. For instance fiee mobile Na ions can be exchanged by cations Ca according to [Pg.551]

This exchange process is apphed for the softening of water. The reaction takes place until the capacity of the ion exchange solid material is used or the total number of attached ions is replaced by ions provided by the solution according to equilibrium. Note tliat this capacity is constant and does not depend on the concentration of the solution - in contrary to adsorption. [Pg.552]

In cation exchange resins an exchange of protons or metalhc ions takes place. With the acid group A this reaction can be described by [Pg.552]

This process is a good example of how a new procedure can at the same time be cost-efficient and environmentally friendly. The principles of this process have been extended, and Rhodia is also manufacturing acetoveratrole at the same plant by use of a zeolite-based process. [Pg.169]

These are more or less identical in both types of process, and comprise the following  [Pg.98]

Partial oxidation techniques were the first to. he industrialized. After having been outclassed for some time by iron molybdate processes, they have marked substantial improvements in recent years. The main processes include the following  [Pg.98]

The earliest employs supported silver crystals. It leads to a heat balance equalized between the vaporizer and the exchanger/reactor stage. It avoids methanol distillation and recycling, and achieves sufficient once-through conversion to leave the residual alcohol in the formaldehyde solution. The total yield is 87.5 molar per cent based on the methanol introduced, and 91 per cent in relation to the methanol converted114. The formaldehyde concentration of the final product ranges from 40 to 44 per cent weight [Pg.99]

Hydrogen, synthesis gases and their derivatives Chapter [Pg.100]

The catalyst is a mixture of metallic oxides deposited in a fixed bed in a multi-tube reactor and operating in the vapor phase. The beat of reaction is removed by the circulation of molten salts. Conversion takes place at 450 to 500 C, at 0.1. 10 Pa absolute, with YHSV ranging from 1000 to 4000 h. Once-through conversion ranges from 90 to 100 per cent and yield from 70 to 80 molar per cent One unit is in operation in Japan. [Pg.102]

The vast majority of essential oils are produced from plant material in which they occur by different kinds of distillation or by cold pressing in the case of the peel oils from citrus fruits. [Pg.8]

Expression or cold pressing is a process in which the oil glands within the peels of citrus fruits are mechanically crushed to release their content. There are several different processes used for the isolation of citrus oils however, there are four major currently used processes. Those are pellatrice and sfumatrice—most often used in Italy—and the Brown peel shaver as well as the FMC extractor, which are used predominantly in North and South America. For more details, see, for example, Tawrence 1995. All these processes lead to products that are not entirely volatile because they may contain cou-marins, plant pigments, and so on however, they are nevertheless acknowledged as essential oils by the International Organization for Standardization, the different pharmacopoeias, and so on. [Pg.8]

In contrast, extracts obtained by solvent extraction with different organic solvents, with liquid carbon dioxide or by supercritical uid extraction (SFE) may not be considered as true essential oils however, they possess most often aroma pro les that are almost identical to the raw material from which they have been extracted. They are therefore often used in the avor and fragrance industry and in addition in food industry, if the chosen solvents are acceptable for food and do not leave any harmful residue in food products. [Pg.9]


We have paid particular attention to industrial processes and have tried to give some indication of the use of particular chemicals. In order to give some idea of the relative magnitudes of production we have included data on annual production. In this, because of availability of data, we have not been entirely consistent in including common data or common units. (World, U.S. or European production figures are used as seem most appropriate or up-to-date - and it must be remembered that for most speciality chemicals U.S. production is dominant.)... [Pg.5]

The use of tracers enables efficient and reliable measurements of oil, gas and water flow in industrial process units and pipe line systems under production conditions thus fundamentally being non-destructive testing methods. Typical problems which can be efficiently assessed by tracer studies include ... [Pg.1053]

Jones J T and Berard M F 1972 Ceramics Industrial Processing and Testing (Ames, lA The Iowa State University Press) pp 14-38... [Pg.2773]

The reactions of biopolymers at interfaces fonn tire basis of some extremely important industrial processes. The primary process in all cases is tire adsorjDtion of biomolecules, usually proteins. If ultimately living cells are adsorbed, tliis always takes place onto a preadsorbed protein layer (which may be secreted by tire cells themselves [130]). These processes can be classified into tliree categories ... [Pg.2839]

Most chemically reacting systems tliat we encounter are not tliennodynamically controlled since reactions are often carried out under non-equilibrium conditions where flows of matter or energy prevent tire system from relaxing to equilibrium. Almost all biochemical reactions in living systems are of tliis type as are industrial processes carried out in open chemical reactors. In addition, tire transient dynamics of closed systems may occur on long time scales and resemble tire sustained behaviour of systems in non-equilibrium conditions. A reacting system may behave in unusual ways tliere may be more tlian one stable steady state, tire system may oscillate, sometimes witli a complicated pattern of oscillations, or even show chaotic variations of chemical concentrations. [Pg.3054]

A major difficulty in an inorganic text is to strike a balance between a short readable book and a longer, more detailed text which can be used for reference purposes. In reaching what we hope is a reasonable compromise between these two extremes, we acknowledge that both the historical background and industrial processes have been treated very concisely. We must also say that we have not hesitated to simplify complicated reactions or other phenomena—thus, for example, the treatment of amphoterism as a pH-dependent sequence between a simple aquo-cation and a simple hydroxo-anion neglects the presence of more complicated species but enables the phenomena to be adequately understood at this level. [Pg.458]

It should be emphasised that whereas the interaction of a sodium salt and an acid chloride is a convenient general laboratory method for preparing all classes of anhydrides, acetic anhydride is prepared on a large scale by other and cheaper methods. Industrial processes are based on reactions indicated by the equations ... [Pg.116]

Hannart, B. and Hoplinger, E.J., 1998. Laminar flow in a rectangular diffuser near Hele-Sliaw conditions - a two dinien.sioiial numerical simulation. In Bush, A. W., Lewis, B. A. and Warren, M.D. (eds), Flow Modelling in Industrial Processes, cli. 9, Ellis Horwood, Chichester, pp. 110-118. [Pg.189]

The industrial process for preparing the reagent usually permits a little hydrolysis to occur, and the product may contain a little free calcium hydroxide or basic chloride. It cannot therefore be employed for drying acids or acidic liquids. Calcium chloride combines with alcohols, phenols, amines, amino-acids, amides, ketones, and some aldehydes and esters, and thus cannot be used with these classes of compounds. [Pg.140]

The large heat of vaporisation of water can reduce the economic feasibility of water in industrial processes. [Pg.32]

In an imioortant industrial process, the Carroll reaction , an ahphatic version of the Claisen rearrangement occurs. See if you can find the right mechanism ... [Pg.105]

BENZALDEHYDE The precursor for speed. It makes up nearly 100% of bitter almond oil. Not a very popular oil with the DEA. Some hints Benzaldehyde is indispensable for the flavoring industry. It is the flavor in almond extract and synthetic benzaldehyde is used in all cherry flavorings. Also, there is currently a little loophole in the system when it comes to a product called Roasted Cassia Oil . Apparently, some manufacturers take cassia oil and run it through some sort of industrial process to change it into benzaldehyde. No one wanted to tell Strike the particulars of how this was done. But one company chemist gave me some hints (You can get really chatty with some of these guys). [Pg.46]

Many saturated nitrogen heterocycles are commercially available from industrial processes, which involve, for example, nucleophilic substitution of hydroxyl groum by amino groups under conditions far from laboratory use, e.g. [Pg.149]

Of course. Pd is a noble metal and expensive, but it is much less expensive than Rh, Pt. and Os. Also, the toxicity of Pd has posed no problem so far. The fact that a number of industrial processes (more than ten at least) based on Pd-catalyzed reactions have been developed and are now operated reflects these advantages of using Pd catalysts commercially[l]. [Pg.1]

Formation of acetaldehyde and metallic Pd by passing ethylene into an aqueous solution of PdCl2 was reported by Phillips in 1894 15] and used for the quantitative analysis of Pd(II)[16], The reaction was highlighted after the industrial process for acetaldehyde production from ethylene based on this reaetion had been developed[l,17,18]. The Wacker process (or reaction) involves the three unit reactions shown. The unique feature in the Wacker process is the invention of the in situ redox system of PdCl2-CuCl2. [Pg.22]

Difunctionalization with similar or different nucleophiles has wide synthetic applications. The oxidative diacetoxylation of butadiene with Pd(OAc)i affords 1,4-diacetoxy-2-butene (344) and l,2-diacetoxy-3-butene (345). The latter can be isomerized to the former. An industrial process has been developed based on this reaction. The commercial process for l,4-diacetoxy-2-butene (344) has been developed using the supported Pd catalyst containing Te in AcOH. 1,4-Butanedioi and THF are produced commercially from 1,4-diacetoxy-2-butene (344)[302]. [Pg.67]

The conjugated diene 1 3 butadiene is used m the manufacture of synthetic rubber and IS prepared on an industrial scale m vast quantities Production m the United States is currently 4 X 10 Ib/year One industrial process is similar to that used for the prepara tion of ethylene In the presence of a suitable catalyst butane undergoes thermal dehy drogenation to yield 1 3 butadiene... [Pg.404]

A large number of organometallic compounds are based on transition metals Examples include organic derivatives of iron nickel chromium platinum and rhodium Many important industrial processes are catalyzed by transition metals or their complexes Before we look at these processes a few words about the structures of transition metal complexes are m order... [Pg.608]

The preparation and structure determination of ferrocene marked the beginning of metallocene chemistry Metallocenes are organometallic compounds that bear cyclo pentadiemde ligands A large number are known even some m which uranium is the metal Metallocenes are not only stucturally interesting but many of them have useful applications as catalysts for industrial processes Zirconium based metallocenes for example are the most widely used catalysts for Ziegler-Natta polymerization of alkenes We 11 have more to say about them m Section 14 15... [Pg.610]

Hydroformylation (Section 17 5) An industrial process for prepanng aldehydes (RCH2CH2CH=0) by the reaction of terminal alkenes (RCH=CH2) with carbon monoxide Hydrogenation (Section 6 1) Addition of H2 to a multiple bond... [Pg.1286]

The reduction of acrylonitrile, CH2=CHCN, to adiponitrile, NC(CH2)4CN, is an important industrial process. A 0.594-g sample of acrylonitrile is placed in a 1 -L volumetric flask and diluted to volume. An exhaustive controlled-potential electrolysis of a 1.00-mL portion of the diluted acrylonitrile requires 1.080 C of charge. What is the value of n for this reduction ... [Pg.537]

The remarks of this and the last section are only a small fraction of what might be said about these important materials. We have commented on some aspects of the polymerization processes and of the polymers themselves that have a direct bearing on the concepts discussed here and elsewhere in this volume. This material provides an excellent example of the symbiosis between theoretical and application-oriented points of view. Each stimulates and reinforces the other with new challenges, although it must be conceded that many industrial processes reach a fairly high degree of empirical refinement before the conceptual basis is quantitatively developed. [Pg.309]

Air. Biofilters are an effective way of dealing with air from industrial processes that use halogenated solvents such chloromethane, dichioromethane, chloroethane, 1,2-dichloroethane and vinyl chloride, that support aerobic growth (26). Both compost-based dry systems and trickling filter wet systems are in use. Similar filters could be incorporated into pump-and-treat operations. [Pg.32]

With reduced sensor cost the range of appHcations now includes thermal vision (2,3) industrial processing, industrial security, poHce work (3), maritime safety, airline safety and vision enhancement for night driving and flying and weather sateUites. For these appHcations, the thermal sensor typically uses a broad spectral band to achieve highest sensitivity. [Pg.290]

Chemical Gas Detection. Spectral identification of gases in industrial processing and atmospheric contamination is becoming an important tool for process control and monitoring of air quaUty. The present optical method uses the ftir (Fourier transform infrared) interference spectrometer having high resolution (<1 cm ) capabiUty and excellent sensitivity (few ppb) with the use of cooled MCT (mercury—cadmium—teUuride) (2) detectors. [Pg.295]

A Procedurefor the Specijication, Calibration and Testing of Strain Gage Eoad Cells for Industrial Process Weighing and Force Measurement, Institute of Measurement and Control, London. [Pg.340]

Some industrial processes produce predorninately latent air conditioning loads. Others dictate very low humidities and when the dew point falls below 0°C, free2ing becomes a major concern. Dehydration equipment, using soHd sorbents such as siUca gel and activated alurnina, or Hquid sorbents such as lithium chloride brine and triethylene glycol, may be used. The process is exothermic and may require cooling the exiting air stream to meet space requirements. Heat is also required for reactivation of the sorbent material. [Pg.362]


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