Multi industrial processes

The Crignard reactant having a long alkyl chain was added to a keto compound the substituents remain undisclosed [134]. Thereby, an enolate is formed which is further reacted in the framework of a multi-stage fine-chemical industrial process. 

Industrial and applied multi-step reaction processes, where oxidizing enzymes are components of industrial processes, include in the pulp and paper industry, in the food and beverage industry, for bioremediation, in biosensors and, more recently, in biofuel cells (discussed in more detail in Section 3.8). 

The volatility of difunctional isocyanates (such as tolylene diisocyanates, hexamethylene diisocyanate, etc.) creates many environmental problems in the urethane industry. These difficulties can be overcome by preparation of NCO-terminated oligomers with low vapor pressure. One approach is the preparation of NCO-ter-minated oligomers by partial cyclotrimerization of difunctional isocyanates. Usually this is achieved by a multi-step process which includes also deactivation of the catalyst at a certain conversion. During our work on cyclotrimerization of isocyanates we found that cyclic sulfonium zwitterions are very active cyclotrimerization catalysts (2). Recently we found that cyclic sulfonium zwitterions under certain reaction conditions act as anionic initiators. This behavior of cyclic sulfonium zwitterions permits preparation of isocyanate oligomers containing isocyanurate rings by a one-step procedure, eliminating the deactivation step. 

There is increasing interest in the study of multi-metallic systems for several reasons. They are potential catalysts in many industrial processes and, because of the common occurrence of multi-metallic species as active sites in many metalloenzymes, they may be used as models for these molecules. In addition, these complexes offer the possibility of studying multi-electron charge transfer and magnetic coupling phenomena. 

Formulation of multi-component emulsions and mixtures are of interest in chemical and industrial processes (Vilar, 2008 Vilar et al., 2008). Standard stirred tank reactors (STR) and oscillatory baffled reactors (OBR) are traditional methods for the formulation of liquid-liquid mixtures and liquid-solid emulsions. Compared with STR, oscillatory baffled reactors provide more homogeneous conditions and uniform mixing with a relatively lower shear rate (Gaidhani et al., 2005 Harrison and Mackley, 1992 Ni et al., 2000). Figure 17 is a sketch of a typical oscillatory baffled reactor. It consists of the reactor vessel, orifice plate baffles, and an oscillatory movement part. The orifice plate baffles play an important role in the OBR for the vertex generation in the flow vessels as well as the radial velocities of the emulsions and mixtures. They are equally spaced in the vessel with a free area in the center of each baffle... 

PET, on the other hand, is a radioactive modality of tomography. Examples of PET applications in industrial process include imaging of slurry mixtures in STR, dispersion of particle pulse in gas-solid fluidized beds, and visualization of multi-phase fluids through sudden expansions. Although such methods require sophisticated facilities, due to the nature of the radiation source, they provide accurate data for detailed model comparison which is of major benefit for industrial design and operation. 

Dimerisation of olefins is a major industrial process, and is carried out on a multi million ton scale annually.111 One of the most important methods is represented by the Shell Higher Olefin Process (SHOP), which can even be run under biphasic conditions. In the oligomerisation of ethylene, the catalyst is generated in situ in 1,4-butanediol from a nickel salt, Na[BH4] and a chelating ligand. The olefins formed in the reaction are immiscible with the polar solvent and are isolated by phase separation and subsequent distillation.[2]... 

It was not in Mittasch s character to be satisfied with this conspicuous achievement. Parallel to extensive studies on the influence of pressure, temperature, gas composition, catalyst poisons and other factors on the synthesis reaction, he worked toward new types of multi-component catalysts for a great number of other catalytic gas reactions. With his associates Ch. Beck, C. Muller, and Ch. Schneider, he thus discovered efficient catalysts for the water gas reaction, for hydrogenations in the gas phase (among which the synthesis of alcohols and hydrocarbons from carbon monoxide and hydrogen is particularly noteworthy), for the production of nitric acid via the oxidation of ammonia, and for many more industrial processes which are the backbone of large segments of our present chemical industry. 

The synthesis of oligomeric peralkylated polyaminophosphazenes based upon the P3 and P4 templates is an elegant (but complicated), hazardous, and expensive multi-step process. To exploit catalysts of this type in silicone synthesis on an industrial scale would require a much simplified and lower-cost synthetic protocol. One of the simplest and lowest-cost routes to a conjugated -P=N- template that forms the framework for the synthesis of phosphazene base materials is via phosphonitrilic chloride oligomers (Fig. 3). These are well-known acidic catalysts used in the silicone industry for the condensation polymerization of silanol-terminated polydimethylsiloxanes. Catalysts of this type are most commonly prepared by the reaction of PCI5 with NH4CI or HMDZ,... 

Several multi-ton industrial processes still use enzymatic resolution, often with lipases that tolerate different substrates. BASF, for example, makes a range of chiral amines by acylating racemic amines with proprietary esters. Only one enantiomer is acylated to an amide, which can be readily separated from the unreacted amine. Many fine chemicals producers also employ acylases and amidases to resolve chiral amino acids on a large scale. l-Acylases, for example, can resolve acyl d,l-amino acids by producing the I-amino acids and leaving the N-acyl-l-amino acid untouched after separation, the latter can be racemized and returned to the reaction. d-Acylase forms the alternative product. Likewise, DSM and others have an amidase process that works on the same principle d,l-amino acid amides are selectively hydrolyzed, and the remaining d-amino acid amide can be either racemized or chemically hydrolyzed. 

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