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Industrial Polymerisation Processes

The oligomerisation of isobutene, with and without isomerisation or fragmentation, and its polymerisation and co-polymerisation are industrial processes of considerable... [Pg.46]

Some studies on the effect of antioxidants have been reported (54-57). Atmospheric oxygen inhibits the polymerisation of coatings etc. as an industrial process. This still awaits a satisfactory alternative to using an inert atmosphere. [Pg.23]

Electron transfer (ET) reactions play a key role in both natural (photosynthesis, metabolism) and industrial processes (photography, polymerisation, solar cells). The study of intermolecular photoinduced ET reactions in solution is complicated by diffusion. In fact, as soon as the latter is slower than the ET process, it is not anymore possible to measure km, the intrinsic ET rate constant, directly [1], One way to circumvent this problem, it is to work in a reacting solvent [2]. However, in this case, the relationship between the observed quenching rate constant and k T is not clear. Indeed, it has been suggested that several solvent molecules could act as efficient donors [3]. In this situation, the measured rate constant is the sum of the individual ksr-... [Pg.327]

What are the advantages of half-sandwich metallocene-based catalysts as compared with heterogeneous Ziegler-Natta catalysts in styrene polymerisation What are the possible consequences of this for developing industrial processes ... [Pg.273]

As regards the coordination homopolymerisation of heterounsaturated monomers, it does not play such an important role as in the case of heterocyclic monomers (with the exception of carbon monoxide). This is because of the high polymerisability of heterounsaturated monomers in the presence of ionic initiators which is taken into account in some industrial processes (e.g. polyformaldehyde). [Pg.426]

The key theme of this three day international conference is the role the PVC industry can play in creating a sustainable future. Papers are divided into nine sessions Strategic direction Challenges and markets PVC profiles Flexibles Polymerisation Sustainability Processing Stabilisers Additives... [Pg.81]

The industrial processes currently used worldwide for polyether polyol synthesis by anionic polymerisation of alkylene oxides are discontinuous processes, a fact that is explained by the great number of polyether polyol types produced in the same reactor and by the relatively low reaction rate of the propoxylation reaction. [Pg.119]

The phenolic lipids of Anacardieum occidentale have been commercially exploited (ref. 174) and those in Rhus vernicifera to a lesser extent. Most of the technical cashew nut shell liquid (CNSL) which results from industrial processing is and has been employed as a phenolic source for formaldehyde polymerisation the products from which in compounded form have been the basis for friction dusts widely used throughout the world in vehicle brake and clutch linings (ref.175). Urushiol has had use over many centuries in the art of Japanese lacquering (ref. 176) and in more recent years has been sometimes supplemented with CNSL. Chemical uses are referred to later. [Pg.520]

Four techniques are used in most industrial processes for the polymerisation of monomers to obtain corresponding polymers. These include (i) bulk or mass, (ii) solution, (iii) suspension and (iv) emulsion polymerisation techniques. However, other techniques such as interfadal, electrochemical and plasma polymerisation are also used to obtain different polymers, particularly in laboratory or low scale production. [Pg.14]

This process has many advantages, as thermal control is excellent in water and the viscosity of the medium remains low and constant. Each droplet of monomer is converted directly into a polymer bead. Provided that the size of the droplets is well controlled, polymer beads of defined size, e.g. in the range 10-1000 pm, are obtained at the end of conversion. This permits easy storage and feeding of moulding machines for transformation into objects. An example of an industrial process for suspension polymerisation is presented in Figure 3.9. [Pg.77]

There is an enormous range of industrial applications. For the main part, latexes are prepared by emulsion polymerisation. The process was developed industrially during the last World War as a way of replacing natural rubbers. Much fundamental and applied research has gone into this area. The relevant reaction mechanisms and physical processes have been quite well understood, although a few minor points of controversy are still discussed in the literature [6.4],... [Pg.188]

Inhibitors (such as 4-ferf-butylcatechol) (306) are usually added to monomers to be stored or transported to prevent premature thermal polymerisation. In precisely-controlled laboratory experiments, it is necessary to remove the inhibitor by distillation. However, industrial processes do not require the removal of inhibitor. Additional amounts of initiator are added to compensate for the presence of inhibitor. [Pg.11]

The polymerisation of light olefins is a very important industrial process because polyethylene and polypropylene have a large demand for a wide range of products. [Pg.173]

The industrial process (Figure 1) consists of a reactor (acting as the reboiler), a packed column, a total condenser and two distillate vessels. The polymer is manufactured through reversible linear polycondensation or step-growth polymerisation. The overall reaction can be characterised by the following scheme ... [Pg.636]

In redox initiation, the free radicals are generated as transient intermediates in the course of a redox reaction that involves an electron transfer process followed by scission to give a free radical. The features of redox initiation, that particularly lend themselves to industrial processes, are the general lack of any induction period before polymerisation begins and a relatively low energy of activation. The low energy of activation allows polymerisation to be carried out from, or at, low temperatures, and this facilitates reaction control of a very exothermic process. [Pg.141]

Ni(CO)4—the first metal carbonyl compound, discovered in 1890 [73]—and Fe(CO)5, which was discovered the following year, are the two most studied metal carbonyl compounds [74]. In particular, the photochemistry of Fe(CO)5 has been extensively studied due to its widespread use in industrial processes as a cheap and reactive compound utilised in a variety of applications, from polymerisation to metallurgy. Consequently, there has been great interest in the mechanisms of reactions, and especially the initial photochemical processes, occurring in Fe(CO)5 upon irradiation under ambient conditions [75]. Initially, such photochemical studies were only possible in low temperature matrices, in which reactive intermediates would be trapped and interrogated by infrared spectroscopy. Several key intermediates such as Fe(CO)4 and Fe(CO>3 have been identified. [Pg.127]

If we work back from solid polymer by adding progressively more amounts of liquid monomer, we see that the glass transition temperature of the now plasticised polymer decreases with the amount of monomer added. Monomer cannot diffuse through polymer below the glass transition temperature, so the reaction stops when the amount of monomer decreases by the amount necessary to raise the transition temperature of the mixture above the reaction temperature. However, the reaction will continue to proceed if the temperature of the reaction is raised, and will go to 100% conversion if the final temperature is above the transition temperature of the soHd polymer. For this reason, many industrial processes carry out the polymerisation using a temperature profile that finishes with a high temperature to ensure that there is no unreacted monomer left in the final product. [Pg.196]


See other pages where Industrial Polymerisation Processes is mentioned: [Pg.416]    [Pg.346]    [Pg.397]    [Pg.269]    [Pg.5]    [Pg.5]    [Pg.29]    [Pg.32]    [Pg.55]    [Pg.59]    [Pg.61]    [Pg.65]    [Pg.213]    [Pg.537]    [Pg.538]    [Pg.539]    [Pg.358]    [Pg.4]    [Pg.154]    [Pg.2520]    [Pg.262]    [Pg.136]    [Pg.39]    [Pg.246]    [Pg.47]    [Pg.103]    [Pg.704]   
See also in sourсe #XX -- [ Pg.214 ]




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Industrial polymerisation processe

Industrial polymerisation processe

Polymerisation products, industrial processes

Processive polymerisation

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