Vinyl chloride grades

Polymerization-grade vinyl chloride should not contain more than the amounts of impurities Hsted in Table 6 (145). 

Table 6. Typical Impurity Levels in Monomer Grade Vinyl Chloride ...

Latex Preparation Analysis. Deionized water was used for the aqueous phase in the polymerization and commercial grade vinyl chloride monomer (99.9% pure) was used without further purification. The emulsifier was a salt of a sulfated fatty alcohol, and the emulsifier solution for metering was prepared to have 0.15 mol/L in water. The initiator system was a water soluble redox system. 

Copolymer sample (grade) Vinyl chloride content in copolymer (%) ... 

Over 70% of the total volume of thermoplastics is accounted for by the commodity resins polyethylene, polypropylene, polystyrene, and poly(vinyl chloride) (PVC) (1) (see Olefin polymers Styrene plastics Vinyl polymers). They are made in a variety of grades and because of their low cost are the first choice for a variety of appHcations. Next in performance and in cost are acryhcs, ceUulosics, and acrylonitrile—butadiene—styrene (ABS) terpolymers (see... 

Tile is based mainly on vinyl chloride and vinyl acetate copolymers. Some polypropylene tile systems have recendy been iatroduced. A petroleum resia is usually employed as an extender and processiag aid conventional vinyl plasticizers and stabilizers also are iacorporated. Reinforcing fibers and limestone constitute the remainder of the tile composition the fibers contribute hot strength for processiag and dimensional stabiHty ia the finished tile, limestone suppHes bulk at an economical cost. Stable pigments are also iacorporated. Siace tile is iastalled oa and below grade level, it is important that the finished product be resistant to the effects of moisture and alkaH. 

Dichloroethane, an important intermediate for vinyl chloride production, is produced by catalytic chlorination of ethylene in either vapor or Hquid phase or by oxychlorination of ethylene. Thermal dehydrochlorination of 1,2-dichloroethane produces vinyl chloride and coproduct hydrogen chloride. Hydrogen chloride is commonly recycled to an oxychlorination unit to produce 1,2-dichloroethane or is processed into sales-grade anhydrous or aqueous hydrogen chloride. 

This chapter has so far dealt with the major fields of use of vinyl chloride polymers, namely plasticised PVC homopolymer, unplasticised PVC, including impact-modified grades, and copolymers particular based on vinyl acetate. There are, however, five particular special forms of vinyl chloride polymer which merit separate consideration, namely crystalline PVC, after-chlorinated PVC (often known as CPVC) and certain graft copolymers and two vinyl-chloride-based copolymers. 

Attempts to improve the heat deformation resistance of PVC by chlorination or by manufacture of more crystalline grades (see Sections 12.9.1 auid 12.9.2) results in a need for much higher processing temperatures and thus reduced processing stability. There may also be a loss in clarity. By copolymerising vinyl chloride with a small amount of V-cyclohexylmaleimide the softening point can... 

The estimation of reactivity of polyhalomethanes in the reactions with the same monomer shows that the quantity of halogen atoms in a molecule is the most essential factor affecting the easiness of homolysis of even one C— Br bond in molecule, and the influence of the halogen nature (chlorine or bromine) is of less significance. For instance, the analysis of the data on relative kinetics of some polyhalomethanes reactions with vinyl chloride allows us to grade the studied polyhalomethanes according to their reactivity, as follows ... 

The first successful static firing of plastisol propellant took place late in 1950 as part of a broad program conducted by Atlantic Research Corp. to investigate and evaluate plastisol propellants and methods for their manufacture (16). Major attention was directed to poly (vinyl chloride), cellulose acetate, and nitrocellulose, although other polymers were tested for their suitability (17). Patent applications were filed for plastisol propellant compositions and manufacturing processes, based on poly(vinyl chloride) (PVC) (19) and on nitrocellulose (18). The commercial availability of dispersion grade PVC enabled work with this resin to advance rapidly. The balance of this paper is devoted to a discussion of PVC plastisol propellants and their manufacture. 

Extruder screws and the range of conditions available on a particular machine may be versatile enough for several materials and grades but if it is desired, say, to extrude polyamide 6.6 or an unplasticized poly(vinyl chloride) more consistent and satisfactory results can be obtained by fitting a dedicated screw designed specially for the material concerned. For polyamide 6.6, for example, the unit should be capable of generating higher temperatures than are needed for an amorphous thermoplastic. 

The majority of PVC is produced by free-radical suspension polymerization of vinyl chloride. PVC is available in a number of grades and forms rigid or flexible resins. A flexible resin is obtained by incorporating plasticizers into the resins. 

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