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Polyethylene rate

Razumovskii and his colleagues appear not to have been aware of the work of Priest et al. and prefer to interpret their own results as supporting a mechanism that involves attack of ozone on the CH,—CH, unit in polyethylene. Rate constants for the reaction have not been measured, and no assessment of the role of other oxidizing species has been made. However, it is presumed that a high-pressure ozonizer was used and that ozone was the active species. [Pg.669]

ABS Acrylonitrile-butadiene-styrene ET Energy transfer HMWPE High molecular weight polyethylene LLDPE Linear low-desnity polyethylene VHMWPE Very high molecular weight polyethylene Ratings listed and numbered in order of performance ... [Pg.163]

Crystallization rate coefficient Crystallization rate parameter Dibenzylidene sorbitol Total volume of growing crystals Radial crystallization rate Preexponential factor in growth rate High density polyethylene Rate of nucleation Avrami constant... [Pg.244]

Atactic polypropylene Number of branches per molecule Branched polyethylene Chlorinated polyethylene Rate of volatilization Differential thermal analysis Ethylene-propylene copolymer Ethylene-propylene-diene copolymer... [Pg.465]

Ziegler found that adding certain metals or their compounds to the reaction mixture led to the formation of ethylene oligomers with 6-18 carbons but others promoted the for matron of very long carbon chains giving polyethylene Both were major discoveries The 6-18 carbon ethylene oligomers constitute a class of industrial organic chemicals known as linear a olefins that are produced at a rate of 3 X 10 pounds/year m the... [Pg.610]

Figure 2.5 Shearing force per unit area versus shear rate. The experimental points are measured for polyethylene, and the labeled lines are drawn according to the relationship indicated. (Data from J. M. McKelvey, Polymer Processing, Wiley, New York, 1962.)... Figure 2.5 Shearing force per unit area versus shear rate. The experimental points are measured for polyethylene, and the labeled lines are drawn according to the relationship indicated. (Data from J. M. McKelvey, Polymer Processing, Wiley, New York, 1962.)...
Solution polyacrylamides can also be prepared at high polymer soHds by radiation processes (80,81). Polyacrylamides with molecular weights up to 20 million can be prepared by inradiation of acrylamide and comonomers in a polyethylene bag with cobalt-60 gamma radiation at dose rates of 120-200 J/kg-h. The total dose of radiation is controlled to avoid cross-linking. [Pg.142]

The spring ensures a soHd closing action and is usually wound from stainless steel wire. The dip tube conducts the product from the container to the valve. It is usually extmded from polyethylene or polypropylene and has an inside diameter of over 2.54 mm, although it can be provided in capillary sizes having diameters down to 0.25 mm. These small tubes are used to reduce flow rate and may function in place of the Hquid metering orifice in the valve housing. [Pg.350]

The film tube is collapsed within a V-shaped frame of rollers and is nipped at the end of the frame to trap the air within the bubble. The nip roUs also draw the film away from the die. The draw rate is controlled to balance the physical properties with the transverse properties achieved by the blow draw ratio. The tube may be wound as such or may be sHt and wound as a single-film layer onto one or more roUs. The tube may also be direcdy processed into bags. The blown film method is used principally to produce polyethylene film. It has occasionally been used for polypropylene, poly(ethylene terephthalate), vinyls, nylon, and other polymers. [Pg.380]

The limiting oxygen index of Tefzel as measured by the candle test (ASTM D2863) is 30%. Tefzel is rated 94 V-0 by Underwriters Laboratories, Inc., in their burning test classification for polymeric materials. As a fuel, it has a comparatively low rating. Its heat of combustion is 13.7 MJ/kg (32,500 kcal/kg) compared to 14.9 MJ /kg (35,000 kcal/kg) for poly(vinyHdene fluoride) and 46.5 MJ /kg (110,000 kcal/kg) for polyethylene. [Pg.370]

Many initiators attack steels of the AISI 4300 series and the barrels of the intensifiers, which are usually of compound constmction to resist fatigue, have an inner liner of AISI 410 or austenitic stainless steel. The associated small bore pipework and fittings used to transfer the initiator to the sparger are usually made of cold worked austenitic stainless steel. The required pumping capacity varies considerably from one process to another, but an initiator flow rate 0.5 L / min is more than sufficient to supply a single injection point in a reactor nominally rated for 40 t/d of polyethylene. [Pg.99]

Cross-linked polyethylene-based compounds that contain dame-retardant components and compounds based on PVC cross-linked by radiation have also received high temperature rating. They find use not only in appHance wires but also in manufacturing under-the-hood automotive wires. [Pg.323]

R. B. Blodgett, "Ethylene—Propylene Rubber and Crosslinked Polyethylene as Insulations for 90°C Rated Medium Voltage Cables," Rubber Chem. Technol, 52, 410-424 (1978). [Pg.330]

AppHcation of an adhesion-promoting paint before metal spraying improves the coating. Color-coded paints, which indicate compatibiHty with specific plastics, can be appHed at 20 times the rate of grit blasting, typically at 0.025-mm dry film thickness. The main test and control method is cross-hatch adhesion. Among the most common plastics coated with such paints are polycarbonate, poly(phenylene ether), polystyrene, ABS, poly(vinyl chloride), polyethylene, polyester, and polyetherimide. [Pg.134]

The introduction of metallocene and single-site polyethylene catalyst systems may eventually change the demand for higher olefins used as comonomers. Some sources indicate that their use will increase the demand for comonomers, but others feel that they will reduce comonomer use. At any rate, it is not expected that their introduction will have a significant effect on comonomer growth rates for the period 1992—1996 (see Olefin polymers). [Pg.441]

Fig. 6. Melt viscosity dependence on shear rate for various polymers A, low density polyethylene at 210°C B, polystyrene at 200°C C, UDEL P-1700 polysulfone at 360°C D, LEXAN 104 polycarbonate at 315°C and E, RADEL A-300 polyethersulfone at 380°C. Fig. 6. Melt viscosity dependence on shear rate for various polymers A, low density polyethylene at 210°C B, polystyrene at 200°C C, UDEL P-1700 polysulfone at 360°C D, LEXAN 104 polycarbonate at 315°C and E, RADEL A-300 polyethersulfone at 380°C.
Fig. 14. Shear viscosity, Tj, and extensional viscosity, Tj as a function of deformation rate of a low density polyethylene (LDPE) at 150°C (111). To convert... Fig. 14. Shear viscosity, Tj, and extensional viscosity, Tj as a function of deformation rate of a low density polyethylene (LDPE) at 150°C (111). To convert...
Fig. 22. Shear viscosity Tj and first normal stress difference (7) vs shear rate 7 for a low density polyethylene at 150°C (149), where (Q) — parallel plate ... Fig. 22. Shear viscosity Tj and first normal stress difference (7) vs shear rate 7 for a low density polyethylene at 150°C (149), where (Q) — parallel plate ...
Meta.1 Oxides. Halogen-containing elastomers such as polychloropreae and chlorosulfonated polyethylene are cross-linked by their reaction with metal oxides, typically ziac oxide. The metal oxide reacts with halogen groups ia the polymer to produce an active iatermediate which then reacts further to produce carbon—carbon cross-links. Ziac chloride is Hberated as a by-product and it serves as an autocatalyst for this reaction. Magnesium oxide is typically used with ZnCl to control the cure rate and minimize premature cross-linking (scorch). [Pg.236]

Types of air strippers include packed towers, tray towers, and spray towers. Packed towers are packed or filled with small forms made of polyethylene [9002-88-4] stainless steel, poly(vinyl chloride) (PVC) [9002-86-2] or ceramic that provide large surface area to volume ratios which increase transfer rates into the air stream. Packed towers operate in countercurrent mode, that is, the aqueous stream enters at the top of the tower while air is blown in from the bottom. An example of this type of unit is shown in Figure 1. Channeling or short circuiting of the aqueous stream is minimized by... [Pg.159]


See other pages where Polyethylene rate is mentioned: [Pg.267]    [Pg.69]    [Pg.387]    [Pg.548]    [Pg.208]    [Pg.476]    [Pg.329]    [Pg.412]    [Pg.408]    [Pg.441]    [Pg.191]    [Pg.194]    [Pg.451]    [Pg.150]    [Pg.150]    [Pg.151]    [Pg.210]    [Pg.296]    [Pg.468]    [Pg.520]    [Pg.528]    [Pg.228]    [Pg.506]    [Pg.348]   


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High-density polyethylene melt flow rate

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Polyethylene face growth rate

Polyethylene growth rate against temperatur

Polyethylene operating rates

Polyethylene oxide) nucleation rate

Polyethylene polymerisation rate

Polyethylene reaction rate

Polyethylene spherulite growth rates

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