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Low-density polyethylenes. See Polyethylene

OLEFIN POLYTffiRS - POLYETHYLENE - LINEAR LOW DENSITY POLYETHYLENE] (Vol 17) LLDPE. See Linear low density polyethylene. [Pg.576]

The majority of spunbonded fabrics are based on isotactic polypropylene and polyester (Table 1). Small quantities are made from nylon-6,6 and a growing percentage from high density polyethylene. Table 3 illustrates the basic characteristics of fibers made from different base polymers. Although some interest has been seen in the use of linear low density polyethylene (LLDPE) as a base polymer, largely because of potential increases in the softness of the final fabric (9), economic factors continue to favor polypropylene (see OlefinPOLYMERS, POLYPROPYLENE). [Pg.163]

An independent development of a high pressure polymerization technology has led to the use of molten polymer as a medium for catalytic ethylene polymerization. Some reactors previously used for free-radical ethylene polymerization at a high pressure (see Olefin polymers, low density polyethylene) have been converted to accommodate catalytic polymerization, both stirred-tank and tubular autoclaves operating at 30—200 MPa (4,500—30,000 psig) and 170—350°C (57,83,84). CdF Chimie uses a three-zone high pressure autoclave at zone temperatures of 215, 250, and 260°C (85). Residence times in all these reactors are short, typically less than one minute. [Pg.387]

AH higher a-olefins, in the presence of Ziegler-Natta catalysts, can easily copolymerise both with other a-olefins and with ethylene (51,59). In these reactions, higher a-olefins are all less reactive than ethylene and propylene (41). Their reactivities in the copolymerisation reactions depend on the sise and the branching degree of their alkyl groups (51) (see Olefin polya rs, linear low density polyethylene). [Pg.430]

Fig. 5. Solubility coefficient at 30°C versus boiling point of ester in a low density polyethylene film (18). For unit conversion see equation 6. Fig. 5. Solubility coefficient at 30°C versus boiling point of ester in a low density polyethylene film (18). For unit conversion see equation 6.
The cooling requirements will be discussed further in Section 8.2.6. What is particularly noteworthy is the considerable difference in heating requirements between polymers. For example, the data in Table 8.1 assume similar melt temperatures for polystyrene and low-density polyethylene, yet the heat requirement per cm is only 295 J for polystyrene but 543 J for LDPE. It is also noteworthy that in spite of their high processing temperatures the heat requirements per unit volume for FEP (see Chapter 13) and polyethersulphone are, on the data supplied, the lowest for the polymers listed. [Pg.161]

Metallocene-catalysed very low density polyethylene (m-VLDPE) has become available with densities of as low as 0.903. This is of use for sealing layers of multi-layer films since sealing can commence at lower temperatures than with conventional materials such as LLDPE and EVA (see Section 11.6) with the polymer seal exhibiting both cold strength and hot tack strength. [Pg.228]

Note that, apart from the filler particle shape and size, the molecular mass of the base polymer may also have a marked effect on the viscosity of molten composites [182,183]. The higher the MM of the matrix the less apparent are the variations of relative viscosity with varying filler content. In Fig. 2, borrowed from [183], one can see that the effect of the matrix MM on the viscosity of filled systems decreases with the increasing filler activity. In the quoted reference it has also been shown that the lg r 0 — lg (MM)W relationships for filled and unfilled systems may intersect. The more branches the polymer has, the stronger is the filler effect on its viscosity. The data for filled high- (HDPE) and low-density polyethylene (LDPE) [164,182] may serve as an example the decrease of the molecular mass of LDPE causes a more rapid increase of the relative viscosity of filled systems than in case of HDPE. When the values (MM)W and (MM)W (MM) 1 are close, the increased degree of branching results in increase of the relative viscosity of filled system [184]. [Pg.26]

LDPE. See low density polyethylene (LDPE) leaf springs 146 ... [Pg.685]

LLDPE. See linear low density polyethylene (LLDPE) load-bearing products 139 ... [Pg.685]

LDL receptor (LDLR), 5.T89 L-DOPA, 2 560, 606 LDPE copolymers, 20 213-214. See also Low density polyethylene (LDPE) LDPE film, gels in, 20 229-230 LDPE homopolymer, 20 212 LDPE ionomers, 20 214 LDPE polymerization, peroxide initiators for, 20 218t... [Pg.513]

Linear combination of atomic orbitals (LCAO) method, 16 736 Linear condensation, in silanol polycondensation, 22 557-558 Linear congruential generator (LCG), 26 1002-1003 Linear copolymers, 7 610t Linear density, 19 742 of fibers, 11 166, 182 Linear dielectrics, 11 91 Linear elastic fracture mechanics (LEFM), 1 509-510 16 184 20 350 Linear ethoxylates, 23 537 Linear ethylene copolymers, 20 179-180 Linear-flow reactor (LFR) polymerization process, 23 394, 395, 396 Linear free energy relationship (LFER) methods, 16 753, 754 Linear higher a-olefins, 20 429 Linear internal olefins (LIOs), 17 724 Linear ion traps, 15 662 Linear kinetics, 9 612 Linear low density polyethylene (LLDPE), 10 596 17 724-725 20 179-211 24 267, 268. See also LLDPE entries a-olefin content in, 20 185-186 analytical and test methods for,... [Pg.523]

Liquid-liquid solvent extraction, 21 399 Liquid lithium, 15 131 Liquid low density polyethylene, 20 205 Liquid lubricants, for extreme environments, 15 256 Liquid lubricated system, coefficient of friction in, 15 209 Liquid magnesium, 15 336 Liquid manometers, 20 646-647 Liquid MDI, 25 462. See also MDI [4,4 -methylenebis(phenyl isocyanate)] Liquid melamine resins, 15 773 Liquid membrane extraction, 10 766 Liquid membranes, 15 800, 814-815 supported, 16 28... [Pg.528]

Molecular orbitals, in organic semiconductors, 22 211 Molecular orbital theory, 16 737 Molecular orientation, in linear low density polyethylene, 20 188-189 Molecular oxygen, 17 746. See also Oxygen (0)... [Pg.596]

Molecular solutions, 8 697 Molecular speciation/quantification, infrared spectroscopy in, 23 140 Molecular spectroscopy, 10 508 Molecular structure. See also Chemical structures Molecular formulas of linear low density polyethylene, 20 182-184... [Pg.597]

Rheological properties, See also Rheology of dry foams, 12 16 of embedding materials, 10 10 of encapsulants, 10 12-13 of linear low density polyethylene,... [Pg.806]

Rotational molding, of linear low density polyethylene, 20 200. See also Rotomolding... [Pg.811]


See other pages where Low-density polyethylenes. See Polyethylene is mentioned: [Pg.338]    [Pg.64]    [Pg.205]    [Pg.555]    [Pg.1060]    [Pg.312]    [Pg.76]    [Pg.329]    [Pg.367]    [Pg.371]    [Pg.432]    [Pg.434]    [Pg.82]    [Pg.327]    [Pg.222]    [Pg.210]    [Pg.740]    [Pg.208]    [Pg.247]    [Pg.616]    [Pg.1050]    [Pg.172]    [Pg.377]    [Pg.367]    [Pg.133]    [Pg.532]    [Pg.534]    [Pg.730]   


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LDPE (See Low-density polyethylene

LLDPE (See Linear low-density polyethylene

Linear low-density polyethylenes. See

Low-density polyethylene

Low-density polyethylenes. See

Low-density polyethylenes. See

Polyethylene density

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