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HDPE

Caused by its high crystallinity, high density polyethylene is the most rigid and least bendable amongst the different types of polyethylene. HDPE has hardly any side branches. Therefore, the density is always higher than 940 kg/m. The rigid and somewhat hard character is useful for a wide range of applications. [Pg.33]

This is the youngest of all the PE types. It looks similar to HDPE but has lower crystallinity due to a larger number of short chain branches. Therefore, it also has a lower density (normally lower than 940 kg/m ). However, PE with densities between 930 and 940 kg/m is often called MDPE or medium density polyethylene. [Pg.33]

LLDPE is used to make flexible as well as rigid products. LLDPE is often used in mixtures with one of the materials mentioned previously in order to make thiimer films. It is also used in packaging made up of multilayer films. LLDPE is very tough and keeps its shape. These properties are useful for the manufacture of larger objects like lids. [Pg.33]


Ffigh-density polyethylene (HDPE) Thermoplastic elastomers... [Pg.1011]

HDPE [OLEFIN POLYMERS - POLYETHYLENE - HIGH DENSITY POLYETHYLENE] (Vol 17)... [Pg.766]

Blends of PET and HDPE have been suggested to exploit the availabiUty of these clean recycled polymers. The blends could combine the inherent chemical resistance of HDPE with the processiag characteristics of PET. Siace the two polymers are mutually immiscible, about 5% compatihilizer must be added to the molten mixture (41). The properties of polymer blends containing 80—90% PET/20—10% HDPE have been reported (42). Use of 5—15% compatbiLizer produces polymers more suitable for extmsion blow mol ding than pure PET. [Pg.231]

The economics of recycling PET are more favorable than recycling HDPE. To iacrease the recycling of HDPE, the separation of bottles made of these two plastics could be omitted and a mixture processed. Coarse, light-colored powders of the two polymers have been prepared by an experimental soHd state shear extmsion pulverization process (55). The powder has been successfully injection molded without pelletization. [Pg.231]

Results obtained for two mixed plastics are summarized in Table 4. A balance exists between process temperature, plastics feed rate, and product yields (67). For example, lower temperatures increase wax formation due to incomplete depolymerization. Slower feed rates and increased residence times reduce wax formation and increase the yield of Hquids. The data summarized in Table 4 illustrate that the addition of PET to a HDPE PP PS mixture changes the performance of the Conrad process. Compared to the reference HDPE PP PS mixture, increased amounts of soHds ate formed. These are 95% terephthahc acid and 5% mono- and bis-hydroxyethyl esters. At higher temperatures, apparentiy enough water remains to promote decarboxylation. [Pg.232]

Price swings, particularly in the PET and HDPE markets have contributed to a retrenchment in the U.S. plastics recycling industry in 1995—1997... [Pg.233]

In 1994 in the U.S., recycled PET, HDPE, LDPE, and PS had a 16—46% cost advantage (4). This cost advantage largely disappeared by 1996. Bureau of Labor Statistics data indicate U.S. plastics prices in mid-1997 are seven percent below those of mid-1995 after being more than ten percent less in 1996... [Pg.233]

HDPE, high density polyethylene PP, polypropylene EVA, ethylene—vinyl alcohol SMC, sheet-molding compound ERP, fiber-reinforced plastic LDPE, low density polyethylene PE, polyethylene BMC, bulk mol ding compound TPE, thermoplastic elastomer. [Pg.369]

In the sheeting market, the low density polyethylenes are less important than the high density resins. The high density resins have excellent chemical resistance, stress-crack resistance, durabiUty, and low temperature properties which make them ideal for pond liners, waste treatment faciUties, and landfills. In thicker section, HMW-HDPE sheet makes good containers, trays, tmck-bed liners, disposable items, and concrete molds. The good durabiUty, abrasion resistance, and light weight are critical elements for its selection. [Pg.378]

There are three basic types of polyethylene foams of importance (/) extmded foams from low density polyethylene (LPDE) (2) foam products from high density polyethylene (HDPE) and (J) cross-linked polyethylene foams. Other polyolefin foams have an insignificant volume as compared to polyethylene foams and most of their uses are as resia extenders. [Pg.421]

Plastic materials represent less than 10% by weight of all packagiag materials. They have a value of over 7 biUion including composite flexible packagiag about half is for film and half for botties, jars, cups, tubs, and trays. The principal materials used are high density polyethylene (HDPE) for botties, low density polyethylene for film, polypropylene (PP) for film, and polyester for both botties and films. Plastic resias are manufactured by petrochemical companies, eg. Union Carbide and Mobil Chemical for low density polyethylene (LDPE), Solvay for high density polyethylene, Himont for polypropylene, and Shell and Eastman for polyester. [Pg.451]

Second, in the early 1950s, Hogan and Bank at Phillips Petroleum Company, discovered (3,4) that ethylene could be catalyticaHy polymerized into a sohd plastic under more moderate conditions at a pressure of 3—4 MPa (435—580 psi) and temperature of 70—100°C, with a catalyst containing chromium oxide supported on siUca (Phillips catalysts). PE resins prepared with these catalysts are linear, highly crystalline polymers of a much higher density of 0.960—0.970 g/cnr (as opposed to 0.920—0.930 g/cnf for LDPE). These resins, or HDPE, are currentiy produced on a large scale, (see Olefin polymers, HIGH DENSITY POLYETHYLENE). [Pg.367]


See other pages where HDPE is mentioned: [Pg.435]    [Pg.478]    [Pg.481]    [Pg.860]    [Pg.230]    [Pg.231]    [Pg.232]    [Pg.232]    [Pg.233]    [Pg.233]    [Pg.233]    [Pg.233]    [Pg.312]    [Pg.314]    [Pg.369]    [Pg.369]    [Pg.375]    [Pg.376]    [Pg.376]    [Pg.378]    [Pg.382]    [Pg.384]    [Pg.384]    [Pg.388]    [Pg.389]    [Pg.421]    [Pg.451]    [Pg.452]    [Pg.453]    [Pg.454]    [Pg.76]    [Pg.323]    [Pg.329]    [Pg.15]    [Pg.161]    [Pg.161]    [Pg.161]    [Pg.368]    [Pg.369]   


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Blend HDPE/PMMA

Blends of HDPE, LDPE, and VLDPE

Blow molding HDPE fuel tank

Blow-molded HDPE containers

Branching in HDPE

CNT/HDPE composites

Chain scissioning stabilized HDPE

Chemiluminescence-HDPE

Containers, HDPE

Coordination polymerization HDPE)

Crosslinked HDPE components

Dispersive mixing HDPE dispersed phase

EVA and HDPE examples of creep modulus (GPa) versus time (h) at room temperature under 3 MPa

Ethylene/1-butene copolymers HDPE)

Extrusion HDPE, deformation flow

Extrusion solid-state, HDPE

Flow diagram of an HDPE STR

Flow diagram of an HDPE loop

Fluorinated HDPE Containers for Other Applications

Fluorinated HDPE barrier container

Fluorination HDPE products

HDPE (See High-density polyethylene

HDPE (high-density

HDPE , production

HDPE Geomembranes with Textured Surface

HDPE Pipes

HDPE Recycling

HDPE UHMWPE examples of stress at yield retention () versus sub-zero temperatures (C)

HDPE crystals

HDPE examples of creep modulus (GPa) versus time (h) for various reinforcements

HDPE examples of stress at yield retention () versus temperature (C)

HDPE extrudates

HDPE for

HDPE injection molding

HDPE lamellae

HDPE manufacture

HDPE melt

HDPE melt, additives

HDPE products

HDPE properties

HDPE, additives

HDPE, additives Antioxidants

HDPE, additives Antistatic agents

HDPE, additives Carbon-blacks

HDPE, additives Fillers

HDPE, additives Peroxides

HDPE, additives Pigments

HDPE, additives Solvents

HDPE, additives Stabilisers

HDPE, additives Volatiles

HDPE, analysis

HDPE, recycled

HDPE-starch blends

HDPE/LDPE melt

HDPE/pristine

HDPE/propane

HDPEs

HMW-HDPE (

Half-life HDPE (

High Density Polyethylene - HDPE - Chapter

High density polyethylene, HDPE additives

High density polyethylene, HDPE composites

High density polyethylene, HDPE coordination polymerization

High density polyethylene, HDPE extrusion

High density polyethylene, HDPE general

High density polyethylene, HDPE nanocomposites

High density polyethylene, HDPE processing

High density polyethylene, HDPE solution process

High density polyethylenes HDPEs)

High molecular weight HDPE

High molecular weight HDPE plastic

High-Density Polyethylene (HDPE) Resins

High-density polyethylene (HDPE

Low molecular weight HDPE

Manufacture of HDPE

Metallocene HDPE

PE-HDPE

PET/HDPE

PONA HDPE degradation products

PP/HDPE

Pipe materials, HDPE

Plastic containers: HDPE

Plastics Beyond HDPE in Wood-Plastic Composite Materials

Polyethylene HDPE

Polyethylene HDPE, LDPE, LLDPE

Polymer HDPE

Polymers (cont HDPE products

Polyolefin HDPE)

Process overview HDPE

Recovery After Nanoindentation of HDPE

Recycling of HDPE

Separation of HDPE Base Cups from PET Beverage Bottles

Service Lifetime of HDPE Geomembranes

Standard Specification for Polyethylene Plastics Molding and Extrusion Materials from Recycled Postconsumer (HDPE) Sources

Surface fluorination HDPE products

Synthesis of HDPE

Technical parameters of HDPE

Tensile strength of HDPE

Thermal and Catalytic Degradation of Waste HDPE

UHMWPE/HDPE

UHMWPE/HDPE composites

Ultra-high molecular weight HDPE

Unival HDPE resins

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