Polyethylene price

Little is known of the market for acetyl chloride. The production and sales are beUeved to be small, but may have potential for very large scale-up. The total U.S. market may amount to only 500 t annually. Acetyl chloride must be shipped in polyethylene-lined dmms having capacities of only 220 L it must be labeled as a corrosive substance. Acetyl chloride generated captively from purchased raw materials probably has a unit value of no more than 0.92—0.95/kg. Shipping costs and other factors set the price at about 3/kg for the commercial trade. 

Table 6 shows the sales estimates for principal film and sheet products for the year 1990 (14). Low density polyethylene films dominate the market in volume, followed by polystyrene and the vinyls. High density polyethylene, poly(ethylene terephthalate), and polypropylene are close in market share and complete the primary products. A number of specialty resins are used to produce 25,000—100,000 t of film or sheet, and then there are a large number of high priced, high performance materials that serve niche markets. The original clear film product, ceUophane, has faUen to about 25,000 t in the United States, with only one domestic producer. Table 7 Hsts some of the principal film and sheet material manufacturers in the United States.

The 1993 price of high purity anhydrous nickel difluoride was 0.55 /g in 100- or 250-g quantities. Small quantities are stored and shipped in polyethylene bottles, whereas large amounts are shipped in fiber board dmms with polyethylene liners. 

The total U.S. consumption of H2TiFg is 20 t/yr. The 1993 price varied between 2.80 to 7.50/kg depending on quantity and specifications. It is packaged in DOT approved polyethylene-lined dmms and the salts in polyethylene-lined fiber board dmms. 

Economics. Rigid foam systems are typically in the range of 32 kg/m (2 Ibs/fT) and, in 1992, had a foam price of about 3.63/kg ( 1.65 per lb) with hquid foam systems at about 2.75/kg. Unit prices for pour-ia-place polyurethane packaging systems fall between the competitive expandable polystyrene bead foam at 3.30/kg and low density polyethylene foams at 5.80/kg. 

The Hst price of 35 kg/m polyethylene foam boards is about 0.58/BE ( 6.90/kg) and that of cross-linked polyethylene foam is about 0.33 to 0.88/kg more expensive than uncross-linked polyethylene foam depending on the density and thickness of the foam. 

Flexographic Inks. Fluorescent toners such as the Radiant GF, Lawter HVT, and Day-Glo HM and HMS Series toners are used in flexographic ink formulations. These products are soluble in blends of alcohol (80%) and ester solvents (20%) and are compatible with modifying materials such as nitroceUulose resins and acryHc solution polymers. Flexographic inks of this type are used most commonly to print products such as ceUophane and polyethylene film for packaging, and also to print paper products such as gift wrap and price labels. 

Sodium borobydride is available as a 12% solution in caustic soda and in soHd form either as powder or pellets (3). The predominant form produced is the solution, the DOT shipping classification for which is corrosive Hquid. Forms of packaging are 18.9-L pails, 208.2-L dmms, and either tank tmck or tank car for bulk shipments. 1991 pricing for the solution form was 40.34/kg of borobydride contained. SoHd sodium borobydride, a white powder packaged in polyethylene bags in metal containers, was priced at 48.39/kg. 

Use the information given in Table 2.1 (Prices of Materials) and in Table 2.4 (Energy Content of Materials) to calculate the approximate cost of (a) aluminium, (b) low-density polyethylene, (c) mild steel and (d) cement in 2004, assuming that oil increases in price by a factor of 1.6 and that labour and other manufacturing costs increase by a factor of 1.3 between 1994 and 2004. 

At the time of writing photodegradants are in an early stage of development and have not yet been fully evaluated. It is a moot point whether or not manufacturers will put such materials into polymer compounds and thus increase the price about 5% without legal necessity. However, if such legislation, considered socially desirable by many, took place one might expect polyethylene... 

There have been some attempts to develop chlorinated polyethylene elastomers. The rubbers possess such attractive properties as very good oil, heat, flame, ozone, and weathering resistance and are also available in a convenient powder form. In spite of being marketed at competitive prices, the chlorinated polyethylene rubbers (designated as CM rubbers by ASTM) took... 

The nylons have found steadily increasing application as plastics materials for speciality purposes where their toughness, rigidity, abrasion resistance, good hydrocarbon resistance and reasonable heat resistance are important. Because of their high cost they have not become general purpose materials such as polyethylene and polystyrene, which are about a third of the price of the nylons. 

A manufacturer considering using a thermoplastic elastomer would probably first consider one of the thermoplastic polyolefin rubbers or TPOs, since these tend to have the lowest raw polymer price. These are mainly based on blends of polypropylene and an ethylene-propylene rubber (either EPM or EPDM) although some of the polypropylene may be replaeed by polyethylene. A wide range of blends are possible which may also contain some filler, oil and flame retardant in addition to the polymers. The blends are usually subject to dynamic vulcanisation as described in Section 11.9.1. 

Specialty waxes include polar waxes for more polar adhesive systems. Examples would be castor wax (triglyceride of 12-hydroxy stearic acid) or Paracin wax N- 2 hydroxy ethyl)-12-hydroxy stearamide) which are used in polyester, polyamide, or with high VA EVA copolymer-based systems. Other common polar waxes are maleated polyethylenes, which are used to improve the specific adhesion of polyethylene-based adhesives, and low molecular weight ethylene copolymers with vinyl acetate or acrylic acid, which are used to improve low temperature adhesion. High melting point isotactic polypropylene wax (7 155°C) and highly refined paraffin wax (7,n 83°C) are used where maximum heat resistance is critical. Needless to say, these specialty waxes also command a premium price, ranging from 2 to 5 times that of conventional paraffin wax. 

Metallocene-based polyethylene does not offer the lower production costs associated with LLDPE. Hence there will be a price premium for the new materials but this is felt to be justified in view of their improved property profile. 

Anhydrous HF was first produced commercially in the USA in 1931 and in the UK from about 1942. By 1992 some eighteen countries were each producing at least 3000 tonnes pa with North America accounting for some 330000 tonnes of the estimated annual world production of about 875 000 tormes, A further 205 000 tonnes was used captively for production of AIF3. Price in 1990 was about l.50/kg for the anhydrous acid and somewhat less for 70% acid. The primary suppliers ship HF in tank-cars of 20-91-tonne capacity and the product is also repackaged in steel cylinders holding 8.0-900 kg (2.7-635 kg in the UK). Lecture bottles contain 340 g HF. The 70% acid is shipped in tank-cars of 32-80-tonne capacity, tank trucks of 20-tonne capacity, and in polyethylene-lined drums holding 114 or 208 I,... 

In the field of plastics, the annual production of polyvinylchloride (PVC) is second only to polyethylene. PVC has long been used in various areas, ranging from agriculture and industry to medical equipment and daily life, due to its well-developed production techniques, easy processing, and low price. However, PVC has its own disadvantages, mainly its low stability toward heat and ultraviolet (UV) light. Also, pure PVC is a very hard material that cannot be easily processed and practically used. Common PVC plastics contain various amounts of plasticizers and other additives, including modifiers, stabilizers, and lubricants. 

An example of the way in which process competition works in the manufacture of plastics is the story of acrylonitrile. The first process for the production of this plastic was based upon the reaction between hydrogen cyanide and acetylene, both hard to handle, poisonous, and explosive chemicals. The raw material costs were relatively low as compared to materials for other monomers, but the plant investment and manufacturing costs were too high. As a result, originally acrylonitrile monomer (1950s) sold for about 30 cents per pound and the future of the material looked dim as other plastics such as polyethylene became available at much lower prices due to their lower production costs. 

Inexpensive plastic dishes can be placed under reagent bottles. There should be beakers beneath burets when they are not in use. Some laboratories cover their reagent shelves with thin sheets of ribbed polyethylene, w hich is available in rolls at a reasonable price. 

Propylene, a light olefin, is like ethylene one of the most important feedstocks for the petrochemical industry. In recent years the main way to obtain propylene and ethylene has been via cracking of naphtha. For this reason the cost of the corresponding polymers, mainly polypropylene and polyethylene, depends on the international oil price. One big challenge for modem chemistry is to look for an alternative production of feedstocks that is independent of the oil-industry. 

PET/HDPE blends, 21 452. See also High density polyethylene (HDPE) Poly(ethylene terephthalate) (PET) Petite yeasts, 26 451 Petitgrain oils, in perfumes, 18 370 PET molding resins, 20 56-57 current prices for, 20 59t properties of, 20 59t uses for, 20 57 PETN, 10 734-735. See also... 

For the global advanced composites market, the average cost of high-performance fibre reinforcements (carbon, aramid, high modulus polyethylene, boron, R/S/T-glass and some E-glass) is estimated from 5.5 to 6 per kg. This moderate price is due to the decrease in the carbon fibre price. Some grades could fall to less than 10/kg in the short or medium term. 

The properties are close to those of polyethylenes, with some differences due to the tertiary carbon linked to the backbone good mechanical properties at ambient temperature, low price, attractive price/property ratios, easy processing, chemical inertness, we absorption of water, low density, good electrical insulation even in wet media, feasibility of welding, versatility of processing methods, broad range of available melt flow rates (MFR). 

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