Ethylene world capacity

Production. MTBE production capacity has grown steadily, usually at an annual rate of 10 to 20% per year. In 1980, world capacity was 30 thousand barrels per day (1.5 X 10 t/yr). By 1990, capacity was up to 180 thousand barrels per day (7 x 10 t/yr). Because of the requirements of the U.S. CAA, production capacity is expected to more than double from 1990 to 1995 (25). By 2000, MTBE may be the second largest organic chemical produced in the United States, second only to ethylene (26). 

In 1989, world capacity for the production of ethylene was approximately 58 x 10 t. The United States production capacity accounted for almost 30% of the world capacity, or approximately 17 x 10 t, followed by Western Europe with almost 26% or 15 x 10 t (116). 

United States production of ethylene oxide in 1990 was 2.86 x 10 metric tons. Approximately 16% of the United States ethylene (qv) production is consumed in ethylene oxidation, making ethylene oxide the second largest derivative of ethylene, surpassed only by polyethylene (see Olefin polymers). World ethylene oxide capacity is estimated by country in Table 11. Total world capacity in 1992 was ca 9.6 x 10 metric tons. 

Ethylene oxide synthesis is one of the largest-volume industrial processes with a produchon rate of some plants of several 100 0001 a (see original citahons in [4]). In 1995, the world capacity for ethylene oxide was approximately 11 200 0001 a. As industrial catalyst silver on alumina is employed. In addihon to large produc-... 

The production of ethylene by gas crackers, mostly from C2, C3, and some C4 feeds, amounts to about 40% of the world ethylene capacity. This results in a small coproduction of benzene compared to benzene co-produced in naphtha and gas oil crackers, which account for 60% of the world s ethylene production capacity. A typical overall benzene yield from ethane cracking is on the order of only 0.6% of the ethane feed, and the yield of benzene from propane cracking is on the order of 3% of the propane feed. In contrast, the... 

The world ethylene production capacity is approximately 120 million tonnes (2008). The regional break-up is shown in Figure 1.1. 

Russia has an annual nameplate ethylene production capacity of 3.49 million tonnes. The plants are scattered across Russia from European Russia to the Far East (Table 1.4). By world standards most plants are small with capacities of 400 kt/y or less. A cross section of feedstocks is used. 

With the permission of the author [3], we borrow here data (Table 1) which indicates the production capacity of the major industrial processes using oxygen for functionalizing hydrocarbons. The production of acetic acid should be added to the list, although 60% of its 6.1 million t/year total world capacity (to reach 67% in the next future) is due to the Monsanto process (methanol carbonylation) [4]. Only the rest (2.4 million t/year) is produced by oxidation of butane or other alkanes or acetaldehyde or, for a small proportion, hy the Showa Denko process (oxidation of ethylene). 

The first group consists of amorphous thermoplastic engineering polymers. These are cyclic olefin polymers (COP) or cyclic olefin copolymers (COC) with ethylene. They were commercialized, for example, as Zeonex (in 1991) and Zeonar (by Zeon), as Topas (Polyplastics), Apel (Mitsui), and Alton (JSR). Topas was originally part of Ticona, before it was sold to Daicel in 2005. A Topas plant with a capacity of 30,000 tpa started up in Oberhausen, Germany, in September 2000. Until that time, world capacity from 4 pilot-scale plants was around 10,000 tpa. 

A comparison was made in the Table III in terms of ethylene production capacity of the top 10 ethylene producing companies, respectively in the world and in Japan. 

Combined 1993 production figures for pure terephthalic acid and dimethyl terephthalate were about 3 5 Mt in the U.S.A., 2Mt in western Europe and l-5Mt in Japan. Over 95% is converted to polyethylene terephthalate by reaction with ethylene glycol. While fibre production remains the largest use, the major area of activity is the production of PET bottle resins, with world capacity scheduled to grow rapidly (presently over 2 Mt per annum, of which 0 9 Mt per annum is in the U.S.A.). 

Figure 6.12.4 shows the ten largest ethylene oxide producers in the world. The largest producer Dow Chemicals (including Union Carbide Corporation) accounts for 16% of the world capacity, followed by SABIC (10%), Shell (7%), and BASF (6%). 

Direct oxidation of propylene with air or pure oxygen (equivalent to ethylene oxide manufacturing) is not efficient, since the silver catalysts used in the direct ethylene oxidation are not suitable for the reaction of alkenes with allylic hydrogen atoms (like propylene). Direct oxidation of propylene results mainly in acrolein formation and total oxidation. Some 3% of the world capacity of PO is produced by very recently developed processes, for example, hydroperoxidation of cumene and propylene and catalytic epoxidation of propylene using H2O2. 

Acetaldehyde, first used extensively during World War I as a starting material for making acetone [67-64-1] from acetic acid [64-19-7] is currendy an important intermediate in the production of acetic acid, acetic anhydride [108-24-7] ethyl acetate [141-78-6] peracetic acid [79-21 -0] pentaerythritol [115-77-5] chloral [302-17-0], glyoxal [107-22-2], aLkylamines, and pyridines. Commercial processes for acetaldehyde production include the oxidation or dehydrogenation of ethanol, the addition of water to acetylene, the partial oxidation of hydrocarbons, and the direct oxidation of ethylene [74-85-1]. In 1989, it was estimated that 28 companies having more than 98% of the wodd s 2.5 megaton per year plant capacity used the Wacker-Hoechst processes for the direct oxidation of ethylene. 

High density polyethylene (HDPE) is defined by ASTM D1248-84 as a product of ethylene polymerisation with a density of 0.940 g/cm or higher. This range includes both homopolymers of ethylene and its copolymers with small amounts of a-olefins. The first commercial processes for HDPE manufacture were developed in the early 1950s and utilised a variety of transition-metal polymerisation catalysts based on molybdenum (1), chromium (2,3), and titanium (4). Commercial production of HDPE was started in 1956 in the United States by Phillips Petroleum Company and in Europe by Hoechst (5). HDPE is one of the largest volume commodity plastics produced in the world, with a worldwide capacity in 1994 of over 14 x 10 t/yr and a 32% share of the total polyethylene production. 

Although a small fraction of the world s vinyl chloride capacity is stiU based on acetylene or mixed actylene—ethylene feedstocks, nearly all production is conducted by the balanced process based on ethylene and chlorine (75). The reactions for each of the component processes are shown in equations 1—3 and the overall reaction is given by equation 4 ... 

Union Carbide Corp. also uses a siUca-supported chromium catalyst in their extremely low cost Unipol gas-phase linear low density ethylene copolymer process, which revolutionized the industry when it was introduced in 1977 (86—88). The productivity of this catalyst is 10 —10 kg polymer/kg transition metal contained in the catalyst. By 1990, the capacity of Unipol linear low density polyethylene reactors was sufficient to supply 25% of the world s total demand for polyethylene. 

Table 11. World Production Capacities for Ethylene Oxide ...

Ethyl acetate is an oxygenated solvent widely used in the inks, pharmaceuticals and fragrance sectors. The current global capacity for ethyl acetate is 1.2 million tonnes per annum. BP Chemicals is the world s largest producer of ethyl acetate. Conventional methods for the production of ethyl acetate are either via the liquid phase esterification of acetic acid and ethanol or by the coupling of acetaldehyde also known as the Tischenko reaction. Both of these processes require environmentally unfriendly catalysts (e.g. p-toluenesulphonic acid for the esterification and metal chlorides and strong bases for the Tischenko route). In 1997 BP Chemicals disclosed a new route to produce ethyl acetate directly from the reaction of ethylene with acetic acid using supported heteropoly acids... 

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