Terephthalic acid was first isolated (from turpentine) by the French chemist Amédée Cailliot (1805–1884) in 1846.[11] Terephthalic acid became industrially important after World War II. Terephthalic acid was produced by oxidation of p-xylene with 30-40% nitric acid. Air oxidation of p-xylene gives p-toluic acid, which resists further air-oxidation. Esterification of p-toluic acid to methyl p-toluate (CH3C6H4CO2CH3) opens the way for further oxidation to monomethyl terephthalate. In the Dynamit−Nobel process these two oxidations and the esterification were performed in a single reactor. The reaction conditions also lead to a second esterification, producing dimethyl terephthalate, which could be hydrolysed to terepthalic acid. In 1955, Mid-Century Corporation and ICI announced the bromide-catalysed oxidation of p-toluic acid directly to terephthalic acid, without the need to isolate intermediates and still using air as the oxidant. Amoco (as Standard Oil of Indiana) purchased the Mid-Century/ICI technology, and the process is now known by their name.[12]
The oxidation of p-xylene proceeds by a free radical process. Bromine radicals decompose cobalt and manganese hydroperoxides. The resulting oxygen-based radicals abstract hydrogen from a methyl group, which have weaker C–H bonds than does the aromatic ring. Many intermediates have been isolated. p-xylene is converted to p-toluic acid, which is less reactive than the p-xylene owing to the influence of the electron-withdrawingcarboxylic acid group. Incomplete oxidation produces 4-carboxybenzaldehyde (4-CBA), which is often a problematic impurity.[12][13][14]
Approximately 5% of the acetic acid solvent is lost by decomposition or "burning". Product loss by decarboxylationtobenzoic acid is common. The high temperature diminishes oxygen solubility in an already oxygen-starved system. Pure oxygen cannot be used in the traditional system due to hazards of flammable organic–O2 mixtures. Atmospheric air can be used in its place, but once reacted needs to be purified of toxins and ozone depleters such as methylbromide before being released. Additionally, the corrosive nature of bromides at high temperatures requires the reaction be run in expensive titanium reactors.[15][16]
The use of carbon dioxide overcomes many of the problems with the original industrial process. Because CO2 is a better flame inhibitor than N2, a CO2 environment allows for the use of pure oxygen directly, instead of air, with reduced flammability hazards. The solubility of molecular oxygen in solution is also enhanced in the CO2 environment. Because more oxygen is available to the system, supercritical carbon dioxide (Tc = 31 °C) has more complete oxidation with fewer byproducts, lower carbon monoxide production, less decarboxylation and higher purity than the commercial process.[15][16]
Insupercritical water medium, the oxidation can be effectively catalyzed by MnBr2 with pure O2 in a medium-high temperature. Use of supercritical water instead of acetic acid as a solvent diminishes environmental impact and offers a cost advantage. However, the scope of such reaction systems is limited by the even more demanding conditions than the industrial process (300–400 °C, >200 bar).[17]
As with any large-scale process, many additives have been investigated for potential beneficial effects. Promising results have been reported with the following.[12]
Ketones act as promoters for formation of the active cobalt(III) catalyst. In particular, ketones with α-methylene groups oxidize to hydroperoxides that are known to oxidize cobalt(II). 2-Butanone is often used.
Zirconium salts enhance the activity of Co-Mn-Br catalysts. Selectivity is also improved.[12]
N-Hydroxyphthalimide is a potential replacement for bromide, which is highly corrosive. The phthalimide functions by formation of the oxyl radical.
Guanidine inhibits the oxidation of the first methyl but enhances the usually slow oxidation of the toluic acid.
Terephthalic acid can be prepared in the laboratory by oxidizing many para-disubstituted derivatives of benzene, including caraway oil or a mixture of cymene and cuminol with chromic acid.
Although not commercially significant, there is also the so-called "Henkel process" or "Raecke process", named after the company and patent holder, respectively. This process involves the transfer of carboxylate groups. For example potassium benzoate disproportionates to potassium terephthalate, and potassium phthalate rearranges to potassium terephthalate.[18][19]
Lummus (now a subsidiary of McDermott International) has reported a route from the dinitrile, which can be obtained by ammoxidationofp-xylene.
Virtually the entire world's supply of terephthalic acid and dimethyl terephthalate are consumed as precursors to polyethylene terephthalate (PET). World production in 1970 was around 1.75 million tonnes.[8] By 2006, global purified terephthalic acid (PTA) demand had exceeded 30 million tonnes. A smaller, but nevertheless significant, demand for terephthalic acid exists in the production of polybutylene terephthalate and several other engineering polymers.[20]
Polyester fibers based on PTA provide easy fabric care, both alone and in blends with natural and other synthetic fibers. Polyester films are used widely in audio and video recording tapes, data storage tapes, photographic films, labels and other sheet material requiring both dimensional stability and toughness.
Terephthalic acid is used in paint as a carrier.
Terephthalic acid is used as a raw material to make terephthalate plasticizers such as dioctyl terephthalate and dibutyl terephthalate.
It is used in the pharmaceutical industry as a raw material for certain drugs.
In addition to these end uses, Terephthalic acid based polyesters and polyamides are also used in hot melt adhesives.
PTA is an important raw material for lower molecular weight saturated polyesters for powder and water-soluble coatings.
In the research laboratory, terephthalic acid has been popularized as a component for the synthesis of metal-organic frameworks.
The analgesic drug oxycodone occasionally comes as a terephthalate salt; however, the more usual salt of oxycodone is the hydrochloride. Pharmacologically, one milligram of hydrochloridum oxycodonae is equivalent to 1.13 mg of terephthalas oxycodonae.
Terephthalic acid is used as a filler in some military smoke grenades, most notably the American M83 smoke grenade and M90 vehicle-employed smoke grenade, producing a thick white smoke that acts as an obscurant in the visual and near-infrared spectrum when burned.
Terephthalic acid is poorly soluble in water and alcohols; consequently, until about 1970 terephthalic acid was purified as its dimethyl ester. It sublimes when heated.
^Cailliot, Amédée (1847). "Études sur l'essence de térébenthine" [Studies of the essence of turpentine]. Annales de Chimie et de Physique. Série 3. 21: 27–40. Terephthalic acid is named on p. 29:『Je désignerai le premier de ces acides, celui qui est insoluble, sous le nom d'acide téréphtalique.』(I will designate the first of these acids, which is insoluble, by the name of terephthalic acid.)
^ abcdeTomás, Rogério A. F.; Bordado, João C. M.; Gomes, João F. P. (2013). "p-Xylene Oxidation to Terephthalic Acid: A Literature Review Oriented toward Process Optimization and Development". Chemical Reviews. 113 (10): 7421–69. doi:10.1021/cr300298j. PMID23767849.
^Wang, Qinbo; Cheng, Youwei; Wang, Lijun; Li, Xi (2007). "Semicontinuous Studies on the Reaction Mechanism and Kinetics for the Liquid-Phase Oxidation of p-Xylene to Terephthalic Acid". Industrial & Engineering Chemistry Research. 46 (26): 8980–8992. doi:10.1021/ie0615584.
^Xiao, Y.; Luo, W.-P.; Zhang, X.-Y.; et al. (2010). "Aerobic Oxidation of p-Toluic Acid to Terephthalic Acid over T(p-Cl)PPMnCl/Co(OAc)2 Under Moderate Conditions". Catalysis Letters. 134 (1–2): 155–161. doi:10.1007/s10562-009-0227-1. S2CID95855968.
^ abZuo, Xiaobin; Subramaniam, Bala; Busch, Daryle H. (2008). "Liquid-Phase Oxidation of Toluene and p-Toluic Acid under Mild Conditions: Synergistic Effects of Cobalt, Zirconium, Ketones, and Carbon Dioxide". Industrial & Engineering Chemistry Research. 47 (3): 546–552. doi:10.1021/ie070896h.
^Pérez, Eduardo; Fraga Dubreuil, Joan; García Verdugo, Eduardo; et al. (2011). "Selective Aerobic Oxidation of para-Xylene in Sub- and Supercritical Water. Part 1. Comparison with Ortho-xylene and the Role of the Catalyst". Green Chemistry. 13 (12): 2389–2396. doi:10.1039/C1GC15137A.
^Ogata, Yoshiro; Hojo, Masaru; Morikawa, Masanobu (1960). "Further Studies on the Preparation of Terephthalic Acid from Phthalic or Benzoic Acid". Journal of Organic Chemistry. 25 (12): 2082–2087. doi:10.1021/jo01082a003.
^Ashford's Dictionary of Industrial Chemicals (3rd ed.). Saltash, UK: Wavelength. 2011. p. 8805. ISBN978-0952267430.
