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Poly(lactic acid)


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G. Losse, G. Bachmann, Synthese von depsipeptiden, Chem. Ber. 1964, 97(9), 2671–2680.

      20 20. D. Vorländer, R. Walter, Die mechanisch erzwungene Doppelbrechung der amorphen Flüssigkeiten im Zusammenhang mit der molekularen Gestalt, Z. Für. Phys. Chem. 1925, 118U(1), 1–30.

      21 21. Y. Ogata, M. Inaishi, Preparation of dl‐alanine by the reaction of (±)‐2‐chloropropionic acid with aqueous ammonia under pressure, Bull. Chem. Soc. Jpn. 1981, 54(11), 3605–3606.

      22 22. P. J. Flory, Molecular size distribution in linear condensation polymers, J. Am. Chem. Soc. 1936, 58(10), 1877–1885.

      23 23. P. D. Watson, Composition of lactic acid production of a highly concentrated acid, Ind. Eng. Chem. 1940, 32(3), 399–401.

      24 24. R. Montgomery, Acidic constituents of lactic acid‐water systems, J. Am. Chem. Soc. 1952, 74(6), 1466–1468.

      25 25. R. Ueda, T. Terajima, The utilization of lactic acid obtained by fermentation, XII. Change in the polymers by dilution with water, Hakko Kogaku Zasshi. 1958, 36, 371–374.

      26 26. S. Bezzi, L. Riccoboni, Memorie della Classe di Scienze Fisiche, Matematiche e Naturali. Reale Accademia d'Italia 1937, 8, 181–200.

      27 27. D. T. Vu, A. K. Kolah, N. S. Asthana, L. Peereboom, C. T. Lira, D. J. Miller, Oligomer distribution in concentrated lactic acid solutions, Fluid Phase Equilibria. 2005, 236(1–2), 125–135.

      28 28. C. H. Holten, A. Müller, D. Rehbinde, Lactic Acid, Verlag Chemie, International Research Association, Copenhagen, 1971.

      29 29. S. Feng, S. Xiang, X. Bian, G. Li, Quantitative analysis of total acidity in aqueous lactic acid solutions by direct potentiometric titration, Microchem. J. 2020, 157, 105049.

      30 30. M. T. Sanz, S. Beltran, B. Calvo, J. L. Cabezas, Vapor liquid equilibria of the mixtures involved in the esterfication of lactic acid with methanol, J. Chem. Eng. Data. 2003, 48(6), 1446–1452.

      31 31. D. T. Vu, Properties and separations of plant‐derived chemicals, Ph.D. thesis, Michigan State University, East Lansing 2007.

      32 32. R. A. Troupe, W. L. Aspy, P. R. Schrodt, Viscosity and density of aqueous lactic acid solutions, Ind. Eng. Chem. 1951, 43(5), 1143–1146.

      Anders Södergård Mikael Stolt and Saara Inkinen

      PLA of high molecular weight is most commonly made by ring‐opening polymerization (ROP) of the ring‐formed dimer, dilactide (lactide; 3,6‐dimethyl‐1,4‐dioxane‐2,5‐dione), which is made by depolymerization of the polycondensed LA (2‐hydroxypropanoic acid). This route is a two‐step reaction that usually involves additional purification steps and is therefore costly. It is often stated in the art that the preparation of high‐molecular‐weight PLA by a direct dehydration condensation reaction is not feasible due to the equilibrium not favoring a high‐molecular‐weight polymer. PLA prepared from polycondensation has low molecular weight and poor mechanical properties and therefore is not suitable for many applications. The commercial interest for solving this problem has increased because of the need of cost‐effective approaches in the manufacturing of LA‐based polymers with a high molecular weight. Solvent‐assisted polycondensation is one way to overcome this problem [4] and melt polycondensation followed by solid‐state polycondensation is another one [5]. The third approach to achieve high‐molecular‐weight LA‐based polymers is to utilize the terminal groups of the prepolymer in linking processes where a linking agent is employed [6]. Such prepolymers can be composed of solely one stereoisomer, combinations of D‐ and L‐lactoyl units in various ratios, lactic acid in combination with other hydroxy acids, or di‐/multifunctional comonomers. If the lactic acid is polycondensated in the presence of difunctional monomers (e.g., diols or diacids), the resulting prepolymer will have the same end groups in both chain ends; that is, the prepolymer is a telechelic macromer [6].

      Since the first commercial products of lactic‐acid‐based polymers were introduced in the market by DuPont, Chronopol, and Cargill at the end of the 1980s and the beginning of the 1990s, PLA has been successfully commercialized by several companies and subsequently found use in several different end‐product categories [7]. However, PLA was initially used mainly in medical applications [8], which continue to be an important field for some PLA producers [9]. Today, PLA is one of the most important bio‐based and biodegradable polymers suitable for a wide variety of applications [10].

      The unique position of PLA in the field of bio‐based products is related to its processability, appearance, and properties such as mechanical strength and barrier. In addition to the medical sector, other uses of PLA include food and nonfood packaging, food service ware, agricultural materials, durable goods, electronics, building, construction, and 3D‐printing [11, 12]. Since 2005, the business of bio‐based material production has grown significantly. In 2020, 18.7% (i.e., 395,000 metric tons) of the total annual production capacity of bioplastics was attributed to PLA [13].

Schematic illustration of manufacturing routes for lactic-acid-based polymers.

      In the past decade, the commercial production of PLA has been boosted by the global shift in consumer awareness toward eco‐friendly packaging, the technological developments and investments related to large‐scale manufacturing, and the concurrent development of suitable applications and products. PLA is hence on its way to become a true commodity polymer.

      At the moment, the American market leader, Natureworks, holds a leading position in terms of PLA production capacity (150,000 metric tons) [7], followed by Total Corbion PLA from the Netherlands with its 75,000 metric tons production site in Thailand [14]. Total Corbion PLA is additionally building a 100,000 metric tons PLA plant, which is to become operational in 2024, in France [15]. Also, Belgian Futerro [16] and Zhejiang Hisun Biodegradable Plastics Corporation [17] are significant PLA producers, with production capacities of 30,000 and 15,000 metric tons, respectively. The Austrian Weforyou Group and its subsidiary Jiangsu Supla Bioplastics should also be noted with their 10,000 metric tons production site in China [18]. Additionally, several other producers exist, and the market is expected to exhibit significant growth during the coming years due to new production sites in China, the United States, and Europe.

      From a chemistry point of view, lactic acid can form PLA by means of the reaction of the hydroxyl and carboxylic acid groups of lactic acid. By removing the water formed during this condensation reaction, the reaction proceeds toward the product side, PLA: