Investigation of Crystal Size Distribution in Purification of Terephthalic Acid from Polyester Textile Industry Waste by Reactive Crystallization

https://doi.org/10.22146/ijc.80820

Bekti Marlena(1*), Hary Sulistyo(2), Rochmadi Rochmadi(3)

(1) Department of Chemical Engineering, Universitas Gadjah Mada, Jl. Grafika 2, Yogyakarta 55284, Indonesia; Center for Standardization and Industrial Pollution Prevention Services, Jl. Kimangunsarkoro No. 6, Semarang 5013, Indonesia
(2) Department of Chemical Engineering, Universitas Gadjah Mada, Jl. Grafika 2, Yogyakarta 55284, Indonesia
(3) Department of Chemical Engineering, Universitas Gadjah Mada, Jl. Grafika 2, Yogyakarta 55284, Indonesia
(*) Corresponding Author

Abstract


The purification of terephthalic acid recovered from an alkali-reduction wastewater by reactive crystallization was investigated. The crude terephthalic acid was reacted with sodium hydroxide solution to form a salt of disodium terephthalate, then acidified with sulfuric acid to get the terephthalic acid with higher purity. Effects of time, pH, concentration, and flow rate of secondary feed solutions, temperature, and stirring rate on Crystal Size Distribution (CSD) of terephthalic acid precipitate were investigated. The results showed that CSD was influenced by the concentration of reactants and the pH solution. On the other hand, time, temperature, flow rate of secondary solution, and stirring rate had no significant effects on the CSD, which the mean size of crystals ±3 μm. The mean size of crystals at solution pH 5, 4, and 3 were 6.03, 9.42, and 10.34 μm, respectively; meanwhile, at concentrations of 0.5, 0.3, and 0.1 M, were 7.57, 3.24, and 3.09 μm, respectively. The semi-batch reactive crystallization with double-feeding at constant pH and temperature produced monodispersed crystals. However, this method needs to be carried out more than once for terephthalic acid purification, which is intended for polyethylene terephthalate (PET) polymerization.

Keywords


crystal size distribution; purification; reactive crystallization; terephthalic acid

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References

[1] Cao, J., Meng, C., Cheng, X., and Pan, X., 2019, Surface alkali deweighting and dyeing of polyester fabric by one-bath and one-step process, Surf. Innovations, 7 (2), 104–111.

[2] Gupta, D., Chaudhary, H., and Gupta, C., 2015, Topographical changes in polyester after chemical, physical and enzymatic hydrolysis, J. Text. Inst., 106 (7), 690–698.

[3] Hilal, N.M., Gomaa, S.H., and ELsisi, A.A., 2020, Improving dyeing parameters of polyester/cotton blended fabrics by caustic soda, chitosan, and their hybrid, Egypt. J. Chem., 63 (6), 2381–2395.

[4] Yang, B., Xu, H., Wang, J., Yan, D., Zhong, Q., and Yu, H., 2018, Performance evaluation of anaerobic baffled reactor (ABR) for treating alkali-decrement wastewater of polyester fabrics at incremental organic loading rates, Water Sci. Technol., 77 (10), 2445–2453.

[5] Chaonan, L., and Jihua, C., 2007, The study of the recovery of highly purified terephthalic acid from alkali weight-reduction wastewater, Int. J. Environ. Pollut., 29 (4), 484–494.

[6] Lewis, A.E., Seckler, M.M., Kramer, H., and Van Rosmalen, G., 2015, Industrial Crystallization: Fundamentals and Applications, Cambridge University Press, Cambridge, UK.

[7] Lee, A.Y., Erdemir, D., and Myerson, A.S., 2019, "Crystals and Crystal Growth" in Handbook of Industrial Crystallization, Eds. Myerson, A.S., Erdemir, D., and Lee, A.Y., Cambridge University Press, Cambridge, UK, 32–75.

[8] Nagy, Z.K., Fujiwara, M., and Braatz, R.D., 2019, "Monitoring and Advanced Control of Crystallization Processes" in Handbook of Industrial Crystallization, Eds. Myerson, A.S., Erdemir, D., and Lee, A.Y., Cambridge University Press, Cambridge, UK, 313–345.

[9] Nicoud, L.H., and Myerson, A.S., 2019, The "Influence of Impurities and Additives on Crystallization" in Handbook of Industrial Crystallization, Eds. Myerson, A.S., Erdemir, D., and Lee, A.Y., Cambridge University Press, Cambridge, UK, 115–135.

[10] Suharso, S., Parkinson, G., and Ogden, M., 2007, Effect of cetyltrimethylammonium bromide (CTAB) on the growth rate and morphology of borax crystals, J. Appl. Sci., 7 (10), 1390–1396.

[11] Karpiński, P.H., and Bałdyga, J., 2019, "Precipitation Processes" in Handbook of Industrial Crystallization, Eds. Myerson, A.S., Erdemir, D., and Lee, A.Y., Cambridge University Press, Cambridge, UK, 216–265.

[12] Pitt, K., Peña, R., Tew, J.D., Pal, K., Smith, R., Nagy, Z.K., and Litster, J.D., 2018, Particle design via spherical agglomeration: A critical review of controlling parameters, rate processes and modelling, Powder Technol., 326, 327–343.

[13] Liu, F., Bagi, S.D., Su, Q., Chakrabarti, R., Barral, R., Gamekkanda, J.C., Hu, C., and Mascia, S., 2022, Targeting particle size specification in pharmaceutical crystallization: A review on recent process design and development strategies and particle size measurements, Org. Process Res. Dev., 26 (12), 3190–3203.

[14] Bałdyga, J., 2016, Mixing and fluid dynamics effects in particle precipitation processes, KONA Powder Part. J., 33, 127–149.

[15] Rewatkar, K., Shende, D.Z., and Wasewar, K.L., 2018, Reactive crystallization of calcium oxalate: Population balance modeling, Chem. Biochem. Eng. Q., 32 (1), 11–18.

[16] Caro, J.A., Woldehaimanot, M., and Rasmuson, Å.C., 2014, Semibatch reaction crystallization of salicylic acid, Chem. Eng. Res. Des., 92 (3), 522–533.

[17] Han, B., and Louhi-Kultanen, M., 2018, Real-time Raman monitoring of calcium phosphate precipitation in a semi-batch stirred crystallizer, Cryst. Growth Des., 18 (3), 1622–1628.

[18] Zhang, W., Zhang, F., Ma, L., Yang, J., Yang, J., and Xiang, H., 2019, Prediction of the crystal size distribution for reactive crystallization of barium carbonate under growth and nucleation mechanisms, Cryst. Growth Des., 19 (7), 3616–3625.

[19] Chen, P.C., Cheng, G.Y., Kou, M.H., Shia, P.Y., and Chung, P.O., 2001, Nucleation and morphology of barium carbonate crystals in a semi-batch crystallizer, J. Cryst. Growth, 226 (4), 458–472.

[20] Tai, C.Y., and Chen, P.C., 1995, Crystal growth and agglomeration of calcium sulfite hemihydrate crystals, Ind. Eng. Chem. Res., 34 (4), 1342–1351.

[21] Slapnik, J., Kraft, G., Wilhelm, T., and Lobnik, A., 2019, Purification of Recycled Terephthalic Acid and Synthesis of Polyethylene Terephthalate, The 1st International Conference on Circular Packaging, Ljubljana, Slovenia, 151–159.

[22] McDonald, M.A., Salami, H., Harris, P.R., Lagerman, C.E., Yang, X., Bommarius, A.S., Grover, M.A., and Rousseau, R.W., 2021, Reactive crystallization: A review, React. Chem. Eng., 6 (3), 364–400.

[23] Rezazadeh, A., Thomsen, K., Gavala, H.N., Skiadas, I.V., and Fosbøl, P.L., 2021, Solubility and freezing points of disodium terephthalate in water-ethylene glycol mixtures, J. Chem. Eng. Data, 66 (5), 2143–2152.

[24] Christian, G.D., Dasgupta, P.K., and Schug, K.A., 2013, Analytical Chemistry, 7th Ed., John Wiley & Sons, Inc., Hoboken, New York, US.

[25] Rehage, H., Semmel, M., and Kind, M., 2020, A dynamic model for process flowsheet simulation of semi-batch precipitation of sparingly soluble salts, Comput. Chem. Eng., 137, 106818.

[26] Amari, S., Sugawara, C., Kudo, S., and Takiyama, H., 2022, Investigation of operation strategy based on solution pH for improving the crystal quality formed during reactive crystallization of L-aspartic acid, ACS Omega, 7 (3), 2989–2995.

[27] Sato, E., Seki, Y., and Takiyama, H., 2019, Control of reaction crystallization of organic compounds using the supersaturation profile, J. Chem. Eng. Jpn., 52 (7), 599–604.

[28] Utomo, J., Asakuma, Y., Maynard, N., Maeda, K., Fukui, K., and Tadé, M.O., 2010, Semi-batch reactive crystallisation of mono-ammonium phosphate: An experimental study, Chem. Eng. J., 156 (3), 594–600.

[29] Li, M., Shang, Z., and Hou, B., 2019, Optimizing the aspect ratio of cephalexin in reactive crystallization by controlling supersaturation and seeding policy, Trans. Tianjin Univ., 25 (4), 348–356.

[30] Park, C., and Sheehan, R.J., 2000, "Phthalic Acids and Other Benzenepolycarboxylic Acids" in KirkOthmer Encyclopedia of Chemical Technology, John Wiley & Son, New York.

[31] Tourbin, M., Brouillet, F., Galey, B., Rouquet, N., Gras, P., Chebel, N.A., Grossin, D., and Frances, C., 2020, Agglomeration of stoichiometric hydroxyapatite: Impact on particle size distribution and purity in the precipitation and maturation steps, Powder Technol., 360, 977–988.

[32] Wiley-VCH, 2016, Ullmann’s Polymer and Plastics, 1st Ed., Wiley-VCH, Weinheim, Germany.

[33] Azarpour, A., Rezaei, N., and Zendehboudi, S., 2020, Product quality control in hydropurification process by monitoring reactor feed impurities: Dynamic mathematical modeling, J. Ind. Eng. Chem., 92, 62–76.

[34] Rao, P.N., Sabavath, G.K., and Paul, S.N., 2021, Impact of MTA blend % in melt spinning process and polyester properties, SN Appl. Sci., 3 (2), 184.



DOI: https://doi.org/10.22146/ijc.80820

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