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Journal articles on the topic 'Interesterification technology'

Author: Grafiati

Published: 30 May 2022

Last updated: 31 May 2022

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1

Bryś, Joanna, Agata Górska, Ewa Ostrowska-Ligęza, Magdalena Wirkowska-Wojdyła, Andrzej Bryś, Rita Brzezińska, Karolina Dolatowska-Żebrowska, et al. "Human Milk Fat Substitutes from Lard and Hemp Seed Oil Mixtures." Applied Sciences 11, no. 15 (July 29, 2021): 7014. http://dx.doi.org/10.3390/app11157014.

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This paper discusses our attempt to generate substitutes for human breast milk fat through the interesterification of mixtures composed of lard and hemp (Cannabis sativa) seed oil. The interesterification was run at 60 °C for 2, 4, and 6 h in the presence of Lipozyme RM IM preparation containing a lipase specific for the cleavage of sn-1,3 ester bonds in triacylglycerol molecules. The interesterification products were analyzed regarding their fatty acid composition and distribution in triacylglycerol molecules. In order to assess the quality of the generated substitutes, in the interesterification products the following were determined: acid value, peroxide number, and oxidative stability. The collected data were statistically processed using Tukey’s test. Following the interesterification, the fats revealed an elevated percentage of free fatty acids and primary oxidation products and reduced oxidative stability compared to those of lard. The last of the above-mentioned phenomena could have been due to the incorporation of polyenic fatty acids into the external positions of triacyclglycerols of lard. The interesterification of lard and hemp seed oil allows scientists to acquire substitutes rich in essential fatty acids and similar to human breast milk fat with respect to the distribution of fatty acids in triacylglycerol molecules.

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2

VINTILA, Iuliana. "A Modern Dewaxing Technology For Edible Oils Refining." DARNIOS APLINKOS VYSTYMAS 19, no. 1 (May 6, 2022): 102–10. http://dx.doi.org/10.52320/dav.v19i1.191.

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The modern dewaxing process using endogenous wax ester hydrolyses (wax desynthetase) activation in optimal reaction conditions provides an efficient, specific and targeted affinity destructuration process orientated towards the wax substrate in order to develop the depparafinage effect. The lipase W/O interfacial activation was studied in the lipolyse and interesterification process but the endogenous O/S dewaesterase activation was until now non-investigated. The isoparaffins structures formation improves the dewaxing yield at 90.7% reported on the miscella crude oil with 270 ppm waxes content with an almost double-cold dewaxed oil stability. The present modern dewaxing technology eliminates the low-efficiency cold/low temperature crystallisation and all the negative effects given by the solvent oil recovery from the kieselgur pomace, cooling agent producing and separation by filtration/centrifugation process.

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3

Callejas Campioni, Nicolás, Leopoldo Suescun Pereyra, Ana Paula Badan Ribeiro, and Iván Jachmanián Alpuy. "Zero-trans fats designed by enzyme-catalyzed interesterification of rice bran oil and fully hydrogenated rice bran oil." OCL 28 (2021): 46. http://dx.doi.org/10.1051/ocl/2021036.

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Zero-trans edible fats attractive to be used for shortenings or margarines were designed solely from rice bran oil (RBO). For this purpose, RBO was fully hydrogenated, blended with the original oil at different percentages, and finally, blends were interesterified by an enzyme-catalyzed process. The interesterification process reduced the concentration of trisaturated and triunsaturated triglycerides and increased the concentration of medium saturation degree molecules, thus increasing their compatibility and causing the moderation of the melting point, as compared with blends. Conversely to blends, products showed a high tendency to crystallize under the β’ polymorph, which is the preferred one for products destined for many edible applications. Results demonstrated that the proper combination of different technologies (total hydrogenation, blending and interesterification) is a versatile and useful technology for designing zero-trans fats from RBO, attractive for the confection of shortenings or margarines for different applications depending on the proportion of each component in the starting blend. This strategy offers an attractive alternative for the diversification of RBO utilization, a valuable vegetable oil still underexploited, providing attractive fats useful for structuring different type of foods.

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4

Callejas Campioni, Nicolás, Leopoldo Suescun Pereyra, Ana Paula Badan Ribeiro, and Iván Jachmanián Alpuy. "Zero-trans fats designed by enzyme-catalyzed interesterification of rice bran oil and fully hydrogenated rice bran oil." OCL 28 (2021): 46. http://dx.doi.org/10.1051/ocl/2021036.

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Zero-trans edible fats attractive to be used for shortenings or margarines were designed solely from rice bran oil (RBO). For this purpose, RBO was fully hydrogenated, blended with the original oil at different percentages, and finally, blends were interesterified by an enzyme-catalyzed process. The interesterification process reduced the concentration of trisaturated and triunsaturated triglycerides and increased the concentration of medium saturation degree molecules, thus increasing their compatibility and causing the moderation of the melting point, as compared with blends. Conversely to blends, products showed a high tendency to crystallize under the β’ polymorph, which is the preferred one for products destined for many edible applications. Results demonstrated that the proper combination of different technologies (total hydrogenation, blending and interesterification) is a versatile and useful technology for designing zero-trans fats from RBO, attractive for the confection of shortenings or margarines for different applications depending on the proportion of each component in the starting blend. This strategy offers an attractive alternative for the diversification of RBO utilization, a valuable vegetable oil still underexploited, providing attractive fats useful for structuring different type of foods.

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5

Iida, Hajime, Natsumi Kageyama, Kazuma Shimura, and Saki Arita. "Interesterification of methyl stearate and soybean oil over potassium titanate." Catalysis Communications 144 (September 2020): 106095. http://dx.doi.org/10.1016/j.catcom.2020.106095.

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6

Bokhari, Awais, Suzana Yusup, Lai Fatt Chuah, Jiří Jaromír Klemeš, Saira Asif, Basit Ali, Majid Majeed Akbar, and Ruzaimah Nik M. Kamil. "Pilot scale intensification of rubber seed ( Hevea brasiliensis ) oil via chemical interesterification using hydrodynamic cavitation technology." Bioresource Technology 242 (October 2017): 272–82. http://dx.doi.org/10.1016/j.biortech.2017.03.046.

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7

Nunes, A. L. B., and F. Castilhos. "Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst." Fuel 267 (May 2020): 117264. http://dx.doi.org/10.1016/j.fuel.2020.117264.

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8

Paula, Ariela V., Gisele F. M. Nunes, Larissa Freitas, Heizir F. de Castro, and Julio C. Santos. "Interesterification of milkfat and soybean oil blends catalyzed by immobilized Rhizopus oryzae lipase." Journal of Molecular Catalysis B: Enzymatic 65, no. 1-4 (August 2010): 117–21. http://dx.doi.org/10.1016/j.molcatb.2009.12.008.

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9

Maddikeri, Ganesh L., Aniruddha B. Pandit, and Parag R. Gogate. "Ultrasound assisted interesterification of waste cooking oil and methyl acetate for biodiesel and triacetin production." Fuel Processing Technology 116 (December 2013): 241–49. http://dx.doi.org/10.1016/j.fuproc.2013.07.004.

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10

Postaue, Najla, Caroline Portilho Trentini, Bruna Tais Ferreira de Mello, Lúcio Cardozo-Filho, and Camila da Silva. "Continuous catalyst-free interesterification of crambe oil using methyl acetate under pressurized conditions." Energy Conversion and Management 187 (May 2019): 398–406. http://dx.doi.org/10.1016/j.enconman.2019.03.046.

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11

Esan, Akintomiwa O., Ojeyemi M. Olabemiwo, Siwaporn M. Smith, and Shangeetha Ganesan. "A concise review on alternative route of biodiesel production via interesterification of different feedstocks." International Journal of Energy Research 45, no. 9 (March 22, 2021): 12614–37. http://dx.doi.org/10.1002/er.6680.

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12

Wangi, Inasanti Pandan, Supriyanto Supriyanto, Hary Sulistyo, and Chusnul Hidayat. "Sodium Silicate Catalyst for Synthesis Monoacylglycerol and Diacylglycerol-Rich Structured Lipids: Product Characteristic and Glycerolysis–Interesterification Kinetics." Bulletin of Chemical Reaction Engineering & Catalysis 17, no. 2 (February 23, 2022): 250–62. http://dx.doi.org/10.9767/bcrec.17.2.13306.250-262.

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Sodium silicate as heterogeneous base catalysts is more environmentally friendly and easily separated by filtration. The objective of this research was to evaluate the activated sodium silicate as catalyst for synthesis of monoacylglycerol (MAG) and diacylglycerol (DAG)-rich structured lipids (SLs) from a palm olein-stearin blend. Sodium silicate was activated and functional group was characterized. Reaction was performed using 5% catalyst (w/w) at various reaction temperature (70–120 °C) for 3 h in a batch stirred tank reactor. Physical properties of SLs, such as melting point, slip melting point, and hardness of SLs were determined. Reaction kinetics were also evaluated. The results show that Si−O bending was reduced and shifted to a Si−O−Na and Si−O−Si functional groups after sodium silicate activation. Temperature had a significant effect on SLs composition at higher than 90 °C. An increase in temperature produced more MAG, resulting in better product physical properties. The best reaction condition was at 110 °C. Rate constants and the Arrhenius equation were also obtained for each reaction step. In summary, the activated sodium silicate catalyzed glycerolysis-interesterification reaction, which produced MAG and DAG at temperature higher than 90 °C. Therefore, the physical properties of SLs were improved. Copyright © 2022 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).

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13

Sytnik, Natalia, Igor Demidov, Ekaterina Kunitsa, Viktoria Mazaeva, and Olga Chumak. "A study of fat interesterification parameters’ effect on the catalytic reaction activity of potassium glycerate." Eastern-European Journal of Enterprise Technologies 3, no. 6(81) (June 26, 2016): 33. http://dx.doi.org/10.15587/1729-4061.2016.71236.

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14

Camacho Paez, B., A. Robles Medina, F. Camacho Rubio, L. Esteban Cerdán, and E. Molina Grima. "Kinetics of lipase-catalysed interesterification of triolein and caprylic acid to produce structured lipids." Journal of Chemical Technology & Biotechnology 78, no. 4 (March 19, 2003): 461–70. http://dx.doi.org/10.1002/jctb.810.

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15

Casas, Abraham, Ángel Pérez, and María Jesús Ramos. "Purification of Methyl Acetate/Water Mixtures from Chemical Interesterification of Vegetable Oils by Pervaporation." Energies 14, no. 3 (February 2, 2021): 775. http://dx.doi.org/10.3390/en14030775.

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Biodiesel production through chemical interesterification of triglycerides requires an excess of methyl acetate that must be recovered once the reaction is finished and the catalyst is neutralized. The present study concerns with the purification of methyl acetate by pervaporation. PERVAP 2201 was chosen as pervaporation membrane due to its high hydrophilic character that makes it suitable for the elimination of water in methyl acetate. Runs were started from concentrations in the feed of 2–8 wt.% of water and working temperatures close to the boiling point of methyl acetate (50, 60, and 70 °C), to get the main design parameters, i.e., permeate flux and selectivity. High temperature favored the permeate flux without compromising the selectivity. However, the flux declines significantly when water contained in the feed is below 2 wt.%. This implies that pervaporation should be used, only to decrease the water content to a value lower than in the azeotrope (2.3% by weight). A solution-diffusion model relating the flux of the permeating compound with the activity of the compound in the feed and the operating temperature has been proposed. The model obtained can be used in the design of the pervaporation stage, thus allowing to know the permeate flux for the different operating conditions.

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16

Prestigiacomo, Claudia, Martina Biondo, Alessandro Galia, Eric Monflier, Anne Ponchel, Dominique Prevost, Onofrio Scialdone, Sebastien Tilloy, and Rudina Bleta. "Interesterification of triglycerides with methyl acetate for biodiesel production using a cyclodextrin-derived SnO@γ-Al2O3 composite as heterogeneous catalyst." Fuel 321 (August 2022): 124026. http://dx.doi.org/10.1016/j.fuel.2022.124026.

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17

Osório, N. M., M. H. Ribeiro, M. M. R. da Fonseca, and S. Ferreira-Dias. "Interesterification of fat blends rich in ω-3 polyunsaturated fatty acids catalysed by immobilized Thermomyces lanuginosa lipase under high pressure." Journal of Molecular Catalysis B: Enzymatic 52-53 (June 2008): 58–66. http://dx.doi.org/10.1016/j.molcatb.2007.11.008.

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18

Debnath, Sukumar, Maya Prakash, and Belur R. Lokesh. "Lipase-Mediated Interesterification of Oils for Improving Rheological, Heat Transfer Properties and Stability During Deep-Fat Frying." Food and Bioprocess Technology 5, no. 5 (January 8, 2011): 1630–41. http://dx.doi.org/10.1007/s11947-010-0485-3.

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19

Kashyap, Shubham S., Parag R. Gogate, and Saurabh M. Joshi. "Ultrasound assisted intensified production of biodiesel from sustainable source as karanja oil using interesterification based on heterogeneous catalyst (γ-alumina)." Chemical Engineering and Processing - Process Intensification 136 (February 2019): 11–16. http://dx.doi.org/10.1016/j.cep.2018.12.006.

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20

AT, Oltiev. "Guarantee of Food Safety of Fat by Technology of Interesterification." Journal of Experimental Food Chemistry 02, no. 04 (2016). http://dx.doi.org/10.4172/2472-0542.1000116.

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21

Makarevičienė, Violeta, and Ieva Sendžikaitė. "Biocatalytic transesterification of rapeseed oil by methyl formate." Žemės ūkio mokslai 26, no. 1 (May 10, 2019). http://dx.doi.org/10.6001/zemesukiomokslai.v26i1.3969.

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Due to the awareness of adverse effects of conventional fuels on environment and on a frequent rise in the crude oil price, the need for a sustainable and environment-friendly alternate source of energy has gained importance. Recently, options have been analysed to replace the triglyceride transesterification process, which is generally used in biodiesel production, by the process where raw glycerol is not generated, whereas triacylglycerides obtained instead glycerol can be directly used as fuel for a diesel engine in a mixture with fatty acid esters. In the present work, interesterification of rapeseed oil to biodiesel was carried out with methyl formate and using lipase as a catalyst. The research was carried out at the Laboratory of Chemical and Biochemical Research for Environmental Technology of Aleksandras Stulginskis University. First, the most effective biocatalyst suitable for the process was selected. 14 different lipases were studied. The samples obtained after the synthesis were analysed by the thin-layer and gas chromatography. Process experiments were performed using a methyl formate to oil molar ratio of 6:1 to 40:1, a lipase amount of 5 to 17% (mass of oil) and synthesis duration of 3 to 48 h. The highest yield of fatty acid methyl esters (FAME) was obtained using Lipozyme RM IM as a catalyst and its optimal amount was 13%. The optimal temperature was found to be 20°C and the duration of interesterification 42 h. The optimal molar ratio of methyl formate to oil was determined to be 32:1. Under the obtained conditions the transesterification degree was 60.68 ± 0.95%.

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22

Wong, Wan‐Ying, Steven Lim, Yean‐Ling Pang, Wei‐Hsin Chen, Man‐Kee Lam, and Inn‐Shi Tan. "Synthesis of glycerol‐free fatty acid methyl ester using interesterification reaction based on solid acid carbon catalyst derived from low‐cost biomass wastes." International Journal of Energy Research, October 29, 2020. http://dx.doi.org/10.1002/er.6041.

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