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Документ Development of soapstock processing technology to ensure waste-free and safe production(Технологічний центр, 2021) Kalyna, V. N.; Koshulko, Vitalii; Ilinska, O. V.; Tverdokhliebova, Natalia; Tolstousova, Oksana; Bliznjuk, Olga; Gavrish, Tatiana; Stankevych, Sergij; Zabrodina, Inna; Zhulinska, OksanaSoapstock is a large-tonnage waste of the oil and fat industry, the disposal of which is environmentally hazardous. Processing of soapstock into industrially valuable products, in particular, fatty acids, is promising. The method for producing fatty acids, which consists in sequential saponification of soapstock with sodium hydroxide solution, salting out with sodium chloride and decomposition with sulfuric acid solution has been investigated. The feature of this work is the study of the effect of salting out conditions of saponified soapstock on the yield and neutralization number of fatty acids. As an experimental sample, sunflower soapstock was used, the indicators of which correspond to DSTU 5033 (CAS 68952-95-4): mass fraction of total fat – 67.3 %, fatty acids – 61.8 %, neutral fat – 5.5 %. Soapstock was subjected to preliminary saponification under the following conditions: duration 85 min., concentration of sodium hydroxide solution 45 %. After that, the saponified mass was subjected to salting out. The obtained core soap was decomposed with the sulfuric acid solution under the following conditions: temperature 90 °C, duration 40 min. Rational salting out conditions were determined: duration (80 min.) and sodium chloride concentration (16 %). Under these conditions, the fatty acid yield is 95.0 %, the neutralization number is 194.8 mg KOH/g. The resulting fatty acids comply with DSTU 4860 (CAS 61788-66-7): the mass fraction of moisture and volatiles is 0.85 %, the mass fraction of total fat is 98.9 %, cleavage depth is 94.2 % oleic acid. This method of soapstock processing increases the fatty acid yield by 3.5 % compared to the method with saponification and decomposition, by 20.3 % compared to the method of soapstock decomposition with sulfuric acid. At the same time, the neutralization number increases by 4.1 % and 8.2 %, respectively. The improved method for fatty acids producing from soapstock provides highquality fatty acids with increased yield.Документ Development of rational technology for sodium glyceroxide obtaining(Технологічний центр, 2022) Korchak, Mykola; Bliznjuk, O. N.; Nekrasov, Serhii; Gavrish, Tatiana; Petrova, Olena; Shevchuk, Natalia; Strikha, Liudmyla; Kostyrkin, Oleg; Semenov, Evgeny; Saveliev, DmytroThe process of sodium glyceroxide obtaining by the reaction of glycerol and sodium hydroxide in the form of an aqueous solution was investigated. Glycerol salts (metal glyceroxides) are important components in the synthesis of many compounds. Glyceroxides are used in the chemical industry, construction, medical practice, etc. Glyceroxides of alkali metals are used in the production of modified fats and biodiesel fuel. P.a.-grade glycerol (CAS Number 56-81-5) was used with a mass fraction of the main substance of 99.5 %. The parameters of sodium hydroxide (CAS Number 1310-73-2) were studied: the mass fraction of the main substance is 98.0 %, the mass fraction of sodium carbonate is 0.5%. Rational conditions for sodium glyceroxide obtaining were determined: temperature (145 °C) and concentration of sodium hydroxide solution (65 %). Under these conditions, the mass fraction of the main substance in the product was 80 %. The melting point (72 °C) and mass fraction of moisture (0.3 %) in sodium glyceroxide were determined. The catalytic activity of the product in the process of transesterification of palm olein was tested. The increase in the melting point of palm olein was 15 °C. Under similar conditions of using potassium glyceroxide with a mass fraction of the main substance of 75.77 %, the increase in the melting point is 12.1 °C. This indicates an increase in the efficiency of the transesterification process using sodium glyceroxide obtained by the developed technology. The research results make it possible to produce sodium glyceroxide under rational conditions with a high mass fraction of the main substance at enterprises that use metal glyceroxides as a production component or commercial product. The determined rational conditions will make it possible to effectively use the company’s resources and predict the quality of the final product. Досліджено процес одержання натрій гліцерату шляхом реагування гліцерину та натрій гідроксиду у вигляді водного розчину. Солі гліцерину (гліцерати металів) є важливими складовими у процесах синтезу багатьох сполук. Гліцерати застосовуються у хімічній промисловості, будівництві, медичній практиці тощо. Гліцерати лужних металів використовуються у виробництві модифікованих жирів та біодизельного пального. Застосовано гліцерин (CAS Number 56-81-5) кваліфікації ч. д. а. з масовою часткою основної речовини 99,5 %. Досліджено показники натрій гідроксиду (CAS Number 1310-73-2): масова частка основної речовини – 98,0 %, масова частка натрій карбонату – 0,5 %. Встановлено раціональні умови отримання натрій гліцерату: температуру (145 °C) та концентрацію розчину натрій гідроксиду (65 %). За цих умов масова частка основної речовини в продукті склала 80 %. В натрій гліцераті визначено температуру плавлення (72 °C) та масову частку вологи (0,3 %). Перевірено каталітичну активність продукту у процесі переетерифікування олеїну пальмового. Підвищення температури плавлення олеїну пальмового склало 15 °C. За аналогічних умов використання калій гліцерату з масовою часткою основної речовини 75,77 % підвищення температури плавлення становить 12,1 °C. Це свідчить про підвищення ефективності процесу переетерифікування з використанням натрій гліцерату, отриманого за розробленою технологією. Результати досліджень дають можливість виробляти натрій гліцерат за раціональних умов з високою масовою часткою основної речовини на підприємствах, де використовують гліцерати металів як складову виробництва або товарний продукт. Встановлені раціональні умови дозволять ефективно використовувати ресурси підприємства та прогнозувати якість кінцевого продукту.Документ Development of safe technology of obtaining fatty acid monoglycerides using a new catalyst(ПП "Технологічний Центр", 2022) Bliznjuk, O. N.; Masalitina, N. Yu.; Mezentseva, Iryna; Novozhylova, Tetiana; Korchak, Mykola; Haliasnyi, Ivan; Gavrish, Tatiana; Fomina, Iryna; Khalil, Viktoriya; Nikitchenko, OlgaFatty acid monoglycerides are a valuable component of the products of various industries. The emulsifying ability of monoglycerides is used in cosmetic, pharmaceutical, and food production. The process of fatty acid monoglycerides obtaining by the reaction of vegetable hydrogenated fat (salomas) with glycerol (glycerolysis method) has been studied. Potassium glycerate is used as a catalyst, which is characterized by high efficiency and safety of production and use. A feature of the work is the study of the dependence of the yield and melting point of monoglycerides on the technological parameters of glycerolysis. As a raw material, hydrogenated refined fat according to DSTU 5040 (CAS Number 68334-28-1) was used: melting point – 48 °C, mass fraction of moisture and volatile substances – 0.08 %, acid value – 0.25 mg KOH/g, peroxide value – 2.8 ½ O mmol/kg. In all experiments, the glycerolysis temperature was 180 °C, the catalyst concentration – 0.5 % in terms of metal. Rational conditions for glycerolysis were determined: duration (90 min.) and glycerol concentration (50 %). Under these conditions, the monoglycerides yield was 32.9 %, melting point – 61.5 °C. The mass fraction of free glycerol in monoglycerides was 1.0 %, acid value – 2.2 mg KOH/g. The efficiency of monoglycerides obtaining using potassium hydroxide and glycerol mixture as a catalyst under certain rational conditions has been studied. The monoglycerides yield of 30.1 %, melting point of 59 °C were obtained. Therefore, the use of potassium glycerate catalyst is more efficient. The results of the study make it possible to improve the technology for the production of fatty acid monoglycerides using a new catalyst and use resources rationally.