17 research outputs found
Determination of Optimal Fluorine Leaching Parameters from the Coal Part of the Waste Lining of Dismantled Electrolytic Cells for Aluminum Production
When aluminum is obtained by electrolysis of cryolite-alumina melts when the baths are sent forΒ capital repairs, a solid technogenic product is formed β waste lining of electrolytic cells (WLEC). The volume of formation of WLEC is 30-50 kg per 1 ton of aluminum. Currently, it is mainly stored at landfills near industrial enterprises, causing harm to the environment. However, this technogenic raw material contains valuable components (fluorine, aluminum, sodium) that can be extracted to produce fluoride salts, which are in demand during the electrolytic production of aluminum. The objects of research were samples of the coal part of the waste lining of dismantled S-8BM (E) type electrolytic cells of Β«RUSAL KrasnoyarskΒ» JSC (Krasnoyarsk) of RUSAL company. According to the X-ray experiment diffraction analysis (using a Bruker D8 ADVANCE diffractometer) of the phase composition of the samples, it was found that the main fluorine-containing compounds are cryolite, chiolite, sodium and calcium fluorides. The total fluorineΒ contentΒ inΒ theΒ studiedΒ samplesΒ averagedΒ 13.1Β %.Β WeΒ conductedΒ studiesΒ onΒ theΒ leachingΒ of fluorine from WLEC with a solution of caustic alkali (NaOH concentration β 17.5 g/dm3). The process wasΒ carried out in a mechanically agitated reactor using a BIOSAN MM-1000 top drive laboratory stirrer with a two-blade nozzle. By the method of mathematical planning of a three-factor experiment, the mutual influence of three leaching conditions on the optimization parameter was established β the extraction of fluorine in solution (in percent). The maximum recovery of fluorine from WLEC to the leach solution averaged 86.4 % and was achieved with the following indicators:processtemperatureβ95Β°C,theratio ofliquidtosolidphaseβ9:1,durationβ 210 min
The Commercialization of Genetic Research: A Pilot Study
With the development of molecular genetics, the field of personalized medicine based on genetic data has been growing at a phenomenal pace. Genetic tests can identify health risks, ancestry, and genealogy, as well as the prediction of drug responses. However, very limited research exists about the marketing practices of companies, which promote and sell DNA ancestry and health-related genetic tests directly to the public.Aim. To evaluate the awareness and attitude about genetic testing in the population of a large industrial city in Russia (on the example of Irkutsk).Materials and methods. A total of 305 respondents β 265 of them were students of higher educational institutions of Irkutsk. The study was conducted on condition of anonymity. The questionnaire was available on the Internet on the basis of the Google Forms service. All basic concepts were explained to the participants during the survey.Results. 94.1 % are interested in conducting genetic testing on a commercial basis. Of the total number of survey participants, 72.8 % expressed a desire to undergo the analysis βHereditary predisposition to diseasesβ, 61 % β βMonogenic diseasesβ, 52.1 % β βEthnoβ. In addition, out of the total number of respondents surveyed, 36.7 % want to undergo genetic testing for research: features of metabolism and food intolerance βDietβ, 22 % β susceptibility to injuries and speed of recovery of physical form βSportβ, 18 % β to hereditarily determined susceptibility to drugs βPharmacyβ. It follows from the answers that the greatest interest among the surveyed people is the determination of predisposition to cardiovascular diseases β 72.5 %, to Alzheimerβs disease β 48.3 % and diabetes mellitus β 40.3 %.Conclusion. The results obtained indicate an interest in the study of predisposition to cardiovascular and neurodegenerative diseases. There is a high need to analyze the assessment of the clinical usefulness of genetic research, to assess the impact of research results on human behavior and the system of regulation of genetic testing in healthcare in general
Assessment of reference intervals of acylcarnitines in newborns inΒ Siberia
Background. The incidence of diseases associated with impaired transport and oxidation of fatty acids is from 1:5,000 to 1:9,000 newborns. High morbidity, risk of death in the absence of timely correction, non-specificity of clinical manifestations define the importance of their timely laboratory diagnosis based on the determination of free carnitine and acylcarnitines in the blood. Reference values for free carnitine and acylcarnitines vary in different populations.Β Β The aim. To determine the reference intervals of free carnitine and acylcarnitines in newborns of the Irkutsk region and to compare them with similar reference intervals in newborns in other countries.Β Β Methods. The analysis of 229 samples of drΡ blood spots of healthy newborn children of the Irkutsk region aged from 0 to 7 days was carried out. Analysis of acylcarnitine concentrations was performed using high performance liquid chromatography with tandem mass spectrometry.Β Β Results. 2.5 and 97.5 percentiles (Β΅mol/l) were calculateed for 13 acylcarnitines: C0 β [8.78; 38.08]; C2 β [3.55; 19.09]; C3 β [0.33; 1.96]; C4 β [0.08; 0.51]; C5 β [0.06; 0.44]; C5DC β [0.03; 0.17]; C6 β [0.01; 0.07]; C8 β [0.01; 0.07]; C10 β [0.02; 0.07]; C12 β [0.04; 0.51]; C14 β [0.07; 0.24]; C16 β [0.58; 3.25]; C18 β [0.35; 1.16].Β Β Conclusion. Differences in acylcarnitine reference intervals were found: compared with other countries, the concentrations of reference intervals for C0, C2, C3, C5DC, C8, C10, C14, C16 and C18 were lower in our study, reference intervals for C5 and C12 were higher in our country
EXPERIENCE OF INTEGRATED USE OF GOLD-BEARING RAW MATERIAL IN THE PRODUCTION OF PRECIOUS METALS
With the depletion of rich gold-bearing ores, the processing started to use polymetallic ores, which, in addition to precious metals, contain other elements that could be valuable after recovery. The problem of using such ores is extremely difficult because of the high cost of recovery of associated valuable components. The paper presents the results of studies on the integrated use of extracted gold-bearing raw materials based on the example of the Berezitovoye deposit (Amurskaya oblast), they have low content of precious metals and many heavy non-ferrous metals (copper, lead). Experimental work was carried out to obtain copper by the method of cementation from solutions formed after the leaching of the impurities of gold-containing cathode deposits with hydrochloric acid. The cementing metal was iron turnings (waste products of the turning shop of the enterprise). Next, it was proposed to use cemented copper as a collector during re-melting of slags β wastes of processing of low-grade polymetallic ores containing precious metals. The authors obtained ingots of alloyed gold with gold weight fraction of 16 %, which meets the requirements of TU 117-2-7-75 on the content of non-ferrous metals. During hydrochloric acid treatment of cathodic deposits silver partially passed into the solution, it was recovered together with cemented copper and, in subsequent melting, passed into alloyed gold. Thus, the method proposed by the authors helps to reduce the content of precious metals in the Β«incomplete production cycleΒ» of the gold recovery factory. The opportunity of selling the cementation copper at the enterprises specializing on manufacturing of jewels is shown, the expected economic effect at the same time amounted to more than 1.8 million rubles
ΠΠΈΠ½Π΅ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΎΡΠ΅Π½ΠΊΠ° Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ Π²ΠΎΡΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΈΡ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ ΠΈ ΠΌΠ°Π³Π½ΠΈΡ ΠΈΠ· Π²ΠΎΠ΄Π½ΡΡ ΡΠ°ΡΡΠ²ΠΎΡΠΎΠ² ΠΈΡ ΡΠΎΠ»Π΅ΠΉ ΠΊΠ°ΠΊ Π°Π»ΡΡΠ΅ΡΠ½Π°ΡΠΈΠ²Π° ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΠ·Ρ ΡΠ°ΡΠΏΠ»Π°Π²ΠΎΠ²
In the non-ferrous metal industry a unique position is given to electrolytic production as being one of the most energy-consuming and environmentally dangerous technologies. Thus, for example, obtaining aluminum by cryolite-alumina melt electrolysis is accompanied by the atmospheric emissions of fluorine-, sulphur-containing substances and hydrocarbons, and magnesium production β by the emission of chlorine and organochlorine compounds. By present time those suggestions in terms of aluminum and magnesium production are considered relevant that are aimed at improving the environmental situation in the vicinity of metallurgical plants. Despite the fact that existing aluminum and magnesium production technologies are under favorable conditions for development and can be really adopted at existing plants, there are ideas and suggestions appearing to create new technologies based on scientific advances in electrolytic light metal production. The authors used magnesium and aluminum as research objects. They considered interaction between metals and aqueous solutions of their salts β MgSO4, MgCl2, Al2(SO4)3, AlCl3 chlorides and sulfates. It is shown that such interactions always take place in a diffuse area that provide for using various design solutions when selecting the process instrumentation. Experimental data were used to determine the reaction order with respect to the solvent, speed and activation energy constants. The results prove the assumption that it is preferable to use chloride media facilitating the process course based on primary electrode reactions and excluding any auxiliary interactions. It is demonstrated that chloride solutions can serve as operating electrolytes and can carry the recovered metal ions. At the same time electrolytic saturation guarantees the impossibility of a reversible process β secondary metal melt which leads to reducing the main indicators of cryolite-alumina melt electrolysis.Π ΠΌΠ΅ΡΠ°Π»Π»ΡΡΠ³ΠΈΠΈ ΡΠ²Π΅ΡΠ½ΡΡ
ΠΌΠ΅ΡΠ°Π»Π»ΠΎΠ² ΠΎΡΠΎΠ±ΠΎΠ΅ ΠΌΠ΅ΡΡΠΎ Π·Π°Π½ΠΈΠΌΠ°ΡΡ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠΈΡΠ΅ΡΠΊΠΈΠ΅ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π°, ΠΎΡΠ½ΠΎΡΡΡΠΈΠ΅ΡΡ ΠΊ Π½Π°ΠΈΠ±ΠΎΠ»Π΅Π΅ ΡΠ½Π΅ΡΠ³ΠΎΠ΅ΠΌΠΊΠΈΠΌ ΠΈ ΡΠΊΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠΈ Π½Π΅Π±Π΅Π·ΠΎΠΏΠ°ΡΠ½ΡΠΌ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡΠΌ. Π’Π°ΠΊ, Π½Π°ΠΏΡΠΈΠΌΠ΅Ρ, ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΠ΅ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΠ·ΠΎΠΌ ΠΊΡΠΈΠΎΠ»ΠΈΡ-Π³Π»ΠΈΠ½ΠΎΠ·Π΅ΠΌΠ½ΡΡ
ΡΠ°ΡΠΏΠ»Π°Π²ΠΎΠ² ΡΠΎΠΏΡΠΎΠ²ΠΎΠΆΠ΄Π°Π΅ΡΡΡ Π²ΡΠ±ΡΠΎΡΠ°ΠΌΠΈ Π² Π°ΡΠΌΠΎΡΡΠ΅ΡΡ ΡΡΠΎΡ-, ΡΠ΅ΡΠΎΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΡ
Π²Π΅ΡΠ΅ΡΡΠ² ΠΈ ΡΠ³Π»Π΅Π²ΠΎΠ΄ΠΎΡΠΎΠ΄ΠΎΠ², ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²ΠΎ ΠΌΠ°Π³Π½ΠΈΡ β Ρ
Π»ΠΎΡΠ° ΠΈ Ρ
Π»ΠΎΡΠΎΡΠ³Π°Π½ΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠΎΠ΅Π΄ΠΈΠ½Π΅Π½ΠΈΠΉ. Π Π½Π°ΡΡΠΎΡΡΠ΅ΠΌΡ Π²ΡΠ΅ΠΌΠ΅Π½ΠΈ Π°ΠΊΡΡΠ°Π»ΡΠ½ΡΠΌΠΈ ΡΠ»Π΅Π΄ΡΠ΅Ρ ΡΡΠΈΡΠ°ΡΡ Π»ΡΠ±ΡΠ΅ ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½ΠΈΡ Π² ΠΎΠ±Π»Π°ΡΡΠΈ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° ΡΠ°ΠΊΠΈΡ
ΠΌΠ΅ΡΠ°Π»Π»ΠΎΠ², ΠΊΠ°ΠΊ Π°Π»ΡΠΌΠΈΠ½ΠΈΠΉ ΠΈ ΠΌΠ°Π³Π½ΠΈΠΉ, Π½Π°ΠΏΡΠ°Π²Π»Π΅Π½Π½ΡΠ΅ Π½Π° ΡΠ»ΡΡΡΠ΅Π½ΠΈΠ΅ ΡΠΊΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΡΠΈΡΡΠ°ΡΠΈΠΈ Π²Π±Π»ΠΈΠ·ΠΈ ΡΠ°ΡΠΏΠΎΠ»ΠΎΠΆΠ΅Π½ΠΈΡ ΠΌΠ΅ΡΠ°Π»Π»ΡΡΠ³ΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΡΠ΅Π΄ΠΏΡΠΈΡΡΠΈΠΉ. ΠΠ΅ΡΠΌΠΎΡΡΡ Π½Π° ΡΠΎ, ΡΡΠΎ ΡΠΎΠ²Π΅ΡΡΠ΅Π½ΡΡΠ²ΠΎΠ²Π°Π½ΠΈΠ΅ ΡΡΡΠ΅ΡΡΠ²ΡΡΡΠΈΡ
ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΠΉ ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ ΠΈ ΠΌΠ°Π³Π½ΠΈΡ ΠΈΠΌΠ΅Π΅Ρ Π±Π»Π°Π³ΠΎΠΏΡΠΈΡΡΠ½ΡΠ΅ ΡΠ΅Π½Π΄Π΅Π½ΡΠΈΠΈ ΡΠ°Π·Π²ΠΈΡΠΈΡ ΠΈ ΡΠ΅Π°Π»ΡΠ½ΡΠ΅ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ Π²Π½Π΅Π΄ΡΠ΅Π½ΠΈΡ Π½Π° Π΄Π΅ΠΉΡΡΠ²ΡΡΡΠΈΡ
ΠΏΡΠ΅Π΄ΠΏΡΠΈΡΡΠΈΡΡ
, Π²ΠΎΠ·Π½ΠΈΠΊΠ°ΡΡ ΠΈΠ΄Π΅ΠΈ ΠΈ ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½ΠΈΡ ΠΏΠΎ ΡΠΎΠ·Π΄Π°Π½ΠΈΡ Π½ΠΎΠ²ΡΡ
ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΠΉ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π½Π°ΡΡΠ½ΡΡ
Π΄ΠΎΡΡΠΈΠΆΠ΅Π½ΠΈΠΉ Π² ΠΎΠ±Π»Π°ΡΡΠΈ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π»Π΅Π³ΠΊΠΈΡ
ΠΌΠ΅ΡΠ°Π»Π»ΠΎΠ². Π ΠΊΠ°ΡΠ΅ΡΡΠ²Π΅ ΠΎΠ±ΡΠ΅ΠΊΡΠΎΠ² ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΡ ΠΏΡΠΈΠΌΠ΅Π½ΡΠ»ΠΈ ΠΌΠ°Π³Π½ΠΈΠΉ ΠΈ Π°Π»ΡΠΌΠΈΠ½ΠΈΠΉ. Π Π°ΡΡΠΌΠΎΡΡΠ΅Π½ΠΎ Π²Π·Π°ΠΈΠΌΠΎΠ΄Π΅ΠΉΡΡΠ²ΠΈΠ΅ ΠΌΠ΅ΡΠ°Π»Π»ΠΎΠ² Ρ Π²ΠΎΠ΄Π½ΡΠΌΠΈ ΡΠ°ΡΡΠ²ΠΎΡΠ°ΠΌΠΈ ΠΈΡ
ΡΠΎΠ»Π΅ΠΉ β Ρ
Π»ΠΎΡΠΈΠ΄Π°ΠΌΠΈ ΠΈ ΡΡΠ»ΡΡΠ°ΡΠ°ΠΌΠΈ MgSO4, MgCl2, Al2(SO4)3, AlCl3. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ ΡΠ°ΠΊΠΈΠ΅ Π²Π·Π°ΠΈΠΌΠΎΠ΄Π΅ΠΉΡΡΠ²ΠΈΡ Π²ΡΠ΅Π³Π΄Π° ΠΏΡΠΎΡΠ΅ΠΊΠ°ΡΡ Π² Π΄ΠΈΡΡΡΠ·ΠΈΠΎΠ½Π½ΠΎΠΉ ΠΎΠ±Π»Π°ΡΡΠΈ, ΡΡΠΎ ΠΎΡΠΊΡΡΠ²Π°Π΅Ρ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΡ ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΠΊΠΎΠ½ΡΡΡΡΠΊΡΠΈΠ²Π½ΡΡ
ΡΠ΅ΡΠ΅Π½ΠΈΠΉ ΠΏΡΠΈ Π²ΡΠ±ΠΎΡΠ΅ Π°ΠΏΠΏΠ°ΡΠ°ΡΡΡΠ½ΠΎΠ³ΠΎ ΠΎΡΠΎΡΠΌΠ»Π΅Π½ΠΈΡ ΠΏΡΠΎΡΠ΅ΡΡΠ°. ΠΠ° ΠΎΡΠ½ΠΎΠ²Π΅ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΡΡ
Π΄Π°Π½Π½ΡΡ
Π½Π°ΠΉΠ΄Π΅Π½Ρ ΠΏΠΎΡΡΠ΄ΠΎΠΊ ΡΠ΅Π°ΠΊΡΠΈΠΈ ΠΏΠΎ ΡΠ°ΡΡΠ²ΠΎΡΠΈΡΠ΅Π»Ρ, ΠΊΠΎΠ½ΡΡΠ°Π½ΡΡ ΡΠΊΠΎΡΠΎΡΡΠΈ ΠΈ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Π°ΠΊΡΠΈΠ²Π°ΡΠΈΠΈ. ΠΠΎΠ»ΡΡΠ΅Π½Π½ΡΠ΅ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ Π΄ΠΎΠΊΠ°Π·ΡΠ²Π°ΡΡ ΠΏΡΠ΅Π΄ΠΏΠΎΡΡΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΡ ΠΏΡΠΈΠΌΠ΅Π½Π΅Π½ΠΈΡ Ρ
Π»ΠΎΡΠΈΠ΄Π½ΡΡ
ΡΡΠ΅Π΄, ΠΎΠ±Π΅ΡΠΏΠ΅ΡΠΈΠ²Π°ΡΡΠΈΡ
ΠΏΡΠΎΡΠ΅ΠΊΠ°Π½ΠΈΠ΅ ΠΏΡΠΎΡΠ΅ΡΡΠ° Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π±Π°Π·ΠΎΠ²ΡΡ
ΡΠ»Π΅ΠΊΡΡΠΎΠ΄Π½ΡΡ
ΡΠ΅Π°ΠΊΡΠΈΠΉ ΠΈ ΠΈΡΠΊΠ»ΡΡΠ°ΡΡΠΈΡ
Π²ΠΎΠ·Π½ΠΈΠΊΠ½ΠΎΠ²Π΅Π½ΠΈΠ΅ ΠΏΠΎΠ±ΠΎΡΠ½ΡΡ
Π²Π·Π°ΠΈΠΌΠΎΠ΄Π΅ΠΉΡΡΠ²ΠΈΠΉ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ Ρ
Π»ΠΎΡΠΈΠ΄Π½ΡΠ΅ ΡΠ°ΡΡΠ²ΠΎΡΡ ΠΌΠΎΠ³ΡΡ ΡΠ»ΡΠΆΠΈΡΡ ΡΠ°Π±ΠΎΡΠΈΠΌΠΈ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ°ΠΌΠΈ ΠΈ Π±ΡΡΡ Π½ΠΎΡΠΈΡΠ΅Π»ΡΠΌΠΈ ΠΈΠΎΠ½ΠΎΠ² Π²ΠΎΡΡΡΠ°Π½Π°Π²Π»ΠΈΠ²Π°Π΅ΠΌΠΎΠ³ΠΎ ΠΌΠ΅ΡΠ°Π»Π»Π°. ΠΡΠΈ ΡΡΠΎΠΌ Π½Π°ΡΡΡΠ΅Π½ΠΈΠ΅ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ° ΡΠ²Π»ΡΠ΅ΡΡΡ Π³Π°ΡΠ°Π½ΡΠΈΠ΅ΠΉ Π½Π΅Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ ΠΎΠ±ΡΠ°ΡΠΈΠΌΠΎΠ³ΠΎ ΠΏΡΠΎΡΠ΅ΡΡΠ° β Π²ΡΠΎΡΠΈΡΠ½ΠΎΠ³ΠΎ ΡΠ°ΡΡΠ²ΠΎΡΠ΅Π½ΠΈΡ ΠΌΠ΅ΡΠ°Π»Π»Π°, ΡΡΠΎ ΠΏΡΠΈΠ²ΠΎΠ΄ΠΈΡ ΠΊ ΡΠ½ΠΈΠΆΠ΅Π½ΠΈΡ ΠΎΡΠ½ΠΎΠ²Π½ΡΡ
ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Π΅ΠΉ ΠΏΡΠΎΡΠ΅ΡΡΠ° ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΠ·Π° ΠΊΡΠΈΠΎΠ»ΠΈΡ-Π³Π»ΠΈΠ½ΠΎΠ·Π΅ΠΌΠ½ΡΡ
ΡΠ°ΡΠΏΠ»Π°Π²ΠΎΠ²
Low-Modulus Cryolite Production Methods Using Anode Gas Cleaning Solutions of Aluminum Smelting
Π ΡΡΠ°ΡΡΠ΅ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½Ρ ΡΠΏΠΎΡΠΎΠ±Ρ ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΠΎΠ³ΠΎ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π½ΠΈΠ·ΠΊΠΎΠΌΠΎΠ΄ΡΠ»ΡΠ½ΠΎΠ³ΠΎ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ°
(ΠΠΠ). ΠΠ΅ΡΠ²ΡΠΉ ΡΠΏΠΎΡΠΎΠ± β ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΠ΅ ΠΠΠ ΠΏΡΡΠ΅ΠΌ ΠΊΡΠΈΡΡΠ°Π»Π»ΠΈΠ·Π°ΡΠΈΠΈ Ρ
ΠΈΠΎΠ»ΠΈΡΠ° ΠΈ ΡΡΠΎΡΠΈΡΡΠΎΠ³ΠΎ
Π°Π»ΡΠΌΠΈΠ½ΠΈΡ. ΠΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΡΠ΅ Π΄Π°Π½Π½ΡΠ΅ ΠΏΠΎΠΊΠ°Π·Π°Π»ΠΈ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ ΠΊΠ°ΠΊ ΡΡΠΎΡΠΈΡΡΠΎΠ³ΠΎ
Π°Π»ΡΠΌΠΈΠ½ΠΈΡ, ΡΠ°ΠΊ ΠΈ Π½ΠΈΠ·ΠΊΠΎΠΌΠΎΠ΄ΡΠ»ΡΠ½ΠΎΠ³ΠΎ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° ΠΈΠ· ΠΊΠΈΡΠ»ΡΡ
ΡΠ°ΡΡΠ²ΠΎΡΠΎΠ² Π³Π°Π·ΠΎΠΎΡΠΈΡΡΠΊΠΈ. ΠΡΠΎΡΠΎΠΉ ΡΠΏΠΎΡΠΎΠ± β
ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΠ΅ ΠΠΠ ΠΏΡΡΠ΅ΠΌ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠΈ ΡΠ΅Π³Π΅Π½Π΅ΡΠ°ΡΠΈΠΎΠ½Π½ΠΎΠ³ΠΎ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° ΡΠ°ΡΡΠ²ΠΎΡΠ°ΠΌΠΈ Π³Π°Π·ΠΎΠΎΡΠΈΡΡΠΊΠΈ
Ρ Π΄ΠΎΠ±Π°Π²Π»Π΅Π½ΠΈΠ΅ΠΌ Π²ΠΎΠ΄Π½ΠΎΠΉ ΡΡΡΠΏΠ΅Π½Π·ΠΈΠΈ Π³ΠΈΠ΄ΡΠΎΠΊΡΠΈΠ΄Π° Π°Π»ΡΠΌΠΈΠ½ΠΈΡ. ΠΠΎ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠ°ΠΌ Π»Π°Π±ΠΎΡΠ°ΡΠΎΡΠ½ΡΡ
ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠΉ Π΄ΠΎΠΊΠ°Π·Π°Π½Π° Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ Π²ΡΠΎΡΠΈΡΠ½ΠΎΠ³ΠΎ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° Ρ Π·Π°Π΄Π°Π½Π½ΡΠΌ ΠΊΡΠΈΠΎΠ»ΠΈΡΠΎΠ²ΡΠΌ
ΠΎΡΠ½ΠΎΡΠ΅Π½ΠΈΠ΅ΠΌ (ΠΠ) Π·Π° ΡΡΡΡ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΡ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² ΠΎΡΠΌΡΠ²ΠΊΠΈ ΡΠ΅Π³Π΅Π½Π΅ΡΠ°ΡΠΈΠΎΠ½Π½ΠΎΠ³ΠΎ
ΠΊΡΠΈΠΎΠ»ΠΈΡΠ°. ΠΠ²ΡΠΎΡΠ°ΠΌΠΈ ΡΠ°ΠΊΠΆΠ΅ Π±ΡΠ»ΠΈ ΠΏΡΠΎΠ²Π΅Π΄Π΅Π½Ρ ΠΎΠΏΡΡΠ½ΠΎ-ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΡΠ΅ ΠΈΡΠΏΡΡΠ°Π½ΠΈΡ ΠΎΡΠΌΡΠ²ΠΊΠΈ
ΡΠ΅Π³Π΅Π½Π΅ΡΠ°ΡΠΈΠΎΠ½Π½ΠΎΠ³ΠΎ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° Π³Π΅ΠΊΡΠ°ΡΡΠΎΡΠ°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΠΎΠΉ ΠΊΠΈΡΠ»ΠΎΡΠΎΠΉ, ΠΏΠΎΠ»ΡΡΠ΅Π½Π½ΠΎΠΉ Π² ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΡΡ
ΡΡΠ»ΠΎΠ²ΠΈΡΡ
Ρ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠ΅ΠΌ ΠΈΠ½Π³ΠΈΠ±ΠΈΡΠΎΡΠΎΠ² ΠΊΠΎΡΡΠΎΠ·ΠΈΠΈThe article deals with the methods of low-modulus cryolite production (LMC). The first method is
to produce LMC by chiolite and aluminum fluoride crystallization. The experimental data indicated
that both aluminum fluoride and LMC can be produced from acid gas cleaning solutions. The second
method is to produce LMC by handling regeneration cryolite with gas cleaning solutions with addition
of an aqueous slurry of aluminum hydrate. Laboratory tests proved the possibility of producing
secondary cryolite with a preselected CD by changing the technological parameters of washing off of
regeneration cryolite. The authors also carried out pilot tests of washing off of regeneration cryolite
with hexafluoro-aluminum acid commercially produced using corrosion inhibitor