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Nickel-containing catalysts for ethylene conversion to motor fuel components and light alkenes 将乙烯转化为汽车燃料成分和轻烯的含镍催化剂
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-26-33
T. R. Karpova, A. V. Lavrenov, M. Moiseenko, E. A. Buluchevskii, T. Gulyaeva, A. Arbuzov
Polyfunctional Ni-containing catalysts supported on the B2O3-Al2O3 and MoO3-Al2O3 were prepared by a sequential impregnation. They were evaluated in ethylene conversion to C5+ alkenes or propylene. The catalysts were characterized by X-ray diffraction, Fourier transformed infrared spectroscopy, Fourier transformed infrared spectroscopy of adsorbed CO, UV-VIS diffuse reflectance spectroscopy, temperature programmed reduction and temperature-programmed desorption of NH3. NiO/B2O3-Al2O3 samples containing Ni2+ cations chemically bonded to the acid support are the most effective catalysts for ethylene oligomerization. The NiO/MoO3-Al2O3 catalyst activity in the ethylene conversion to propylene is related with the presence of ethylene dimerization active sites, i.e. Ni2+ cations bonded to the support acidic sites, and active sites of metathesis in the form of monomolybdate species.
通过顺序浸渍法制备了以 B2O3-Al2O3 和 MoO3-Al2O3 为载体的多官能团含镍催化剂。在乙烯转化为 C5+ 烯烃或丙烯的过程中对这些催化剂进行了评估。通过 X 射线衍射、傅立叶变换红外光谱、吸附 CO 的傅立叶变换红外光谱、紫外可见光漫反射光谱、NH3 的温度编程还原和温度编程解吸对催化剂进行了表征。含有与酸性载体化学键合的 Ni2+ 阳离子的 NiO/B2O3-Al2O3 样品是最有效的乙烯低聚催化剂。在乙烯转化为丙烯的过程中,NiO/MoO3-Al2O3 催化剂的活性与乙烯二聚化活性位点(即与载体酸性位点结合的 Ni2+ 阳离子)以及以单钼酸盐形式存在的偏聚活性位点有关。
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引用次数: 0
Study of the influence of the gas circulation ratio on the production of C5–C18 alkenes in the Fischer–Tropsch synthesis 研究气体循环比对费托合成生产 C5-C18 烯烃的影响
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-34-42
I. Zubkov, O. D. Denisov, M. A. Timokhina, A. Savost’yanov, R. Yakovenko
The process of producing C5+ hydrocarbons, including unsaturated ones, on a zeolite-containing catalyst Сo-Al2O3 /SiO2 /ZSM-5/Al2O3 in flow and flow-circulation modes of operation at a temperature of 250 °C, a pressure of 2.0 MPa, GHSV 1000 h–1 has been studied , H2 /CO ratio = 1.70 in the source gas and circulation ratios of 4, 8 and 16. It was determined that the process indicators (selectivity and productivity for C5+ products) pass through a maximum at a circulation ratio of 8. The use of gas circulation in comparison with flow synthesis mode allows you to regulate the composition of products. An increase in the circulation ratio in the range of 4–16 leads to an increase in the proportion of formed olefins with a hydrocarbon chain length containing 5–20 carbon atoms, from 53.9 wt.% up to 65.7 wt.%. The use of a zeolite-containing catalyst intensifies the formation of C8–C12 alkenes in comparison with the Co-Al2O3 /SiO2 catalyst by 3,3 times – the content increases from 13,5 wt.% up to 44.2 wt.% at similar values of circulation ratio, pressure and H2 /CO ratio = 1.70 in the source gas. It was found that as the circulation ratio increases, the rate of deactivation of the zeolite-containing catalyst decreases, which may be caused by a decrease in the partial pressure of water in the reaction volume.
在温度为 250 °C、压力为 2.0 MPa、GHSV 为 1000 h-1 的条件下,在源气中 H2 /CO 的比例为 1.70,循环比为 4、8 和 16 的情况下,研究了含沸石催化剂 Сo-Al2O3 /SiO2 /ZSM-5/Al2O3 在流动和流动-循环操作模式下生产 C5+ 碳氢化合物(包括不饱和碳氢化合物)的工艺。结果表明,循环比为 8 时,工艺指标(C5+ 产品的选择性和生产率)达到最大值。与流动合成模式相比,使用气体循环可以调节产品的成分。循环比在 4-16 之间时,烃链长度为 5-20 个碳原子的烯烃比例从 53.9% 增加到 65.7%。与 Co-Al2O3 /SiO2 催化剂相比,使用含沸石催化剂可将 C8-C12 烯烃的生成量提高 3.3 倍--在循环比、压力和源气体中 H2 /CO 的比例 = 1.70 的相似值条件下,其含量从 13.5 wt.% 提高到 44.2 wt.%。研究发现,随着循环比的增加,含沸石催化剂的失活率降低,这可能是由于反应体积中水的分压降低所致。
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引用次数: 0
Variation of the shapes of catalytic blocks in the autothermal reforming of hexadecane, propane and methane using mathematical modeling 利用数学建模改变十六烷、丙烷和甲烷自热转化过程中催化块的形状
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-51-58
S. Zazhigalov, V. A. Shilov, A. Zagoruiko, P. Snytnikov
In this work, mathematical modeling of the autothermal reforming of hexadecane, propane and methane on catalytic blocks of different geometric shapes was carried out. It was shown that the convex shape of the block towards the oncoming reaction flow can increase the maximum temperature in the frontal zone, while the concave shape contributes to a more uniform temperature distribution along the entire length of the catalytic layer. The work also investigated the effect of the reaction flow rate on the change in the temperature gradient, which can subsequently be used to prevent the formation of hot spots and catalyst deactivation. The results obtained can serve as the basis for future research in the field of autothermal reforming and optimization of the geometric parameters of catalysts for the conversion of hydrocarbon fuels into synthesis gas.
在这项研究中,对不同几何形状的催化块上十六烷、丙烷和甲烷的自热重整进行了数学建模。结果表明,催化块朝向迎面而来的反应流的凸面形状可提高正面区域的最高温度,而凹面形状则可使催化层整个长度上的温度分布更加均匀。这项工作还研究了反应流速对温度梯度变化的影响,温度梯度变化可用于防止形成热点和催化剂失活。所获得的结果可作为今后在自热转化领域开展研究和优化将烃类燃料转化为合成气的催化剂几何参数的基础。
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引用次数: 0
The use of microalgae biomass for the production of marketable products. Part 6: Bioplastic from microalgae 利用微藻生物质生产适销产品。第 6 部分:微藻生物塑料
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-76-84
Y. V. Samoylova, K. N. Sorokina, V. N. Parmon
This article is part of a series of reviews devoted to the using microalgae biomass to obtain widely used products. In this review, microalgae are considered as a potential and renewable feedstock for producing functional materials that have found their application in the polymer industry. Strong, stable and biodegradable bioplastics from microalgae are an alternative to traditional petroleumbased plastics. The ways of obtaining bioplastics from microalgae, using the biomass directly (polyhydroxyalkanoates, starch, cellulose, organic acids), as well as using it blending with other polymers, are considered. Data are presented on the prospects of using bioplastics from microalgae, including as a result of biomass biorefinery.
本文是关于利用微藻生物质获得广泛应用产品的系列综述的一部分。在这篇综述中,微藻被视为生产功能材料的潜在可再生原料,这些功能材料已在聚合物行业中得到应用。来自微藻的强韧、稳定和可生物降解的生物塑料是传统石油基塑料的替代品。本文探讨了从微藻中获取生物塑料的方法,包括直接使用生物质(聚羟基烷酸酯、淀粉、纤维素、有机酸)以及与其他聚合物混合使用。数据显示了使用微藻生物塑料的前景,包括作为生物质生物精炼的结果。
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引用次数: 0
Industrial aluminum hydroxides: Part 1. Phase composition and textural characteristics of industrial aluminum hydroxides/oxides 工业氢氧化铝:第 1 部分。工业氢氧化铝/氧化物的相组成和纹理特征
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-6-14
A. P. Bebyakina, M. I. Farid, A. Boretskaya, S. Egorova, A. Lamberov
The most common component in the design of heterogeneous catalysts for oil refining and petrochemistry are aluminum oxides. Each type of hydrocarbon raw materials and technological process corresponds to the optimal characteristics of aluminum oxide supports and catalysts: specific surface area, pore size, phase and impurity compositions. Due to the trend towards import substitution, the research of domestic producers of aluminum hydroxide used for the synthesis of aluminum oxides is becoming more relevant. In this work, domestic industrial samples of aluminum hydroxides were studied by methods of X-ray phase analysis, thermogravimetry combined with differential scanning calorimetry, low-temperature nitrogen adsorption and elemental analysis. It is established that the objects of research are most often phase-inhomogeneous, in which impurities of iron, silicon and calcium are present. The influence of the degree of crystallization and the size of the coherent scattering regions of aluminum hydroxides, mainly with the structure of boehmite and, in some cases, containing bayerite, on the textural characteristics of the resulting aluminum oxides is shown.
在炼油和石油化学的异相催化剂设计中,最常见的成分是氧化铝。每种类型的碳氢化合物原料和技术工艺都对应着氧化铝载体和催化剂的最佳特性:比表面积、孔径、相和杂质成分。由于进口替代的趋势,对国内用于合成氧化铝的氢氧化铝生产商的研究变得越来越重要。本研究采用 X 射线相分析法、热重法结合差示扫描量热法、低温氮吸附法和元素分析法对国内氢氧化铝工业样品进行了研究。研究结果表明,研究对象多为均相物,其中存在铁、硅和钙等杂质。结晶程度和铝氢氧化物相干散射区的大小(主要是波来石结构,在某些情况下含有贝叶石)对所得铝氧化物纹理特征的影响显而易见。
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引用次数: 0
Co and Ni-containing catalysts for heavy oil refining: the effect of ethanol on the composition and structure of catalytic cracking products 用于重油炼制的含钴和含镍催化剂:乙醇对催化裂化产品成分和结构的影响
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-59-65
K. K. Urazov, N. Sviridenko, N. S. Sergeev, A. S. Akimov, V. D. Ogorodnikov
The study deals with the products of thermal processing of heavy oil in the presence of Ni- and Co-containing catalysts that are formed in situ from the mixture of corresponding salts with ethanol. In comparison with thermal cracking, in the catalytic process the yield of bright fractions increases from 51 to 63 % and the yield of coke decreases from 3 to 2 wt.%. In the case of mixed Ni and Сo catalyst, the least yields of gas (5 wt.%) and coke (0.1 wt.%) are observed. A decrease in the sulfur content occurs in the products of both thermal (by 17 %) and catalytic cracking (from 12 to 32 rel.%) predominantly due to its removal as gaseous products. The structuralgroup characteristics of the averaged asphaltene molecules were studied before and after heavy oil cracking. XRD of solid cracking products was used to identify Ni0.96S, Ni9S8 and Co9S8 phases.
该研究涉及在含镍和钴催化剂存在下对重油进行热加工的产物,这些催化剂是由相应的盐与乙醇的混合物就地形成的。与热裂解相比,在催化过程中,光亮馏分的产量从 51% 增加到 63%,焦炭的产量从 3 wt.% 减少到 2 wt.%。在混合使用 Ni 和 Сo 催化剂的情况下,气体(5 重量百分比)和焦炭(0.1 重量百分比)的产量最低。热裂解(降低 17%)和催化裂化(从 12% 到 32%)产物中的硫含量都有所降低,主要是由于硫以气态产物的形式被去除。对重油裂解前后平均沥青质分子的结构组特性进行了研究。固体裂解产物的 XRD 被用来识别 Ni0.96S、Ni9S8 和 Co9S8 相。
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引用次数: 0
Experimental studies and mathematical modeling of the catalytic conversion of biodiesel fuel into synthesis gas 生物柴油燃料催化转化为合成气的实验研究和数学建模
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-43-50
V. A. Shilov, S. Zazhigalov, M. A. Burmatova, A. Zagoruiko, P. Snytnikov
In this work, steam reforming and autothermal reforming of methyl oleate (a model compound of biodiesel fuel) into synthesis gas on a structured Rh-containing catalyst were investigated. It has been shown that the conversion of methyl oleate proceeds through the stage of thermal cracking followed by the conversion of the resulting organic compounds with a shorter carbon skeleton. Based on the experimental results, a mathematical model was developed that takes into account the radial temperature gradient and represents an effective tool for quantitatively describing and optimizing the biodiesel conversion process.
在这项工作中,研究了油酸甲酯(生物柴油燃料的一种模型化合物)在含 Rh 结构催化剂上进行蒸汽转化和自热转化为合成气的情况。实验结果表明,油酸甲酯的转化过程经历了热裂解阶段,然后转化为碳骨架较短的有机化合物。根据实验结果建立的数学模型考虑了径向温度梯度,是定量描述和优化生物柴油转化过程的有效工具。
{"title":"Experimental studies and mathematical modeling of the catalytic conversion of biodiesel fuel into synthesis gas","authors":"V. A. Shilov, S. Zazhigalov, M. A. Burmatova, A. Zagoruiko, P. Snytnikov","doi":"10.18412/1816-0387-2024-2-43-50","DOIUrl":"https://doi.org/10.18412/1816-0387-2024-2-43-50","url":null,"abstract":"In this work, steam reforming and autothermal reforming of methyl oleate (a model compound of biodiesel fuel) into synthesis gas on a structured Rh-containing catalyst were investigated. It has been shown that the conversion of methyl oleate proceeds through the stage of thermal cracking followed by the conversion of the resulting organic compounds with a shorter carbon skeleton. Based on the experimental results, a mathematical model was developed that takes into account the radial temperature gradient and represents an effective tool for quantitatively describing and optimizing the biodiesel conversion process.","PeriodicalId":17783,"journal":{"name":"Kataliz v promyshlennosti","volume":"107 S2","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-03-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140224554","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Oxidative chlorination of hydrocarbons. Part 1. The Deacon reaction. Oxidative chlorination of saturated hydrocarbons C1 and C2 碳氢化合物的氧化氯化。第 1 部分。迪肯反应。饱和碳氢化合物 C1 和 C2 的氧化氯化反应
Pub Date : 2024-01-23 DOI: 10.18412/1816-0387-2024-1-5-33
M. Flid
The review paper considers main regularities of the hydrogen chloride oxidation (the Deacon reaction) and oxidative chlorination of methane and ethane. The most efficient catalysts for these processes were shown to be the copper chloride systems on various supports, which contain also chlorides of alkaline and rare-earth metals that decrease the carry-over of the active phase from the catalyst surface and increase the activity. The main kinetic and technological regularities of the oxychlorination processes were considered. The conditions that promote an increase in the yield of target products – lower chloromethanes at oxychlorination of methane and vinyl chloride at oxychlorination of ethane – were revealed. Variants of technological schemes for the oxychlorination processes were proposed.
这篇综述论文探讨了甲烷和乙烷的氯化氢氧化(Deacon 反应)和氧化氯化的主要规律。研究表明,这些过程中最有效的催化剂是各种载体上的氯化铜体系,其中还含有碱金属和稀土金属的氯化物,可减少催化剂表面活性相的携带,提高催化剂的活性。研究考虑了氧氯化过程的主要动力学和技术规律。揭示了提高目标产品产量的条件--甲烷氧氯化时的低氯甲烷和乙烷氧氯化时的氯乙烯。提出了各种不同的氧氯化工艺技术方案。
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引用次数: 0
Photocatalytic oxidation of model organic dyes in the presence of Na+, NO2–, NO3– ions: theoretical and applied aspects 模型有机染料在 Na+、NO2-、NO3- 离子存在下的光催化氧化:理论与应用问题
Pub Date : 2024-01-23 DOI: 10.18412/1816-0387-2024-1-69-82
A. V. Zaitsev, V. P. Shesterkin, E. A. Kirichenko, M. S. Kruglov
The influence of the concentration of Na+, NO2–, NO3– ions on the rate of photocatalytic oxidation of model organic dyes was studied in the article: cationic – methylene blue (MB); anionic – methyl orange (MO). Based on studies of hydrochemical indicators of polluted rivers in urban areas (Khabarovsk, Russia) in the period from 1999 to 2019, it was shown that the concentration of ions varies in the ranges: 0.005–0.7 mg/l for NO2–; 0.05–15 mg/l for NO3–; 13–180 mg/l for Na+. Optical spectrophotometry was used to study the kinetics of photooxidation of MC and MO in the concentration ranges of the studied ions: 0–1–10–100–1000–10000 mg/l using P25 titanium oxide as a photocatalyst. The photooxidation time (t) was estimated at various values of the degree of transformation (α) of dyes at: initial – 10 %t; medium – 50 %t; final – 90 %t stages of the photocatalytic process. The effect of absorption of light quanta with wavelengths of 200–350 nm by Na+/NO2– and Na+/NO3– ions is shown depending on the concentrations of these ions in the photocatalytic solution. Recommendations for practical applications of the method of photocatalytic water purification of real polluted waters are given, showing the need to take into account the concentration of the studied ions. A description of the observed effect of ions on the rate of photocatalytic oxidation of model organic dyes is proposed from the point of view of the band structure of semiconductors, elements of the theory of electrolytic dissociation and recombination of free radicals in photocatalytic processes.
文章研究了 Na+、NO2-、NO3- 离子浓度对模型有机染料光催化氧化速率的影响:阳离子-亚甲基蓝(MB);阴离子-甲基橙(MO)。根据 1999 年至 2019 年期间对城市地区(俄罗斯哈巴罗夫斯克)受污染河流的水化学指标的研究表明,离子浓度在以下范围内变化:0.005-0.7 毫克/毫升,0.005-0.7 毫克/毫升,0.005-0.7 毫克/毫升,0.005-0.7 毫克/毫升:NO2- 为 0.005-0.7 毫克/升;NO3- 为 0.05-15 毫克/升;Na+ 为 13-180 毫克/升。光分光光度法用于研究 MC 和 MO 在所研究离子浓度范围内的光氧化动力学:使用 P25 氧化钛作为光催化剂,研究了 0-1-10-100-1000-10000 mg/l 浓度范围内 MC 和 MO 的光氧化动力学。在光催化过程的初始 - 10 %t;中期 - 50 %t;最终 - 90 %t 阶段,根据染料转化程度 (α)的不同值估算了光氧化时间 (t)。Na+/NO2- 和 Na+/NO3- 离子对波长为 200-350 纳米的光量子的吸收效果取决于光催化溶液中这些离子的浓度。对实际污染水域的光催化水净化方法的实际应用提出了建议,表明需要考虑所研究离子的浓度。从半导体的带状结构、光催化过程中的电解解离和自由基重组理论要素的角度,对观察到的离子对模型有机染料光催化氧化速率的影响进行了描述。
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引用次数: 0
Microwave-assisted synthesis of solketal from glycerol and acetone 微波辅助从甘油和丙酮中合成索酮醛
Pub Date : 2024-01-23 DOI: 10.18412/1816-0387-2024-1-60-68
V. A. Bolotov, A. E. Kibilyuk, V. N. Parmon, V. N. Panchenko, M. Timofeeva
Herein, microwave-assisted synthesis of solketal from glycerol and acetone in the presence of montmorillonite modified with aqueous solution of 0.25 mol/l HCl (0.25M HCl/MM) was demonstrated. The reaction was studied in a methanol solution at an acetone/glycerol molar ratio of 2.45–7.53, a catalyst concentration of 1.2–2.8 wt.% (based on the mass of loaded glycerol), and 30–56 °C. Solketal was shown to be the major product with 96.1–99.2 % selectivity. The maximum solketal yield of 91.3 % with 98.6 % selectivity was obtained in 15 min of the reaction at an acetone/glycerol molar ratio of 7.53, a catalyst loading of 2.3 wt.% and 56 °C. The catalytic properties of 0.25M HCl/MM in the reaction under MW heating and thermal conventional heating were compared. It was found that the yield of solketal in the MW-assisted synthesis is 2 times higher compared to the process with conventional heating.
本文展示了在用 0.25 摩尔/升盐酸水溶液(0.25M HCl/MM)修饰过的蒙脱石存在下,微波辅助从甘油和丙酮合成索酮醛的过程。研究在甲醇溶液中进行,丙酮/甘油摩尔比为 2.45-7.53,催化剂浓度为 1.2-2.8 wt.%(基于负载的甘油质量),温度为 30-56 °C。结果表明,主要产物为 Solketal,选择性为 96.1-99.2%。在丙酮/甘油摩尔比为 7.53、催化剂负载量为 2.3 wt.%、温度为 56 ℃ 的条件下,反应 15 分钟后可获得 91.3 % 的最高茄酮产量和 98.6 % 的选择性。比较了 0.25M HCl/MM 在 MW 加热和传统热加热条件下反应的催化特性。结果发现,与传统加热工艺相比,MW 辅助合成的 Solketal 收率高出 2 倍。
{"title":"Microwave-assisted synthesis of solketal from glycerol and acetone","authors":"V. A. Bolotov, A. E. Kibilyuk, V. N. Parmon, V. N. Panchenko, M. Timofeeva","doi":"10.18412/1816-0387-2024-1-60-68","DOIUrl":"https://doi.org/10.18412/1816-0387-2024-1-60-68","url":null,"abstract":"Herein, microwave-assisted synthesis of solketal from glycerol and acetone in the presence of montmorillonite modified with aqueous solution of 0.25 mol/l HCl (0.25M HCl/MM) was demonstrated. The reaction was studied in a methanol solution at an acetone/glycerol molar ratio of 2.45–7.53, a catalyst concentration of 1.2–2.8 wt.% (based on the mass of loaded glycerol), and 30–56 °C. Solketal was shown to be the major product with 96.1–99.2 % selectivity. The maximum solketal yield of 91.3 % with 98.6 % selectivity was obtained in 15 min of the reaction at an acetone/glycerol molar ratio of 7.53, a catalyst loading of 2.3 wt.% and 56 °C. The catalytic properties of 0.25M HCl/MM in the reaction under MW heating and thermal conventional heating were compared. It was found that the yield of solketal in the MW-assisted synthesis is 2 times higher compared to the process with conventional heating.","PeriodicalId":17783,"journal":{"name":"Kataliz v promyshlennosti","volume":"32 7","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-01-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"139603723","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
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Kataliz v promyshlennosti
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