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Оптимiзовано метод синтезу тонкодисперсного порошку ткеля, призначе-ного для виробництва твердих сплавiв, прямим електролiзом розчину амто-комплексу ткелю. Показано формуван-ня в оптимальтх умовах коралоподiбних частинок порошку розмiром 40-70 мкм, що легко тддаються розмолу до сферо-гдних складових. Визначено максималь-ну температуру електролту, показано позитивний вплив добавки Трилону Б на характеристики порошку. Визначено катодний та анодний вихи) за струмом
Ключовi слова: амнокомплекс ткелю, порошок шкелю, твердi сплави, дендрит, Трилон Б
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Оптимизирован метод синтеза тонкодисперсного порошка никеля, предназначенного для производства твердых сплавов, прямым электролизом раствора аминокомплекса никеля. Показано формирование в оптимальных условиях кораллоподобных частиц порошка размером 40-70 мкм, легко размалывающихся на сфероидные составляющие. Определена максимальная температура электролита, показано положительное влияние добавки Трилона Б на характеристику порошка. Определены катодный и анодный выходы по току
Ключевые слова: аминокомплекс никеля, порошок никеля, твердые сплавы, дендрит, Трилон Б -□ □-
UDC 54.057:544.653:621.13:661.13
|DOI: 10.15587/1729-4061.2018.121595]
DEFINITION OF SYNTHESIS PARAMETERS OF ULTRAFINE NICKEL POWDER BY DIRECT ELECTROLYSIS FOR APPLICATION IN SUPERALLOY PRODUCTION
V. Kovalenko
PhD, Associate Professor** Department of Analytical Chemistry and Food Additives and Cosmetics* Е-mail: vadimchem@gmail.com V. Kotok PhD, Associate Professor** Department of Processes, Apparatus and General Chemical Technology* Е-mail: valeriykotok@gmail.com S. Vlasov Doctor of Technical Sciences, Professor Department of underground mining National Mining University Yavornytskoho ave., 19, Dnipro, Ukraine, 49005 Department of building manufacture*** Е-mail: ocmy@ukr.net *Ukrainian State University of Chemical Technology Gagarina ave., 8, Dnipro, Ukraine, 49005 **Department of Technologies of Inorganic Substances and Electrochemical Manufacturing*** ***Vyatka State University Moskovskaya str., 36, Kirov, Russian Federation, 610000
1. Introduction
Ultrafine metal powders are used in various fields of engineering and manufacturing. Nickel powder, owing to its high electrical conductivity, catalytic and electrocatalytic properties, magnetic characteristics and high corrosion resistance is used for various applications. For instance, it is used for the preparation of special cement [1], as a catalyst [2], and for the preparation of colloids [3].
Ultrafine nickel powder is also necessary for the manufacturing of super alloys [4, 5], which are widely used in mining, aerospace and metal processing industries. Superalloys, which are also called pseudo-alloys are not true alloys but composite materials. Usually, composite materials of organic [6, 7], inorganic [8] or mixed organic-inorganic nature [9, 10] are composed of matrix material and filler material [11]. At the same time, superalloys have a different structure: the majority of hard material
particles are held together by a molten metal binder (Ni in particular).
Superalloys are prepared by means of powder metallurgy: a mixture of hard component and metal [12] (sometimes oxide of metal binder [13]) is sintered under pressure to obtain metal-ceramic workpieces. The described technology leads to special requirements for nickel powder. Primarily, it must be free from volatile compounds or metals (zinc, magnesium), as this can lead to the formation of caverns inside the formed workpiece. Powder particles size should be 5-50 |^m. Additionally the mixture of hard component and nickel is ground in alcohol before forming a workpiece, so another requirement for nickel powder is susceptibility to grinding.
The main parameters of superalloys are mechanical durability and stability at high temperatures [14]. In particular, these properties are important for application in the mining industry, and especially in the aerospace field [15]. Superalloys are used for the manufacturing of turbines for jet
and rocket engines. Thus, when manufacturing such critical parts, more stringent requirements are imposed on the composition of nickel powder, determined by synthesis methods and conditions [16].
2. Literature review and problem statement
When developing the method for preparing any material, the raw material is usually analyzed first and then the method is chosen with respect to the product requirements.
Based on principles of sustained development and the fact that nickel is a rather expensive metal, the best sources of nickel are various nickel-containing waste in various forms. Primarily, this can be liquid nickel-containing waste [17]. Superalloy scrap with the nickel binder is well suited for preparing nickel powder for manufacturing of superalloys. The scrap can be utilized in two ways [18, 19]:
- directly as a source of solid nickel;
- as a source of nickel salts after selective dissolution.
The other source of nickel can be scrap of batteries employing nickel oxide electrode, particularly alkaline batteries [20, 21]. In this case, the active electrode material (P-Ni(OH)2 [22] and a-Ni(OH)2 [23]) must be treated to obtain a solution of nickel salts. Nickel oxide electrodes of hybrid supercapaci-tors [24, 25] can be processed in the same way.
Many methods for the preparation of ultrafine nickel powder have been developed [26-40]. In [26], the evaporation-condensation method is proposed, however, this method requires special equipment and the process must be conducted under inert atmosphere. A method was developed for processing of solid nickel waste by treating them with molten metals [27], with zinc in particular [28]. The method consists in dissolving nickel in molten metal and then stripping the metal and obtaining nickel powder. Such method is not used to prepare nickel powder for superalloys, because it would contain admixtures of zinc or other metals. In [29], the solvothermal process for obtaining nickel powder has been described. A method for the preparation of nickel powder by reduction of nickel cation with hydrazine has also been developed [30]. In [31], the preparation of nickel powder from freshly precipitated nickel hydroxide by reduction with sodium hypophosphite has been described. However, this leads to the formation of Ni-P alloy powder, which is not suitable for the preparation of superalloys. It has been also proposed to use polyols as reducing agents [32], additionally, the paper also proposes the use of strong surfactants. This is likely because of absorption of surfactants on the surface of forming metal particles (as described in [33]). In this case, the powder would be contaminated with surfactant residue, which makes it unsuitable for the preparation of superalloys. The same can also be said about nickel powder, prepared by reduction with Ti(III) [34]. In this case, the nickel powder would be contaminated with volatile titanium compounds. One of the most common methods for the preparation of nickel powder is reduction with hydrogen from salts [35], and also oxides [36]. The prepared nickel powder is susceptible to grinding, doesn't contain any impurities, however, the production requires a hydrogen station and heating. A carbonyl method for the preparation of nickel powder is used [37], however, it employs highly toxic nickel carbonyl.
One of the most promising methods for the preparation of Ni powder is electrolysis, which allows controlling the parameters of the resulting powder. Methods of electro-
lyte-plasma synthesis [38, 39] and electrolysis with impulse current at elevated voltage [40] have been proposed. However, the usage of plasma-electrochemical process or high-voltage electrolysis complicates the equipment and significantly increases the cost of the process.
The more acceptable method is direct electrolysis of a nickel salt solution. In order to obtain nickel powder, it is necessary to conduct electrolysis at current densities that significantly exceed the limiting current density. However, under such conditions, the near-cathode volume is alkalined-ed and nickel is precipitated in the form of nickel hydroxide. In order to avoid this, the electrolysis of nickel salt (most commonly - nickel sulfate) is conducted in the presence of ammonium sulfate. In a basic medium, the ammonium cation transforms into ammonia, which forms an ammine complex with nickel, which can pass through the alkaline near-cathode layer to the cathode and upon discharge forms nickel powder [37].
Electrolysis of nickel sulfate with ammonium sulfate allows preparing nickel powder that is suitable for the preparation of superalloys. However, the detailed data on electrolysis parameters, electrolyte composition for the preparation of powder specifically for use in superalloys (susceptible to grinding, without admixtures of compact metal) are uncertain.
3. The aim and objectives of the study
The aim of the work is to determine synthesis conditions of ultrafine nickel powder for use in the preparation of superalloys.
To achieve this aim, the following objectives were set:
- to study the influence of the electrolyte temperature on the properties of the prepared nickel powder;
- to study the influence of electrolyte composition on the synthesis process and properties of nickel powder;
- to conduct a comparative analysis of prepared nickel powder samples and determine the optimal electrolysis conditions.
4. Materials and methods
4. 1. Electrolyte composition for preparation of nickel powder
For the preparation of nickel powder, the base solution of the following composition was used: Ni2+ 0.1 mol/L, NH4+
1 mol/L, NH3H20 up to pH 11. As a source of Ni2+, nickel sulfate NiSO4-7H2O, obtained from spent alkaline batteries was used, a source of NH4+ - ammonium sulfate, pH of the solution was corrected with aqueous ammonia solution.
4. 2. Study of electrode reactions during nickel powder synthesis
Electrode reactions were studied by recording cathodic and anodic polarization curves. The studies were conducted in a special three-electrode cell with the auxiliary platinum electrode. Ag/AgCl (KCl sat.) electrode was used as a reference electrode. The reference electrode was placed into a glass with a saturated KCl solution. The other glass, with the working and auxiliary electrodes, was filled with the electrolyte for nickel powder synthesis. Stainless steel was used as a working electrode for the cathodic process, and
nickel for anodic. In order to avoid the edge effect, the working electrode was placed into a Teflon cassette, composed of two rectangular parts, one of which had a round hole with a diameter of 0.012 m. In order to create an electrical contact between two glasses, a Luggin-Haber capillary filled with the studied solution was used. Polarization curves were recorded using the Ellins P-8 digital potentiostat (Russia). Potential scan rates were 1 mV/s and 5 mV/s.
4. 3. Electrolysis method for preparation of nickel powder
The electrolysis had been conducted in the flow-through polypropylene cell. The cell was equipped with stainless steel cathode and two nickel anodes. The electrolysis had been conducted at a current density of 100 A/dm2. During the electrolysis, large amounts of heat were generated. In order to evaluate the influence of synthesis temperature, the electrolysis was conducted under the following conditions:
- no cooling;
- evaporative cooling: the cell was placed into a tissue cover that was in the water and under airflow;
- water-cooling: the cell was placed in a large container with cold water;
- snow-water cooling: the cell was placed in a large container with a mixture of water and snow.
4. 4. Study of nickel powders
After electrolysis, nickel powder was removed from the cathode, washed a few times with distilled water and dried at room temperature.
Morphology and particle size were studied using the JEOL JSM-6510LV scanning electron microscope ("JEOL", Japan). Chemical composition was studied by means of EDX analysis using the Hitachi S4500 microscope (Japan).
5. Results of studying the conditions of electrochemical _synthesis of nickel powder_
5. 1. Study on the influence of temperature on characteristics of nickel powder
The results of evaluating the influence of the cell temperature on the characteristics of nickel metal powder are presented in Table 1.
Table 1
Influence of the cooling method and temperature on characteristics of nickel powder.
Cooling method Temperature, °C Powder quality
no cooling 98 Very coarse powder with inclusions of compact metal
evaporative cooling 81-82 Coarse powder, low susceptibility to grinding
water-cooling 74 Moderately fine powder, can be ground with effort
snow-water cooling 45-48 Ultrafine powder, easy to grind
Lower temperature leads to a finer powder and higher susceptibility to grinding. At high temperatures, the formation of compact metal is observed.
5. 2. Study on the influence of electrolyte composition on electrode reactions during nickel powder synthesis
When studying the influence of temperature during electrolysis without cooling, it was discovered that the solution color had changed from purple to blue. This indicated decreasing concentration of ammonia. Therefore, the influence of ammonia concentration on cathodic and anodic processes was studied. For that, solutions with ammonia concentrations of 50 %, 110 %, 150 % and 200 % of the base concentration were prepared.
Polarization curves in solutions with different concentrations of ammonia are presented in Fig. 1 (anodic curves) and Fig. 2 (cathodic curves).
Fig. 1. Anodic polarization curves of the nickel electrode in electrolytes for nickel powder synthesis with different ammonia concentrations
-14-12-10:
-a
-6-4 -22
2000 0 -2000 E, mV
-4000
Fig. 2. Cathodic polarization curves in electrolytes for nickel powder synthesis with different ammonia concentrations
It should be noted that in the electrolyte for powder synthesis, the nickel anode is partly soluble. Polarization curves show plateaus of limiting passivation current. It should also be noted that at an ammonia concentration of 2Cb (200 % of the initial concentration), the current was significantly higher.
Lowering of ammonia concentration did not impact the cathodic curve significantly. However, after the cathodic curve was recorded, a green deposit of nickel hydroxyl-com-pounds was observed on the electrode. An increase in ammonia concentration leads to increased polarization, which should improve the powder quality.
5. 3. Study on the effect of complexing agent additive on characteristics of nickel powder
In order to maintain a stable concentration of complexed ions, it was decided to employ and additional complexing agent. As such additional complexing agent, Trilon B was added in the amount of 20 % of the ammonia amount in the solution. In order to study the influence of Trilon B, nickel powders were prepared from electrolytes with and without
Trilon B. It should be noted, that snow-water cooling was used for these experiments in order to create optimal temperature conditions. SEM images are shown in Fig. 3, 4.
It was discovered that the powder is composed of small spherical particles that form coral-like grains about 4570 p.m. These agglomerates easily break apart even with little effort applied. Particles of compact metal were observed in the sample prepared with Trilon B additive.
the addition of Trilon B does not significantly impact the composition of nickel powder.
The cathodic and anodic current yields have been determined for electrolytes with and without Trilon B additive (Table 3).
Table 3
Current yields for nickel powder synthesis
Current Efficiency, %
Electrolyte Cathodic Anodic
(powder synthesis) (nickel dissolution)
Base 41 5
Base with Trilon B 35 8
The values presented in Table 3 reveal that the addition of Trilon B leads to a decrease in current yield for nickel powder synthesis and increase in current yield for nickel anode dissolution.
a b
Fig. 3. SEM images of nickel powder prepared without Trilon B additive. Magnification: a — x 1,330, b — x4,000
a b
Fig. 4 SEM images of nickel powder prepared with Trilon B additive. Magnification: a — x 1,330, b — x4,000
Table 2 shows the composition of nickel powders prepared without and with Trilon B additive.
Table 2
Chemical composition of nickel powder samples
Samples Element content, % mass
Ni Si P S Fe Co Zn
Sample with Trilon B 99.028 0.008 0.029 0.03 0.018 0.65 0.047
Sample without Trilon B 99.054 0.015 0.024 0.022 0.015 0.72 0.055
Samples Element content, % mass
As Cd Sn Ca Sb Pb Bi Al
Sample with Trilon B 0.002 0.003 0.004 0.001 0.001 0.005 0.002 0.055
Sample without Trilon B 0.004 0.002 0.002 0.001 0.001 0.006 0.003 0.076
The content of admixtures in both samples is low. The content of Ni is 99.03-99.05 %. The primary admixture in nickel powder is Co 0.65-0.72 %. It should be noted that
6. Discussion of the results of the study of electrochemical synthesis of nickel powder
During the electrolysis for the synthesis of nickel powder at ¿=100 A/dm2, the Joule heating causes electrolyte temperature to rise. The results presented in Table 1 show that low electrolyte temperatures result in fine powder. This is in agreement with the data, according to which higher polarization leads to smaller particle size. And with an increase in temperature, the polarization is decreased. It was discovered that for the formation of nickel powder that is suitable for superalloy production, the electrolyte temperature should not exceed 50 °C, which requires intense electrolyte cooling.
Analysis of the anodic polarization curves in the electrolyte with different ammonia contents (Fig. 1) revealed significant passivation of the nickel anode. All curves shows a pronounced passivation plateau, with the current density for nickel dissolution being insignificant - 1.5 mA/dm2. It is likely explained by the basic media of the electrolyte, despite the presence of ammonia as a complexing agent. At the ammonia concentration of 50-150 % of the base electrolyte, the behavior of the anodic curves is not affected significantly. Doubling of the ammonia content (200 % of the base electrolyte) leads to a significant increase in the nickel dissolution current because of complex formation, however, the absolute value of the current density is still low - 2.3 mA/dm2.
The influence of ammonia concentration on the cathodic process is more significant. Increased concentration of ammonia leads to a significant increase in polarization because of more stable ammine complex, which results in a decrease of limiting current density. As a result, the particle size would decrease, resulting in a finer powder. Upon decreasing the ammonia concentration two times (50 % of the base electrolyte), the polarization almost did not change. Upon a decrease in ammonia concentration in the highly basic cathod-ic layer of the electrolyte, a part of nickel would react with the formation of insoluble hydroxyl compound. Inclusion of hydroxides and basic salts significantly decreases the quality of the product, so it is necessary to maintain the ammonia concentration or introduce additional complexing agents.
Trilon B was introduced to the electrolyte for nickel powder synthesis in order to decrease the concentration of free nickel cations, lower the limiting current density and
increase the polarization of nickel formation. This should also lead to the formation of finer powder. This hypothesis is further supported by the SEM results. It should be noted that particles of compact metal had been observed in the powder prepared from the base electrolyte. This is likely because of local drop in ammonia concentration or local heating. The presence of such compact metal particles decreases the quality of nickel powder for use in superalloys. Introduction of Trilon B prevents the formation of compact metal and allows preparing a powder with similar-sized particles that constitute agglomerates. The influence of Trilon B on the electrolysis process is supported by the data in Table 3. Because of the formation of a sufficiently stable complex of Trilon B with Ni2+, the anodic current yield of nickel dissolution is increased and cathodic current yield is decreased.
The introduction of Trilon B almost doesn't affect the composition of the synthesized powder. In general, it should be noted that electrochemically synthesized nickel powder is of high purity. It should also be mentioned that the most significant impurity is Co, which is not harmful for the production of superalloys. Co on par with nickel is the most widespread metal binder in superalloys for various applications. Taking into account the discussions above, the synthesized nickel powders contain 99.67-99.77 % of the component necessary for the production of superalloys.
It should be noted, that electrolysis parameters were studied using a laboratory model for the periodic process. However, modern trends in technology development lie in the transition to continuous processes, which provide better stability of the product's characteristics. Thus, before industrial implementation, it is necessary to develop a pilot
reactor for continuous electrochemical synthesis and verify synthesis parameters.
7. Conclusions
1. It had been discovered that higher temperatures lead to lower powder dispersion. At an electrolyte temperature of 90-95 °C, nickel powder contains large amounts of compact metal. Lowering of temperature to 45-48 °C leads to the formation of ultrafine powder, though it contains some amount of compact metal.
2. It had been discovered, that an increase in ammonia concentration in the electrolyte increases the polarization of nickel formation and decreases the powder particle size. A decrease in ammonia concentration can lead to contamination of the powder with low-soluble hydroxyl compounds of nickel. It was proposed to introduce an additional complexing agent - Trilon B. It was discovered that the addition of Trilon B allows preventing the formation of compact nickel and enables to prepare 40-71 ^m long coral-like dendrites, composed of spherical particles that easily split apart. It was discovered that the introduction of Tilon B decreases the cathodic yield for the nickel formation from 41 % to 35 %, while increasing the anodic current yield for nickel from 5 % to 8 %.
3. The optimal conditions for electrolysis with the formation of ultrafine nickel metal powder, suitable for the production of superalloys had been determined: temperature below 45 °C, pH no lower than 11 (maintain with ammonia), addition of Trilon B.
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40. Preparation of nanosized nickel powder by direct-current electrolysis combined with high-voltage spark discharge / Ibishev K. S., Malyshev V. P., Kim S. V., Sarsembaev B. S., Egorov N. B. // High Energy Chemistry. 2017. Vol. 51, Issue 3. P. 219-223. doi: 10.1134/s0018143917030055
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Встановлено вплив добавок метакаолi-на i каолта на формування мжро- макро-структури й властивостей лугоактивова-них шлакових цементiв i бетотв. Проведено порiвняльне дослидження впливу цих добавок. Встановлено, що введення 2,5-5,0 % добавки каолту мае бшьш ефективний вплив на процеси структуроутворення i властивостi, тж добавка метакаолту. Окрiм того, замi-на добавки метакаолту каолтом спрощуе технологiчний процес виробництва й суттево знижуе варт^ть цементу и бетону
Ключовi слова: бетон, каолт, лугоакти-вований цемент, метакаолт, мщтсть при
стиску, морозостштсть
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Исследовано влияние добавок метакаоли-на и каолина на формирование микро- макроструктуры и свойств щелочеактивирован-ных шлаковых цементов и бетонов. Проведено сравнительное исследование влияния этих добавок. Установлено, что введение 2,5-5,0 % добавки каолина оказывает более эффективное влияние на процессы структурообразо-вания и свойства, чем добавка метакаоли-на. Кроме того, замена добавки метакаолина каолином упрощает технологический процесс производства и существенно снижает стоимость цемента и бетона
Ключевые слова: бетон, каолин, щелоче-активированный цемент, метакаолин, прочность при сжатии, морозостойкость -□ □-
UDC 691.5
|DOI: 10.15587/1729-4061.2018.119624|
A COMPARATIVE STUDY ON THE INFLUENCE OF METAKAOLIN AND KAOLIN ADDITIVES ON PROPERTIES AND STRUCTURE OF THE ALKALI-ACTIVATED SLAG CEMENT AND CONCRETE
P. Krivenko
Doctor of Technical Sciences, Professor* Е-mail: pavlo.kryvenko@gmail.com O. Petropavlovskyi PhD, Senior Researcher* O. Kovalchuk PhD, Senior Researcher* Е-mail: kovalchuk.oyu@gmail.com *Scientific Research Institute for Binders and Materials Kyiv National University of Construction and Architecture Povitroflotskiy ave., 31, Kyiv, Ukraine, 03037
1. Introduction
Environmental concerns arising from cement production due to CO2 emissions and high energy consumption required for high-temperature firing can be eliminated by a wider use of blended and composite cements [1].
One of such cements is the alkali-activated cement [2] (further, the AAC) which attracted an interest of scientists and industry worldwide [3] and promoted its fast development in recent years [4].
The AACs vary in proportions of basic oxides in the system N(K)2O-CaO-Al2O3-SiO2-H2O and, according
to this, can be divided into three types: high, low and medium-calcium alkali-activated cements [5]. This predetermines a phase composition of the hydration products, hence, properties of the cements and concretes on their basis [6].
The most widely used are the alkali-activated cements with metallurgical slags as an aluminosilicate component -the alkali-activated slag cements (further, the AASCs).
Since metallurgical slags vary in chemical composition [7], correcting additives are to be added in order to give the required (target) properties to a cement stone [8]. These additives can affect both properties of the alkali-activated cement paste and alkali-activated cement concrete due to more
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