Research of the Obtaining Process of Protective Phosphate Nanocoatings

This article presents thermodynamic calculations of the interaction of zinc and iron chlorides with phosphoric acid. The influence of temperature and duration of the interaction on the degree of decomposition of metal chlorides is also determined. It is established that with increasing the temperature and the duration of interaction, the degree of conversion of zinc and iron chlorides to metal phosphates increases and the residual chlorine content in the product simultaneously decreases. The quality control of the obtained products was carried out using physical, chemical and crystal-optical methods of analysis. keywords: Phosphates, Zinc and iron chlorides, Phosphoric acid, Metal phosphates, Metal corrosion.


INTROdUCTION
The protection of metal and structural products from corrosion is one of the most important problems of great importance for the national economy.
In this regard, one of the topical problems is to obtain anti-corrosive protective nanostructured coatings from production waste and reduce import substitution products.
Phosphate nanocoatings are one of the types of products obtained as a result of the interaction of the metal with a solution of phosphoric acid.These nanocoatings are a crystalline films of phosphate salts of iron and manganese or iron and zinc that are sparingly soluble in water.Such salts are stable under atmospheric conditions, in lubricating oils and organic solvents, but are destroyed in acids and alkalis.Phosphate coatings have high electrical resistance and withstand a voltage of up to 250 V, and after impregnation with insulating oils-up to 1000V 1 .
Phosphate nanocoatings are not wetted with molten metal, and this property is used in metallurgical production.The phosphate layer, impregnated with lubricants, favorably affects the processes of wire drawing, drawing pipes, stamping and transporting oil 2 .
The carbon and low-alloy steels, cast iron, some non-ferrous and light metals can be subjected to phosphatization.
In recent years, more attention has been paid to the phosphatizing of non-ferrous metals.Processes of phosphatizing zinc, cadmium, nickel, covar alloy, etc. have been developed.The film formed on such metals consists mainly of four-water tertiary zinc phosphate.Zinc-resistant film to corrosion on cadmium is formed for 10-20 min on nickel and covar for 30-40 minutes.In solutions containing accelerator additives, the duration of cadmium phosphatizing can be reduced to 5-10 min zinc up to 3-5 minutes.Painting coatings, applied on nickel by phosphate ground are suitable for products operating in a humid atmosphere 3 .Some authors 4 developed the composition and methods of application of phosphate and chromium coats.Proposed method includes treatment of surface first with phosphatizing solution of the following composition, g-L -1 : zinc monosulfate, 12-14; zinc nitrate, 18-22; sodium phosphate, 5-10; orthophosphoric acid, 4-5 and remainder being water; then phosphatizing in solution at concentration of 15-30 g/l and impregnation of coat in solution at concentration of 80-100 g-L -1 are performed followed by drying at temperature of 100-120 O C.
The next invention 5 relates to protection of metals against corrosion and is designed for a preliminary treatment of the metal surface for the follow-up paint application.The method involves phosphatization of the metal surface in the aqueous solution and this is performed by spraying the aqueous solution on the metal surface for 40-60 sec.at the point of entry into the phosphatization tank by immersing the metal into the phosphatization tank for 2.5 min and spraying the aqueous solution on the metal surface for 40-60 sec at the output of the phosphatization tank with temperature of the aqueous solution being 35-40°C.
In work 6 , a metal surface is treated with aqueous solution containing zinc, nitrate, nickel, and chlorate ions; when fine-crystalline corrosion-resistant phosphate coating is to be obtained at phosphatization temperature 30-45 o within a period of time 2 to 10 minutes.The method is suitable in mechanical engineering, instrumentation engineering, and can also be applied when performing phosphatization of passenger compartments and cars and trucks bodies.
The authors of the invention 7 studied the solution of phosphatization and a method of treatment of a metal surface with the solution and it is pertinent to treatment of metal surfaces, in particular, to phosphatization and may be used for protection of metals against corrosion in any branch of engineering industry and instrumentmaking industry at realization of painting activities.The solution contains a phosphorous-containing compound, an oxidizing agent neutralizing the component and water at pH 3.0-4.2.
A group of scientists developed a solution for phosphating a metal surface 8 .The solution contains (in g-L-): nitrate ions 1.8-6.5, chlorate ions 2.7-7.8,molybdenum ions 0.01-0.04,and also phosphate ions (in terms of P 2 O 5 ) 6.7-17.0 and calcium ions 0.9-3.5 in the form of a Khibini apatite concentrate.The application of the proposed solution allows to obtain phosphate coatings with high corrosion resistance, to use available technical raw materials for solution preparation.
In work 9 , a brief overview of the current research worldwide in the chemical synthesis of copper nanoparticles is discussed.Chemical methods are used to synthesize copper nanoparticles and among them chemical reduction is the most frequently applied method for the preparation of stable, colloidal dispersions in organic solvents.
In paper 10 , the chemical hazards of nanoparticles to human and environment were studied.This literature review has been commissioned to explore the physical and chemical properties of nanoparticles that could differentially influence toxicity, use of nanoparticles in industry and the potential hazards.This article has summarized the current state of knowledge on the potential risks posed by nanoparticles.
In next work 11 , the ther modynamic characteristics of the chemical interaction of zinc chloride with phosphoric acid were researched.It was found, that with the increase of the temperature and the duration of chemical interaction, a transformation degree of zinc and iron chlorides into phosphates increases and a residual content of chlorine in the products decreases simultaneously.A quality control of the received products was carried out using methods of chemical and crystal-optical analysis.
In paper 12 , the technology for processing metal waste of phosphate compounds of metals was developed in order to use them as nanocoating.An adequate mathematical model with the best mode of the process was obtained.
When processing chloride sublimes containing ZnCl 2 , PbCl 2 , CuCl 2 , FeCl 2 , etc., the hydrometallurgical method produces non-ferrous metal salts, which are used to produce oxides, chlorides, sulfates and phosphates of metals.Processing zinc chloride with phosphoric acid makes it possible to obtain especially pure zinc phosphate, salts of lead and iron.The resulting zinc phosphates are used in the phosphatizing of metals and the preparation of mineral fertilizers or as corrosion inhibitors.
Therefore, the processing of zinc chloride on zinc phosphates is of both scientific and practical interest.It is necessary to study the kinetic parameters of the process of obtaining Zn(H 2 PO 4 ) 2 from zinc chloride.The presence of iron phosphate in the composition of zinc phosphate enhances the quality of phosphate coatings.

METHOdS ANd MATERIALS
Zinc phosphate is obtained from the chloride sublimates, containing Zn-18.3%, Cl-28.9%,others-62.8%.After separation of insoluble impurities and chloride compounds (FeCl 2 , PbCl 2 , etc.), the solution containing zinc chloride is treated with 45% phosphoric acid.Hydrochloric acid can be obtained from the hydrogen chloride evolved in this process.
Preliminary thermodynamic calculations show the probability of a reaction of the interaction of zinc chloride with phosphoric acid with the formation of Zn(H 2 PO 4 ) 2 .2H 2 O, FeHPO 4 and HCl, as evidenced by the negative value (-∆GT°) of Gibbs energy.The calculation of the Gibbs energy values was carried out using a computer in the temperature range 298-433 K.
For obtaining zinc chloride, at the beginning of each cycle, a chloride sublimate in an amount of 100 g is dissolved at a temperature of 25°C, while PbCl 2 and an insoluble precipitate fall out in the precipitate.After filtration a solution, containing ZnCl 2 and FeCl 2 is treated by adding a stoichiometric amount of 73% H 3 PO 4 .The formation of phosphates of zinc and iron occurs according to the following reactions (1) and (2).
The process proceeds with intensive stirring in the temperature range 60-120°C and a duration of 40-60 minutes.In this case, hydrogen chloride is released into the gas phase, while Zn(H 2 PO 4 ) 2 and FeHPO 4 are precipitated.
Quality control and investigation of the products obtained was carried out using chemical and crystal-optical methods of analysis.X-ray phase analysis was performed on the URS-50 IM device, differential-thermal analysis was performed on a derivatograph (Paulik, Aulik systems, etc.) in the temperature range 20-1000°C with a heating rate of 10 deg/minutes.IR spectral analysis was performed on a UR-20 spectrometer in the frequency range from 400 to 3600 cm -1 .

RESULTS ANd dISCUSSION
The effect of temperature and duration on the degree of conversion of zinc and iron chlorides into metal phosphates (αconv.) is given in Tables 1 and 2, from which it follows that with increasing temperature and duration of interaction, the degree of conversion of zinc and iron chlorides into metal phosphates increases and simultaneously the residual chlorine content in the product decreases 13 .This indicates that as the temperature increases in the liquid phase, the particles of a mixture of zinc and iron phosphates is formed in a large amount, and the amount of free phosphoric acid decreases.From the results given in Table 1 it can be seen that as the temperature and duration of interaction increase, the degree of conversion of zinc chloride into monozincphosphate increases and the residual chlorine content in the product decreases at the same time.The resulting hydrochloric acid containing 28-30% HCl meets the requirements, imposed on the quality of technical hydrochloric acid.
On the basis of the conducted research it is established that the optimal parameters of the process are the temperature of 100-120°C, the duration of the interaction is 40-60 minutes.The degree of conversion of zinc chloride into monozinc phosphate is 99.9-100%, and chlorine is practically absent.Table 2 shows the results of decomposition of iron chloride with phosphoric acid.Table 2 shows that with increasing the duration and temperature the yield of FeHPO 4 increases, simultaneously the content of FeCl 2 and a free acidity in product decreases.At the same time, the yield of FeHPO 4 at 170°C is 5.94 g and chlorine is practically absent.
IR spectral analysis was performed on a UR-20 spectrometer in the frequency range from 400 to 3600 cm -1 .The presence of the monoclinic form of Zn(H 2 PO 4 ) 2 .2H 2 O was confirmed by X-ray diffraction analysis with a full correspondence of the values between the interplanar distances (d, A) and the relative intensities (l / l1) of the sample when surveying on a diffractometer.The obtained product was studied by X-ray diffraction on a DRON-3 instrument in the interval 20-68°, differential-thermal analysis on a derivatograph (Paulik, Pulik-Erdei) in the temperature range 20-1000 o at a heating rate of 10 deg-min -1 .
Derivatographic studies of products -FeHPO 4 (temperature 170°C and duration 90 min) showed that in the temperature range 300-950°C thermal effects were fixed.The exothermic effect at 368, 410°C is due to the conversion of FeHPO 4 to FePO 4 , and at 810, 950°C -by the melting of iron.
The derivatogram of Zn(H 2 PO 4 ) 2 .2H 2 O, starting at 60°C, sharply deflects the DTA curve from the baseline, caused by the endothermic effect in the temperature range 60-156°C and refers to the melting process of Zn(H 2 PO 4 ) 2 .2H 2 O in crystalline hydrate water and accompanied by a slight loss of mass -2.12%.The second endothermic effect at 232°C is caused by the removal of the crystalline hydrate and part of the constitutional water with partial condensation of mono-zinc phosphate Zn(H 2 PO 4 ) 2 .As the sample is heated from 390 to 840°C, further condensation and the appearance of several endothermic effects and a small loss of mass of the sample occur.The endothermic effect at 790 and 830°C corresponds to the polymorphous transformation of zinc metaphosphate and the melting of a mixture of zinc metaphosphate and pyrophosphate, and at 892° corresponds to the melting process of all the decomposition products of mono-zinc phosphate.On the IR spectrum, the band with weakly expressed maxima at 3420 and 3600 cm -1 can be attributed to the valence vibrations of the OH¯ group and the formation of relatively strong hydrogen bonds.The band with a maximum at 1650 cm -1 corresponds to vibrations of water molecules, and the bands 640 and 585; 1025 and 950; 1150 and 1070 cm -1 probably indicate the complexity of the spectrum due to the low symmetry of the H 2 O 4 -atom.
Thus, our studies have shown the possibility of obtaining zinc and iron chlorides, and iron monozinc phosphate and hydrophosphate, X-ray phase and IR spectral analysis for the presence of Zn(H 2 PO 4 ) 2 .2H 2 O and FeHPO 4 and the absence of chlorine in the product.
Mass-spectrum analysis of the obtained zinc phosphate showed the presence of phosphorus content in the product is 8.42%, zinc 43.89% and insignificant amount of chlorine 0.91% (Fig. 2), and the presence of iron 18.74%, phosphorus 14.52 % (Fig. 3).The size of phosphates ranges from 0.1 μm to 100 μm.Such phosphate compounds meet the requirements of State standard and can be used as anticorrosive coatings for construction and products.Thus, our studies have shown the possibility of obtaining zinc and iron phosphates from ZnCl 2 and FeCl 2 , and X-ray phase analyzes for the presence of Zn(H 2 PO 4 ) 2 .2H 2 O and FeHPO 4 in the product.

Fig. 2 .Fig. 3 .
Fig. 2. Electronic image of the obtained zinc phosphate and its chemical composition