On the Process and Products of Hydrolytic Decomposition of Titanium Tetrachloride
L. N. Shchegrov and Ya. E. Vilnyanskii
Submitted 1961-01-01 | SovietRxiv: ru-196101.37880 | Translated from Russian

Abstract Generated abstract

This study examines the vapor phase hydrolysis of titanium tetrachloride by water vapor in a dynamic system over 25 to 750°C, with several TiCl4:H2O molar ratios. The authors measured product composition, hygroscopic behavior, chloride retention, and phase structure using chemical analysis and X-ray powder methods. They found that hydrolysis begins immediately and proceeds very rapidly, producing variable titanium oxychloride and hydroxychloride compounds at 25 to 150°C rather than products described by simple stoichiometric equations. Complete conversion to TiO2 was not achieved at 300°C, while anatase TiO2 with low residual chloride formed at 500 to 750°C, and a previously unidentified crystalline phase appeared among products formed at 75 to 150°C.

Full Text

Chemistry

L. N. Shchegrov and Ya. E. Vilnyanskii

ON THE PROCESS AND PRODUCTS OF THE HYDROLYTIC DECOMPOSITION OF TITANIUM TETRACHLORIDE

(Presented by Academician S. I. Volfkovich, April 4, 1961)

The least studied is the vapor-phase hydrolysis of titanium tetrachloride at relatively low temperatures (25–150°), when the formation is possible not of dioxide, but of titanium oxy- and hydroxychlorides (^1). The latter may form as by-products in processes of chlorination of titanium-containing raw materials (^2,^3) and rectification of technical titanium tetrachloride (^4). Information on the conditions of formation and the properties of titanium oxy- and hydroxychlorides is scant and often contradictory (^4–^6).

In the present work we studied the interaction of TiCl₄ vapor with H₂O vapor in a dynamic system in the temperature range 25–750°. The ratio of the molar concentrations of TiCl₄ and H₂O in the reaction mixture was 1 : 1, 1 : 2, 1 : 3, and 1 : 4, respectively. The experimental part of the study consisted in saturating an inert carrier gas, with respect to the reagents, with definite amounts of TiCl₄ and H₂O vapors, after which the two streams were combined at a specified temperature in the reactor; the reaction products were trapped and subjected to further study. In all experiments the interaction of TiCl₄ with H₂O vapor began immediately after their contact in the reactor, which was visually observed from the formation of a white smoke (aerosol), whereas Hudson (^1) reports that the indicated reaction occurs only several minutes after mixing the reagents. It was established that changing the mean residence time of the reagent mixture in the reaction zone from 11.85 sec to 0.23 sec (a decrease by ~50 times) has no substantial influence on the magnitude of the degree of hydrolytic decomposition of TiCl₄. Evidently, the vapor-phase hydrolysis of TiCl₄ proceeds with extremely high speed.

Figure 1

Fig. 1. Dependence of the titanium content in TiCl₄ hydrolysis products on the reaction temperature:
A — 1 : 1; B — 1 : 2; V — 1 : 3; G — 1 : 4

Particles of the solid reaction products obtained in the temperature range 25–150° are very fine, but have the property of sticking together with the formation of small, shapeless, highly hygroscopic lumps; therefore all work with them was carried out in a chamber filled with dry air. They have a yellowish coloration, the intensity of which decreases with increasing hydrolysis temperature and with increasing molar concentration of water in the reaction mixture. It was established that these substances are good dielectrics.

The composition of the TiCl₄ hydrolysis products, as shown by Figs. 1 and 2, depends on the conditions under which they are obtained. Changing the TiCl₄ : H₂O ratio in the reaction mixture from 1 : 1 to 1 : 3 leads to a decrease in the titanium content and

chlorine in the hydrolysis products (curves A, B, V). However, at the ratio \(\mathrm{TiCl_4:H_2O}=1:4\), the titanium content increases and the chlorine content decreases (curve G in Figs. 1 and 2) in the hydrolysis products obtained at temperatures of 25, 50, and 75°. The latter phenomenon is associated with the interaction of the \(\mathrm{TiCl_4}\) hydrolysis products with vapors of “excess” water, leading to the liberation of HCl from the indicated substances.

The composition of the vapor-phase hydrolysis products of \(\mathrm{TiCl_4}\), obtained in the temperature range 25–150° and consisting of compounds of variable composition, is proposed to be expressed by the formulas:

\[ \mathrm{TiO_a(OH)_{2-2a}Cl_2}, \qquad \text{where } a=0\div 1; \]

\[ \mathrm{Ti(OH)_xCl_{(4-x)}\cdot nH_2O}, \qquad \text{where } x:(4-x)=1\div 3. \]

Thus, the results of experiments on the hydrolytic decomposition of \(\mathrm{TiCl_4}\) in the temperature range 25–150° showed that the actual reaction cannot be expressed by any of the simple equations usually cited in the literature \((^{5,6})\). Complete hydrolytic decomposition of \(\mathrm{TiCl_4}\) did not occur in the experiments described even at 300°, since the reaction product obtained at this temperature contained about 15% chloride ion, rather strongly bound to titanium. At 500° the product of \(\mathrm{TiCl_4}\) hydrolysis was \(\mathrm{TiO_2}\), containing no more than 2% chloride ion. At 750° the chloride-ion content in \(\mathrm{TiO_2}\) decreases to 0.1–0.2%.

Figure 2

Fig. 2. Dependence of the chlorine content in the \(\mathrm{TiCl_4}\) hydrolysis products on the reaction temperature. Designations as in Fig. 1

Fig. 3 presents a typical picture of the dependence of the change in weight of \(\mathrm{TiCl_4}\) hydrolysis products, obtained in the range 25–100°, on the time of their residence in atmospheric air. As is seen from Fig. 3, the curve of weight change at first rises sharply, reaching a maximum, after which a decrease in weight occurs. This is explained by the fact that, along with adsorption of moisture by the \(\mathrm{TiCl_4}\) hydrolysis product, a chemical reaction occurs between it and the added water, with liberation of hydrogen chloride into the gas phase. After a certain time, the rate of water adsorption by the substance becomes equal in magnitude to the rate of the hydrolysis reaction (maximum on the curve in Fig. 3). Subsequently the hydrolysis process begins to predominate over the sorption process, and the weight of the substance decreases.

Figure 3

Fig. 3. Change in weight of \(\mathrm{TiCl_4}\) hydrolysis products as a function of residence time in atmospheric air

To study the phase composition of the products obtained by hydrolytic decomposition of \(\mathrm{TiCl_4}\), the method of X-ray qualitative phase analysis of polycrystalline substances was used (Debye–Scherrer method). It was established that the products of vapor-phase hydrolysis of \(\mathrm{TiCl_4}\), obtained in the temperature range:

1) 75–150° form a new crystalline phase, previously unknown, with a structure different from the structures of known titanium compounds. This new phase is no longer detected at 300°;

2) 25–50° and ratios of \(\mathrm{TiCl}_4 : \mathrm{H}_2\mathrm{O}\) in the reaction mixture of \(1 : 1\), \(1 : 2\), and \(1 : 3\) show no crystalline structure by X-ray analysis. However, after a short time in moist atmospheric air they acquire an unmistakably crystalline structure, and their interference pattern is close to that shown by the products obtained in the interval 75–150°;

3) 300–750°—are titanium oxide \(\mathrm{TiO}_2\) with the anatase structure.

Ural Polytechnic Institute
named after S. M. Kirov

Received
2 IV 1961

CITED LITERATURE

  1. R. F. Hudson, Proc. of the XI Intern. Congr. of Pure and Appl. Chem., 1, London, 1947, p. 297.
  2. R. L. Powell, Chem. Eng. Progr., 50, 11, 578 (1954).
  3. L. W. Rowe, W. R. Opie, J. Metals, 7 (11), sect. 1, 1189 (1955).
  4. T. A. Zavaritskaya, S. S. Pustovalova, Tsvetnye metally, No. 10, 50 (1958).
  5. G. P. Luchinskii, Titanium Tetrachloride, Moscow, 1939.
  6. König, Pfordten, Ber., 21, 1708 (1888).

Submission history

On the Process and Products of Hydrolytic Decomposition of Titanium Tetrachloride