Patent Application
20060051267
This invention relates to a process for the removal of multiple metal chlorides from a crude titanium tetrachloride stream produced by chlorination of titanium-bearing compounds, and more particularly to a process wherein the removal of multiple metal chlorides occurs in a single reaction vessel.
In the production of titanium tetrachloride, raw materials, including ilmenite or rutile ores or other titanium-containing materials such as those obtained from beneficiating these ores, are reacted with chlorine and carbon (carbochlorination) to yield a mixture of metal chlorides in a crude titanium tetrachloride stream, from which titanium tetrachloride of sufficient purity may be recovered that may be used as a starting material to make titanium metal or titanium dioxide pigment.
Common metal chloride impurities present in the crude titanium tetrachloride include chlorides and complex chlorides of aluminum, niobium, tantalum, and vanadium. These metal chloride impurities are not susceptible to removal by distillation because of the proximity of their boiling points to that of titanium tetrachloride or their solubility in the titanium tetrachloride. They can have a detrimental impact on downstream processes. Thus, it is important to remove them or treat them to inhibit their detrimental properties.
Aluminum chloride, for example, is highly corrosive and attacks the metal materials of construction in the equipment downstream of its formation; thus, aluminum chloride must be rendered non-corrosive via treatment with a passivating agent early in the processing of making crude titanium tetrachloride.
Niobium and tantalum chlorides may condense downstream and cause fouling problems. Conveniently these two metal chlorides may be removed in the passivation of the aluminum chloride through their preferential reaction with certain aluminum passivating agents.
Water, sodium chloride, sodium hydroxide or a mixture of these are the most common agents added to passivate aluminum chloride. The passivated aluminum compounds are more easy-to-separate from the crude titanium tetrachloride stream than aluminum chloride. Aluminum passivating agents are selected to form aluminum compounds that are not corrosive to the equipment. See, for example, U.S. Pat. Nos. 2,600,881; 4,125,586; and U.S. Pat. No. 4,521,384. Furthermore, as taught by Bonsack in U.S. Pat. No. 4,070,252, use of water to treat crude titanium chloride streams also converts niobium and tantalum chlorides to species insoluble in liquid titanium tetrachloride, which can be readily removed by filtration or other simple separation techniques.
Vanadium chlorides form colored species that must be removed if the titanium tetrachloride is to be used for production of titanium dioxide pigment. Typically, treatment agents are added to the crude titanium tetrachloride to chemically modify these vanadium compounds so that they may be removed. Therefore, there is a body of art that teaches treatment for removing vanadium chlorides from titanium tetrachloride, but this body of art is essentially separate from that of the passivation of aluminum chloride in titanium tetrachloride.
The prior art in the passivation of vanadium chlorides discloses the use of catalytic metals, such as iron and copper or other agents such as activated carbons, hydrogen, hydrogen sulfide and a number of organic compounds, such as oils, esters, and amines. Examples of prior art teachings for removal of vanadium compounds from crude titanium tetrachloride include the following. Swiss Patent No. 262267, published in 1949, discloses removing colored metal chlorides (Cr, and V) by treating the crude titanium tetrachloride, at an elevated temperature, with a metal-free organic compound which is carbonized by the chlorides. U.S. Pat. No. 2,560,424 discloses a method to remove the colored impurities from titanium tetrachloride by simultaneously adding to the crude titanium tetrachloride small amounts of aluminum metal and anhydrous aluminum chloride. Australian Patent No. 219,385 teaches the use of metallic sodium to remove vanadium impurities from titanium tetrachloride.
While methods have long been available for treatment of crude titanium tetrachloride, treatments to remove the metal chlorides of aluminum, niobium and tantalum have been practiced separately from treatments to remove vanadium chlorides from crude titanium tetrachloride. The present invention is a method to remove metal chloride impurities including the chlorides of aluminum and vanadium in a way that minimizes the loss of process raw materials such as titanium containing materials, coke, chlorine, and vanadium and aluminum passivating agents. The present process is more cost effective, produces less waste and more product and is the result of a simple change in the sequence of and locations for the additions of the aluminum and vanadium passivating agents.
The present invention provides a method in the purification of a crude titanium tetrachloride chlorinator discharge from the carbochlorination of titanium containing materials to minimize the loss of raw materials resulting from passivation of aluminum chloride and vanadium oxychloride, comprising:
The addition of the vanadium and aluminum passivating agents may be made such that the vanadium passivating agent and the aluminum passivating agent are mixed into the discharge essentially simultaneously or the vanadium passivating agent may be mixed into the discharge before the aluminum passivating agent is mixed into the discharge, or the vanadium passivating agent may be mixed into the discharge after the aluminum passivating agent is mixed into the discharge or the vanadium passivating agent may be mixed into the discharge both before and after the aluminum passivating agent is mixed into the discharge.
The present invention is a method in the purification of a crude titanium tetrachloride chlorinator discharge from the carbochlorination of titanium containing materials to minimize the loss of raw materials resulting from passivation of aluminum chloride and vanadium chlorides.
The term vanadium chlorides as used herein includes vanadium oxychloride compounds and other vanadium chloride compounds that are not susceptible to removal from crude titanium tetrachloride by distillation.
In the present invention, the passivation of vanadium chlorides may be accomplished in a two step addition of the vanadium passivating agent or in a single step addition. In the two step addition, a vanadium passivating agent is mixed into the discharge in an amount sufficient to reduce, but not eliminate the vanadium chlorides present and form one or more easy-to-separate vanadium-containing compounds. When titanium oxychloride is present in the discharge treated with the vanadium passivating agent, no aluminum passivating agent is added. When titanium oxychloride is not present, an amount of aluminum passivating agent sufficient to form titanium oxychloride is added to form easy-to-separate aluminum-containing compounds. The easy-to-separate vanadium- and aluminum-containing compounds may be separated from the discharge. Then, a second addition step of a vanadium passivating agent in an amount sufficient to passivate the remaining vanadium chlorides is made to form easy-to-separate vanadium-containing compounds, followed by a separation step to form a purified titanium tetrachloride.
In the single step addition of the vanadium passivating agent, sufficient vanadium passivating agent is mixed into the discharge to passivate all of the vanadium chlorides in a single step, and, if necessary, addition of aluminum passivating agent is made if there remains active aluminum chloride in the discharge as determined by the absence of titanium oxychloride in the discharge. In any event, all of the aluminum chloride present in the discharge must be passivated, no matter which method (two step or single step) is used to passivate the vanadium chlorides, since the presence of active aluminum chloride after this point in the overall purification process will result in corrosion of downstream equipment.
The terms passivating and passivation as used herein mean converting the vanadium- and aluminum-containing compounds present in the crude titanium tetrachloride discharge to compounds that are easy-to-separate from the titanium tetrachloride and neutralizing the compounds' adverse effects. “Easy-to-separate” typically means a solid, but it also includes compounds that may be separated from the titanium tetrachloride by distillation or removal as an adsorbed species, and the like. Surprisingly, it has been found that the product of the passivation of vanadium oxychloride in crude titanium tetrachloride discharge with an organic oil is a passivating agent for aluminum chloride. The result of this discovery according to the present invention is an improved chlorination process wherein there is the potential to save production costs by reducing the titanium yield loss while at the same time improving raw material utilization to reduce process cost and the amount waste—solid, liquid, and vapor.
In the present invention, the point of addition of the passivating agents into the flow of the chlorinator product stream, that is, crude titanium tetrachloride discharge, may be optimized for (1) the reduction and elimination of corrosion from active aluminum chloride, (2) minimal yield losses of raw materials, and (3) to take advantage of the ability of passivated vanadium compounds to provide at least part of the total amount of passivating agent needed to control passivation of aluminum chloride, as measured by titanium oxychloride concentration.
Addition of the aluminum passivating agent is dependent on whether there is titanium oxychloride in the crude titanium tetrachloride chlorinator discharge stream. Aluminum chloride is completely passivated once titanium oxychloride is formed in the discharge. Aluminum passivating agent may be mixed into the chlorinator discharge simultaneously with the vanadium passivating agent or before addition of the vanadium passivating agent or after addition of the vanadium passivating agent. After mixing the vanadium or aluminum passivating agent into the chlorinator discharge, the discharge is analyzed for titanium oxychloride. If titanium oxychloride is formed, addition of aluminum passivating agent is not required. If no titanium oxychloride is formed, then an amount of aluminum passivating agent sufficient to passivate the aluminum chloride and react with the titanium tetrachloride to form titanium oxychloride is mixed into the chlorinator discharge.
Water is most preferred as the aluminum passivating agent in the present process. Water solutions or mixtures may be used as passivating agents even if the materials other than the water show no reactivity towards aluminum chloride.
Since some fraction of the aluminum chloride is passivated by the reaction product of vanadium oxychloride with the vanadium passivating agent, it is preferable to add only 1 to 1.5 times the amount of passivating agent to stoichiometrically react with the remaining aluminum in the discharge. More preferably the amount of aluminum passivating agent added is 1.1 to 1.3 times the stoichiometric requirement.
Organic oils have been found to be useful as vanadium passivating agents including petroleum oils, such as mineral oils and waxes, animal fat, and vegetable oils and combinations thereof. The organic oil may be hydrogenated. A specific example of a useful organic oil is hydrogenated naphthenic oil. The essential element in selecting a substance as a vanadium passivating agent is the ability of the reaction product of the passivating agent with vanadium oxychloride to function as an aluminum passivating agent. Those skilled in the art may find other organic compounds that are functionally equivalent to an organic oil that are also useful as the vanadium passivating agent. Similarly, some inorganic vanadium passivating agents may also be useful as functional equivalents to the organic oil, so long as there are no detrimental effects, such as color formation in the titanium tetrachloride, or where the passivated compounds may become re-chlorinated. Especially preferred as the organic oil vanadium passivating agent is a hydrogenated naphthenic oil.
The amount of vanadium passivating agent is based on the agent's stoichiometric reaction ratio with the vanadium chlorides. Ideally, this ratio should be determined experimentally, rather than theoretically. Preferably the amount of vanadium passivating agent added is 0.8 to 1.2 times the stoichiometric quantity required to react with the vanadium chlorides to be removed from the stream being treated, which may be all or any fraction of the vanadium present in that stream. More preferably the amount of vanadium passivating agent is from 0.95 to 1.1 times the stoichiometric requirement.
Regardless of the amount of vanadium passivating agent added, it is possible to calculate the amount of vanadium removal reaction products capable of passivating aluminum chloride and then reduce the amount of aluminum passivating agent or reduce the addition rate by an equivalent amount which can substantially reduce titanium losses due to excess addition of aluminum passivating agents which react with titanium tetrachloride. For example, one method to calculate the amount of vanadium removal reaction products capable of passivating aluminum chloride is by infrared spectroscopy, based on concentration of vanadium oxychloride in the chlorinator discharge.
Following addition of the passivating agents, there is provided a separation step wherein the easy-to-separate vanadium- and aluminum-containing compounds are separated from the titanium tetrachloride chlorinator discharge to form a purified titanium tetrachloride using a vapor-liquid-solid separation process or a solid-liquid separation process. A vapor-liquid-solid separation process is typically a distillation process, preferably selected from the group consisting of flashing distillation and multi-stage distillation. A solid-liquid separation process is typically filtration or centrifugation.
The separation process may occur in one or more steps. For example, depending on the order of addition of the vanadium and aluminum passivating agents, intermediate separation steps may be performed. Particularly, in a two step addition of the vanadium passivating agent, a separation step may be performed after all of the aluminum chloride has been converted to easy-to-separate aluminum-containing compounds. A separation step is performed after the second addition of the vanadium passivating agent.
Alternatively, following a separation step after addition of vanadium passivating agent, a purge containing products from the passivation of vanadium chlorides may be used as the aluminum passivating agent.
Process control methods for the addition of the aluminum passivating agent, the vanadium passivating agent, or both can be applied to the present invention. For example, the control methods disclosed in U.S. Pat. No. 6,562,312 are particularly useful for controlling addition of aluminum passivating agent. Therein is provided, an in-process, real time control loop capable of controlling the passivation of aluminum chloride in crude titanium tetrachloride chlorinator discharge wherein an aluminum passivating agent is mixed into the discharge in an amount sufficient to form titanium oxychloride. The amount of aluminum passivating agent added is controlled based on comparison of the titanium oxychloride concentration measured in-process with an aim point. Preferably, the concentration of titanium oxychloride is measured by an optical method selected from the group consisting of transmission filter Infrared spectroscopy, transmission Fourier Transform Infrared spectroscopy, Raman spectroscopy, Attenuated Total Reflectance Infrared spectroscopy, and Attenuated Total Reflectance Fourier Transform Infrared spectroscopy.
The presence and concentration of titanium oxychloride may be measured by use of transmission filter Infrared spectroscopy, transmission Fourier Transform Infrared spectroscopy, Raman spectroscopy, and Attenuated Total Reflectance Infrared spectroscopy, and Attenuated Total Reflectance Fourier Transform Infrared spectroscopy in a frequency range of from 800 to 2000 cm-1.
For accuracy and precision, it is most preferred to measure the presence and the concentration of titanium oxychloride by diamond based Attenuated Total Reflectance Fourier Transform Infrared at a frequency of about 820 cm-1. Diamond based attenuated reflectance means that the infrared probe or detector placed in the process stream has a diamond element. Suitable probe units include those manufactured by ASI Applied Systems of Millersville, Md., Axiom Analytic, Inc. of Irvine, Calif. and others.
In the following examples VOCl3 passivation is measured by Fourier Transform Infrared Spectroscopy (FTIR).
A round bottomed flask was filled with 100 mL TiCl4, 0.92 g VOCl3 (5.31 mmol), and 0.174 g AlCl3 (1.30 mmol). The AlCl3 was handled air-free to avoid moisture contamination. The reaction mixture was heated to 100° C. Hydrogenated naphthenic oil (ERGON Incorporated's product brand Ergon H-750) was added (1.0333 g). The reaction mixture was held at temperature for 30 minutes. At this point, all of the VOCl3 was passivated, as measured by FTIR. To determine how much unreacted AlCl3 remained, 30 microliter (1.61 mmol) of water were added by syringe. Any AlCl3 in solution would react with the water before TiOCl2 was formed. A total of 1531 ppm TiOCl2 was generated from the water addition, as observed by FTIR. If all of the AlCl3 was present, only 280 ppm should have been observed. Since an extra 1301 ppm TiOCl2 (1.67 mmol) formed, all of the AlCl3 had already been passivated in the solution.
A round bottomed flask was filled with 100 mL TiCl4, 0.92 g VOCl3 (5.31 mmol), and 1.74 g AlCl3 (13.0 mmol). The AlCl3 was handled air-free to avoid moisture contamination. The reaction mixture was heated to 100° C. The oil from Example 1 was added (1.0401 g). The reaction mixture was held at temperature for 30 minutes. At this point, all of the VOCl3 was passivated, as measured by FTIR. To determine how much unreacted AlCl3 remained, 290 microliter (16.1 mmol) of water were added by syringe. A total of 6808 ppm TiOCl2 was generated from the water addition. If all of the AlCl3 was still present, only 2371 ppm TiOCl2 should have been observed. Since an extra 4437 ppm TiOCl2 (5.70 mmol) formed, part of the AlCl3 was passivated in the solution. The amount of AlCl3 reacted was stoichiometrically equivalent to the amount of oxygen initially present in solution as part of the VOCl3, within experimental error.
Water was added as an aluminum passivating agent to a crude TiCl4 stream containing metal chloride contaminants AlCl3 and VOCl3 produced by the chlorination of titanium-bearing ore, following discharge from the chlorinator and separation of condensable solids. Water addition was in control by the control method described in U.S. Pat. No. 6,562,312. The hydrogenated, naphthenic oil, from Example 1 (vanadium passivating agent) was added to the TiCl4 stream at the same location as the water addition. In contrast to operating the process in the absence of the vanadium passivating agent, the demand for aluminum passivating agent was reduced by 50% while reducing VOCl3 by 20% of its original concentration.
Cross-reference is made to U.S. Provisional Application No. 60/439190 filed on Jan. 9, 2003, which is incorporated herein by reference in its entirety.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US04/00765 | 1/9/2004 | WO | 7/20/2005 |
| Number | Date | Country | |
|---|---|---|---|
| 60439190 | Jan 2003 | US |
