A METHOD FOR THE REMOVAL OF TICL4-VAPOUR FROM GAS-STREAMS

Abstract: A method for the removal of TiCl₄-vapour from gas-streams which comprises conducting under anhydrous conditions a gas-stream over a bed of a solid material containing hydroxyl groups, while adsorbing the TiCl₄ on the solid material under liberation of hydrogen chloride and then regenerating the solid material by treating with water or steam and reusing the regenerated bed of solid material for the removal of TiCl₄-vapour from gas-streams.

Description: The invention relates to a method for the removal of TiCl₄-vapour from gas-streams. The presence of TiCl₄ in gas-streams, such as waste gas-streams, poses an important problem, when these gases are emitted in the atmosphere. In the literature several methods for the removal of TiCl₄-vapour have been described. In the US patent specification 2,682,930 has been described a method for separating and recovering TiCl₄ from a residual gas mixture with the aid of adsorbent carbon. The TiCl₄ can be recovered uncompletely from the carbon, but the used temperatures are high and the process is carried out under anhydrous conditions. In the US patent specification 4,474,587 has been described a process for the treatment of waste gas, wherein activated carbon is used to adsorb the TiCl₄ in the waste gas. A disadvantage of carbon is that after a partly recovery of TiCl₄ from the carbon, the latter still contains a great deal of reactive TiCl₄ which must still be destroyed and neutralized. In the USSR patent specification 990,273 has been described a method for the removal of TiCl₄-vapour from industrial waste gases by passage over a porous sorbent coated with metallic copper. Regeneration of the sorbent is complicated. It is also known to treat TiCl₄-vapour containing waste gas with an aqueous calcium hydroxide solution, followed by an aqueous sodium hydroxide solution (see the US patent specification 4,474,587). Applicant has found that when using a caustic scrubber in the removal of TiCl₄-vapour an acidic mist in the scrubber overheads system is formed, pipelines are plugged and operational problems exist. In the US patent specification 4,157,374 is disclosed a process for the purification of waste gases, containing up to 15% by weight of gaseous metal chlorides by passing the waste gases through a bed of activated carbon to remove the metal chlorides, passing stripping gas through the bed and passing stripping gas and entrained gaseous metal chlorides through a bed of metal oxides of the groups IIA, IIIA, IVA or IVB while contacting the gases with water vapour. Hydrogen chloride from the feed gas and liberated by hydrolysis of metal chlorides, is absorbed in water. The process is costly because of the expense of heat and gases needed to generate the carbon adsorbers and the need to replace spent activated carbon (see the description in US patent specification 4,209,496). In the US patent specification 4,209,496 is disclosed an improved process for treating waste gases, however no mention is made that the bed of metal oxides can be regenerated. Applicant has now found a method for the removal of TiCl₄-­ vapour from gas-streams which comprises conducting under anhydrous conditions a gas-stream over a bed of a solid material containing hydroxyl groups, while adsorbing the TiCl₄ on the solid material under liberation of hydrogen chloride and then regenerating the solid material by treating with water or steam and reusing the regenerated bed of solid material for the removal of TiCl₄-vapour from gas-streams. The regeneration of the solid material is carried out with water or steam, e.g. at a temperature between 120 °C and 250 °C. The gaseous TiCl₄ in the gas under anhydrous conditions reacts with the hydroxyl groups of the solid material under liberation of hydrogen chloride. The solid material is preferably a metal oxide. Numerous metal oxides, even after calcining, contain still hydroxyl groups on their surface. Examples are alumina, silica and titanium dioxide. The TiCl₄ is bound via O-atoms with the metal oxide surface, but still Cl-atoms remain, which latter will react with water or steam to form again hydroxyl groups under liberation of hydrogen chloride. At this stage the solid material is regenerated. When water or steam is added at the same time that TiCl₄ is conducted over the solid material rapid plugging of the solid material bed occurs and pressure drop takes place and makes the process unsuitable to be further carried out. The adsorbent is preferably the spent silica based titanium dioxide catalyst for the reaction of propylene with ethylbenzene hydroperoxide to prepare propylene oxide and alpha-phenyl ethanol. The method according to the invention has the advantage that the solid material containing hydroxyl groups can be regenerated and reused a number of times, e.g. ten times, but more times are not excluded. The method has moreover the advantage that no mist is formed and no plugging occurs. The gas-streams which have been conducted through a bed of solid material containing hydroxyl groups may further be conducted through water, preferably through a basic aqueous solution in order to dissolve and neutralize the liberated hydrogen chloride. The gas-streams containing neither TiCl₄ nor hydrogen chloride may be emitted into the atmosphere. In an integrated process the hydroxyl groups containing material is a guard bed installed between the vessel where the TiCl₄ containing gas is produced and the caustic scrubber where the acidic components are collected, before the gas may be emitted in the atmosphere. The guard bed prevents the formation of mist and solids in the caustic scrubber. The guard bed is easy to operate. Generally the absorption of the TiCl₄ takes place at atmospheric pressure or superatmospheric pressure. The temperature at which the absorption takes place may range from room temperature 20 °C up to 300 °C, preferably a temperature between 100 °C and 250 °C. Example A gas-stream containing TiCl₄-vapour and nitrogen was made by leading nitrogen gas through a flask containing liquid TiCl₄. The N₂-flow containing TiCl₄-vapour was conducted through a guard bed of 110 ml at a temperature of 200 °C and further led into a one metre long packed glass scrubbing column, at the top of which water flowed down which was collected at the bottom and again recycled to the top of the column. The guard bed consisted of spent titanium dioxide catalyst on silica. 40 litres of nitrogen loaded with in total 2 g TiCl₄ were passed through the guard bed before a dense mist appeared, indicating a TiCl₄ breakthrough of the bed. The experiment was repeated, but just before the breakthrough could take place, the nitrogen flow was halted. In one hour 40 ml water in the form of steam were passed through the guard bed at 200 °C, after which the bed was stripped with dry pure nitrogen for 30 min. Again 38 litres of nitrogen containing 2 g TiCl₄ could be passed over the guard bed. 40 ml water in the form of steam was then passed through the guard bed, after which the bed was stripped with dry nitrogen again. The procedure was repeated, but the absorption of the TiCl₄ was stopped after 35 litres of nitrogen loaded with TiCl₄-vapour had been led over the guard bed, before regenerating. The test was ended after 14 cycles of loading and regeneration, without having observed the occurrence of mist in the scrubber at any time. After drying it appeared that the 110 ml guard bed (weight 46 g) had gained 12 g in weight.

Claims: 1. A method for the removal of TiCl₄-vapour from gas-streams which comprises conducting under anhydrous conditions a gas-stream over a bed of a solid material containing hydroxyl groups, while adsorbing the TiCl₄ on the solid material under liberation of hydrogen chloride and then regenerating the solid material by treating with water or steam and reusing the regenerated bed of solid material for the removal of TiCl₄-vapour from gas-streams. 2. A method as claimed in claim 1, wherein the absorption of TiCl₄ is carried out at a temperature from 20 °C to 300 °C. 3. A method as claimed in claim 1 or 2, wherein the regeneration is carried out with steam at a temperature between 120 °C and 250 °C. 4. A method as claimed in any one of the claims 1-3, wherein the solid material is a metal oxide. 5. A method as claimed in claim 4, wherein the solid material is alumina, silica or titanium dioxide. 6. A method as claimed in claim 5, wherein the solid material is spent silica based titanium dioxide catalyst. 7. A method as claimed in any one of the claims 1-6, wherein the gas-streams containing hydrogen chloride are conducted through water after leaving the bed of solid material. 8. A method as claimed in claim 7, wherein the gas-streams are conducted through a basic aqueous solution.

Inventors: REMAN, WILLEM GEORGE
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1987
Main classification: B01D53
IPC codes: B01D53