Method for recovering a gaseous boron trifluoride bf3 and the usage of the product formed in the method
BACKGROUND OF THE INVENTION 
     It is well known to prepare poly-α-olefines, which can be used e.g. as a lubricant or as a component thereof, by using a complex of BF 3  and a co-catalyst as a catalyst, as described e.g. in U.S. Pat. Nos. 3,780,128 and 4,434,309. A catalyst complex is separated by distillation from the poly-α-olefine to be obtained as a reaction product, and the catalyst complex can thereafter be reused for catalyzing a similar polymerization reaction (see, e.g. FI Patent No. 80 891). 
     When separating the catalyst complex from the reaction product by distillation, a small portion (less than 10%) of this complex decomposes and the gaseous BF 3  is released, causing a chemical loss. Due to this chemical loss, this compound (BF 3 ) which is hazardous to environment, has to be recovered e.g. by means of a washer. 
     In order to avoid the decomposition of the catalyst complex, the distillation is performed in a reduced pressure, and thereby in a lower temperature. The underpressure can be achieved by means of a fluid ring pump or a torque pump (a fluid ejector pump). Usually, the fluid ring pump, which can be a piston pump, a centrifugal pump, rotary sealed pump etc., is sealed with a fluid ring, wherein the fluid is water or an inert fluid with respect to the gases to be removed. The efficiency of the fluid-ring and/or torque pump may be further increased by placing a mechanical blaster (e.g. a rotary piston pump) in series with said pump. 
     SUMMARY OF THE INVENTION 
     The present invention relates to a method for recovering a gaseous boron trifluoride BF 3  from the exhaust gases of an underpressure distillation, and to the use of the product formed in the method. 
     The present invention further relates to a method, by means of which the decomposition of the catalyst complex, i.e. the release of the boron trifluoride BF 3 , may be further reduced or totally prevented. 
     The present invention further relates to the removal of a gaseous boron trifluoride from the exhaust gases of a vacuum pump when polymerizing α-olefines by using a boron trifluoridi/alcohol complex as a catalyst. 
     More particularly, in the method of the present invention the underpressure is caused either by a fluid ring pump or a torque pump, wherein the fluid ring or correspondingly the fluid moments are achieved by means of a complex formed by a liquid BF 3  and a C 1  -C 15  alcohol, or by means of a fluid jet of this alcohol. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     The following drawings are illustrative of embodiments of the invention and are not meant to limit the scope of the invention as encompassed by the claims. 
     FIG. 1 shows a device used in a method in accordance with the present invention wherein a pump, heat exchanger and separating container are used in the boron recovery process. 
     FIG. 2 shows another embodiment of the present invention wherein a torque pump is used in combination with a propellant circulating pump and separating container. 
     FIG. 3 shows another embodiment of the present invention wherein an ejector pump and a fluid ring pump are placed in a series. 
     FIG. 4 shows an embodiment of the present invention as illustrated in FIG. 2 wherein a heat exchanger is provided between the torque pump and separating container. 
     FIG. 5 shows an embodiment of the present invention as illustrated in FIG. 3 wherein a heat exchanger is provided between the ejector pump and the separating container. 
     FIG. 6 shows an embodiment as illustrated in FIG. 2 wherein a heat exchanger is provided between the ejector pump and the propellant circulating pump. 
     FIG. 7 shows an embodiment of the present invention as illustrated in FIG. 1 wherein a mechanical blaster is arranged in series with a fluid ring pump. 
    
    
     DETAILED DESCRIPTION 
     In one embodiment of the present invention, a fluid ring pump is used during the distillation for reducing the pressure, wherein the fluid ring is formed by a C 1  -C 15  alcohol to be used as a co-catalyst of a catalytic BF 3  and forming complex with BF 3 . The alcohol used is preferably a relatively short-chained monoalcohol, e.g. butanol. 
     In another embodiment of the present invention, a torque pump (an ejector pump) is used as a pressure-reducing pump, in which the fluid moment, i.e. in practice the fluid jet, is formed by the fluid jet of the co-catalyst. 
     The BF 3  -alcohol complex formed as a product of the method can be reused as a catalyst, preferably when polymerizing poly-α-olefines. 
     The pressure range in which the pump can be used essentially depends on the requirements related to the distillation. The absolute pressure is usually less than 50 kPa, even 1 kPa. However, the pressure is not a limiting factor, since the method can always be used when it is desirable to pump gases with a fluid ring pump and/or a pump of an ejector type, possibly assisted by a mechanical blaster, in which the gas and the fluid can be intimately mixed with each other. The temperature to be used during the pumping depends on the boiling point (the steam pressure) of the selected alcohol and the cooling mode. The temperature range is generally from about 20° to about 60° C. Either a water or air cooling, or both together, can be used. 
     In the fluid ring, when the co-catalyst is the substance forming the fluid ring or the substance to be jetted in the fluid jet, the complex between the catalyst, i.e. BF 3 , and the co-catalyst forms immediately when these materials come into contact with each other in the underpressure pump. The complex formed can be recovered, returned to a reactor and reused as polymerization catalyst. 
     BF 3  and the alcohol which have come into contact with each other form a complex in such a way that all BF 3  to be removed binds to the alcohol, whereby the loss and emission of the catalyst into the surrounding atmosphere is totally avoided. 
     FIGS. 1-7 show different equipment arrangements by which the present invention can be applied. 
     When separating the catalyst complex from the reaction product, the gaseous components or vacuum gases separating therefrom enter the fluid ring pump or the ejector pump 1 (possibly assisted by a mechanical blaster, e.g. a rotary piston pump), by means of which they are pumped into a separating container 2, from which the pure gases, i.e. those not containing the catalyst, the recovered catalyst complex and the mixture to be circulated, are removed. 
     The mixture to be circulated is then returned to the pump, for example in a cooled state. This can be accomplished by means of a heat exchanger 3. Alternatively, the cooling can occur after the pump as shown in FIG. 4. 
     If the pump for the vacuum gases is a torque pump, a separate propellant circulating pump 4 is needed, as shown in FIGS. 2, 4 and 6. 
     The alcohol forming a complex with BF 3  and forming the fluid ring of the pump or forming the fluid jet of the ejector pump is added either to the separating container 2, as shown in FIGS. 1, 3 and 5, or just before the separate propellant circulating pump 4, as shown in FIGS. 2, 4 and 6. 
     It is also possible to use several pumps when desired. As an example, FIG. 3 depicts an arrangement of an ejector and fluid ring pump placed in series. 
     FIG. 7 shows the use of a blaster, e.g. a propellant circulating pump, in series with a fluid ring pump.