Method of producing allylacetate
The present invention relates to producing unsaturated esters of carboxylic esters and more particularly to a method of producing allylacetate which can be used as a starting material in chemical and petrochemical industries for preparing various products of organic synthesis as well as a range of polymer materials. 
     Known in the art is a method of producing allylacetate by oxyacetylation of propylene with acetic acid and oxygen in a gaseous phase at a temperature from 150°-250° C under a pressure of 1-10 atg in the presence of a catalyst containing a palladium salt, for example, palladium acetate, and activators on a support, mainly, aluminium oxide or silicic acid. 
     Salts of bismuth, copper, vanadium, sodium, potassium and other metals are used as activators. The process is carried out both in a stationary and in a fluidized bed of a catalyst. 
     The yield of allylacetate per litre of a catalyst per hour is 430-495 g/1.hr when the process is run in a stationary bed of a catalyst. 
     In case the process is conducted in a fluidized bed of a catalyst, the yield of allylacetate is 790 g/l.hr. 
     The principal disadvantage of the known methods is a low yield of allylacetatate per litre of a catalyst per hour due to poor efficiency of the catalyst. 
     The object of the invention is to increase the yield of allylacetate. 
     Said object is accomplished in a method of producing allylacetate by oxyacetylation of propylene with acetic acid and oxygen in a gaseous phase at a temperature from 150°-250° C under a pressure of 1-10 atg in the presence of a catalyst containing a palladium salt and activators on a support, according to the invention, as a palladium salt use being made of a complex salt thereof, namely, tetraamonium palladium acetate of the formula / Pd(NH 3 ) 4  /(CH 3  COO) 2 . 
     To increase the yield of allylacetate it is expedient to use a catalyst containing 1-10 wt % of tetraammonium palladium acetate. 
     To increase the catalyst efficiency it is preferable to use a mixture of zinc acetate and sodium acetate with copper acetylacetonate or copper acetate as activators. 
     The proposed method is realized as follows. 
     A vapour-gas mixture of propylene, acetic acid, and oxygen is passed through a reactor loaded with a catalyst at 150°-250° C and 1-10 atg. Said vapour gas mixture is condensed after leaving the reactor with subsequent isolation of the desired product. 
     The process is run in a stationary bed of the catalyst. 
     The catalyst contains tetraammonium palladium acetate in an amount of 1-10% of the total weight of the catalyst, 2.5 wt% of copper acetylace tonate or copper acetate, and 10 wt% of a mixture of zinc and sodium acetates in a ratio of 1:1 on a support, aluminium oxide thermally treated at 900° C being used as the support. 
     The catalyst is prepared in the following way. A 20% solution of NH 3  is added to an aqueous solution of tetraammonium palladium acetate up to pH = 12. The solution temperature is raised to 40°-50° and then copper acetylacetonate or copper acetate, sodium acetate, and zinc acetate are dissolved in succession in said solution at 40°-50° with stirring. The impregnation of aluminium oxide with the resulting solution is performed at 50° C. The support is kept in said solution for 4 hours, after which excess solution is decanted and the wet catalyst is dried at 85°-90° under a residual pressure of 300-350 mm Hg to a moisture content of 1%. 
     The use of tetraammonium palladium acetate as the main component of the catalyst increases the yield of allylacetate per litre of the catalyst per hour up to 2,180 g/1.hr due to enhancing the catalyst efficiency. 
     For a better understanding of the present invention specific examples of realizing the proposed method are given hereinbelow by way of illustration. 
    
    
     EXAMPLE 1 
     250 ml of a catalyst containing 2.0 wt % of tetraammonium palladium acetate, 2.5 wt % of zinc and sodium acetates in a 1:1 ratio deposited on aluminium oxide are put into a reactor. A vapour-gas mixture containing 3,000 nl/hr of propylene, 200 nl/hr of oxygen, and 800 g/hr of acetic acid is passed through the catalyst at 210° C under 5 atg. The vapour-gas mixture leaving the reactor is condensed and rectified. The yield of allylacetate is 1,435 g per litre of the catalyst per hour. 
     EXAMPLE 2 
     250 ml of a catalyst containing 10.0 wt % of tetraammonium palladium acetate, 2.5 wt % of copper acetylacetonate, and 10 wt % of a mixture of zinc and sodium acetates in a 1:1 ratio deposited on aluminium oxide are put into a reactor. A vapour-gas mixtureof propylene, oxygen, and acetic acid in amounts as described in Example 1 is passed through the catalyst at 210° under 5 atg. 
     The yield of allylacetate is 1,560 g per litre of the catalyst per hour. 
     EXAMPLE 3 
     250 ml of a catalyst containing 4.2 wt% of tetraammonium palladium acetate, 2.5 wt % of copper acetylacetonate, and 10 wt % of a mixture of zinc and sodium acetates in a 1:1ratio deposited on aluminium oxide are put into a reactor. A vapour-gas mixture containing propylene, acetic acid, and oxygen in amounts as described in Example 1is passed through the catalyst. 
     The yield of allylacetate is 1,135 g per litre of the catalyst per hour. 
     EXAMPLE 4 
     250 ml of a catalyst the composition of which is similar to that described in Example 3 are put into a reactor. A vapour-gas mixture containing 3,000 nl/hr of propylene, 200 nl/hr of oxygen, and 800 g hr of acetic acid is passed through the catalyst at 210° C under 6 atg. 
     The yield of allylacetate is 1,845 g per litre of the catalyst per hour. 
     EXAMPLE 5 
     250 ml of a catalyst the composition of which is similar to that described in Example 3 are put into the reactor. A vapour-gas mixture having the composition similar to that described in Example 4 is passed through the catalyst at 210° under 7 atg. 
     The yield of allylacetate is 2,180 g per litre of the catalyst per hour. 
     EXAMPLE 6 
     250 ml of a catalyst the composition of which is similar to that described in Example 3 are put into the reactor. A gas mixture containing 3,000 nl/hr of propylene, 200 nl/hr of oxygen, and 800 g/hr of acetic acid is passed through the catalyst. 
     The yield of allylacetate is 2,020 g per litre of the catalyst per hour. 
     EXAMPLE 7 
     250 ml of a catalyst containing 4.2 wt % of tetraammonium palladium acetate, 2.5 wt% of copper acetate, and 10 wt % of a mixture of zinc and sodium acetates in a 1:1ratio are put into a reactor. 
     A mixture of propylene, acetic acid, and oxygen in amounts similar to those described in Example 6 is passed through the catalyst at 190° under 5 atg. 
     The yield of allylacetate is 1,180 g per litre of the catalyst per hour. 
     EXAMPLE 8 
     250ml of a catalyst containing 10 wt % of tetraammonium palladium acetate, 2.5 wt % of copper acetate, and 10 wt % of a mixture of zinc and sodium acetates in a 1:1 ratio is put into a reactor. A mixture of propylene, oxygen, and acetic acid in amounts similar to those described in Example 6 is passed through the catalyst at 210° under 5 atg. The yield of allylacetate is 1,530 g per litre of the catalyst per hour.