T 0658/90 (Saddles/NIPPON) 24-02-1994

1. The appeal is admissible.

2. The amendments in the claims meet the requirements of Article 123(2) and (3).

3. The request for correction pursuant to Rule 88 in Claim 1 is allowable since it is immediately apparent that the terms "ehtylene", "siler" and "cc" are erroneous and that the only possible correction the skilled person would think about when reading the patent in suit is the following: "ethylene", "silver" and "cm3" respectively.

4. None of the cited documents discloses a silver catalyst for the production of ethylene oxide containing an alkali metal promoter and having a carrier in the shape of Intalox saddles or Berl saddles with the dimensions defined in Claim 1. Therefore the catalyst according to Claim 1 is novel. This not being in dispute there is no need to give further details.

5. The problem underlying the invention was defined in the patent in suit taking the processes and catalysts of document (8) or document (9) as the starting point in the prior art. These documents disclose silver catalysts for the production of ethylene oxide by catalytic vapour phase oxidation of ethylene with molecular oxygen in the presence of a halogenated inhibitor, comprising silver and at least one accelerator selected from the group consisting of alkali metals and alkali metal compounds deposited on a porous inorganic refractory carrier, i.e. silver catalysts as defined in the preamble of Claim 1. The silver catalyst of document (8) is prepared by a method including the succession of steps as defined in the amended Claim 7 of the patent in suit whereas the method of manufacture of the silver catalyst according to document (8) comprises the succession of steps defined in the amended Claim 8. The carrier used in the silver catalysts of document (9) is in the form of pellets or rings, the average equivalent diameter of which lies with the range of 3 to 20 mm, preferably 3 to 10. mm (cf. column 4, lines 46-50).

The catalyst of document (9), contrary to the catalyst of document (2) considered by the Opposition Division as closest prior art, contains the same promoter as the claimed catalyst. Furthermore, it is used for the production of ethylene oxide in the presence of a halogenated inhibitor in opposition to the catalyst of document (2). Therefore, document (9) is considered by the Board to represent the closest prior art.

5.1. According to the patent in suit, the catalysts of documents (8) and (9) are not fully satisfactory in selectivity (cf. page 2, lines 35-49). Starting from (9) as closest prior art, the problem underlying the patent in suit can be seen in providing a silver catalyst for the production of ethylene oxide in the presence of a halogenated inhibitor, which catalyst exhibits an improved selectivity to ethylene oxide.

It is proposed to solve this problem by using a carrier in the shape of Intalox saddles or Berl saddles having the dimensions recited in Claim 1. Furthermore, the carrier has a specific pore volume in the range of 0.06 to 1.0 cm3/g. The pore volume, which is not mentioned in the closest prior art, was however not alleged to be responsible for the improvement in selectivity.

It is indicated in the patent in suit that the claimed catalysts suffer only minimal pressure loss in the catalyst bed. However, as pointed out by the Appellant in the appeal statement, the comparative examples of the patent in suit show that the pressure loss obtained with a carrier in the form of Berl saddles or Intalox saddles is about the same as the pressure loss of a catalyst comprising Raschig rings (cf. examples 4 and 5 compared to control example 8 or example 1 compared to control example 2). Accordingly, an improvement in the pressure loss cannot be taken into consideration for the definition of the problem.

5.2. The question arises whether the problem defined above has been solved by the features recited in Claim 1. The Appellant has not contested that a slight improvement in selectivity to ethylene oxide is achieved with the catalysts of the invention over those of the prior art. However, the Appellant has argued that it could not be derived from these comparative examples, in particular from example 1 and control example 2 on the one hand and from examples 4 and 5 and control example 8 on the other hand, that this slight improvement was attributable to the different shape of the carrier since not only the shape has been changed but also other parameters having an influence on the selectivity.

The catalysts of table 2 were prepared by the method of the closest prior art. The carriers of examples 4 and 5, i.e. Intalox saddles and Berl saddles exhibit the same pore volume, BET surface area and ratio of apparent surface area/apparent volume as the Raschig rings of the comparative control example 8, however their packed specific gravities are higher. The silver contents of the corresponding catalysts have accordingly been adapted so that the three tested catalysts contain similar amounts of silver in the packed bed. These catalysts were prepared by the same method and under the same operating conditions except for the silver oxalate concentration in the solution to be impregnated, which was slightly lower in the examples 4 and 5 than in the control example 8, and for the temperature of the final treatment at high temperature (550-950 C) in nitrogen. The latter was performed at 630 C in examples 4 and 5 and at 640 C in control example 8.

Although different concentrations of the silver salt in the impregnation solution may have an influence on the distribution of the silver on the surface of the carrier and therefore on the selectivity, as pointed out by the Appellant, the differences of concentration in the compared examples are not so great that it could be prima facie concluded that they affect the selectivity. Likewise, the difference of 10 C between temperatures lying in the order of 630 C is relatively small so that no prima facie conclusion can be drawn on its possible influence upon the selectivity. It is indeed derivable from document (9) that the final treatment at a temperature between 550-950 C improves the selectivity to ethylene oxide in comparison with a catalyst which was not submitted to this heat treatment, however it does not follow therefrom that the difference of 10 C in the temperature of this heat treatment would be responsible for the improvement in selectivity. In this context it is further observed that the catalysts of examples 9 and 10 of table 3 (Intalox saddles and Berl saddles) exhibit an improved selectivity over the control example 13 (Raschig rings) although a heat treatment at high temperature (630 or 640 C) was not performed.

In connection with the different packed specific gravities, it should be noted that if the Intalox saddles have the same packed specific gravity as the Raschig rings, the improvement in selectivity over the catalyst in the form of Raschig rings is still achieved: cf. table 1, example 1 and control example 2. The pore volume in control example 2 is indeed lower than in example 1 (0.27 cm2/g instead of 0.32), however the Appellant has not shown that this lower pore volume would impair the selectivity of the catalyst of control example 2, which on the other hand exhibits a greater ratio of apparent surface area/apparent volume.

As regards the different reaction temperatures which the Appellant has made the basis of an objection at the oral proceedings, it is observed that these temperatures are those which give the same ethylene conversion of 13%. No evidence has been brought to show that the lower selectivity of the control catalyst 8 results from the difference of 7 C in the reaction temperatures (239 C for control example 8 and 232 C for example 5) and not from the different shapes.

The Appellant's assumption that the slight improvement in selectivity results from parameters other than the different shapes of the carrier is not in agreement with the statement in the patent in suit that the replacement of the Raschig rings by Intalox saddles or Berl saddles leads to a catalyst exhibiting a heretofore unattainable high selectivity. Furthermore, as indicated above, the Appellant has brought no evidence that the discussed other differences are so great that they are responsible for the improvement in selectivity. In such a situation where the Opponent makes an assertion which is contrary to the teaching of the patent in suit without bringing any evidence to substantiate this assertion, which is contested by the Patentee, the Board has to decide in favour of the party not having the burden of proof, i.e. in the present case the Respondent (cf. T 219/83, OJ EPO, 1986). The Appellant's argument that parameters which might affect the selectivity have been changed in addition to the shape of the carrier is certainly not sufficient to reverse the burden of proof. In these circumstances, the Board concludes that in the absence of evidence to the contrary, it is credible in view of the examples and control examples of the patent in suit and of the statements at page 3, lines 26 to 31, and page 4, lines 2 to 9, that the technical problem has been solved by the shape and dimensions of the carrier defined in Claim 1.

5.3. Neither document (9) nor document (8), which are both concerned with the problem of improving the selectivity of the silver catalyst to ethylene oxide, suggests that this selectivity might be improved by a catalyst in the shape of saddles.

5.4. Document (2) aims at providing a silver catalyst for the partial oxidation of ethylene to ethylene oxide, which avoids the necessity of using a halogenated inhibitor and permits improved productivity and/or a lower operating temperature. This is achieved by selecting a carrier having an apparent porosity greater than 30% and pore diameters as well as an average pore diameter which fall within well defined ranges (cf. pages 4 and 5, Claim 1). According to (2) these features give the optimum combination of ethylene oxide selectivity and catalyst activity (see page 7, first paragraph and page 15, table II). Thus, the improvement in selectivity is not attributed to the shape of the support but to the particular pore dimensions of the carrier.

Document (2) further teaches that the carrier may take almost any geometrical configuration, the configuration being suitably cylindrical, spheroidal or spherical from the standpoint of simplicity (cf. page 7, last paragraph). Spherical pellets are used in the examples. According to page 8, first paragraph, engineering factors such as the ability to pack uniformly, the mechanical strength, the pressure drop and the stability may influence the choice of the configuration. Accordingly the use of more complicated shapes, such as saddles or rings, may be necessary. This teaching does not suggest that the selectivity of the catalyst might be improved by using these more complicated configurations, let alone that saddles might lead to an improved selectivity over rings. Therefore, the skilled person would not be prompted in view of document (2) to replace the rings by saddles in the catalyst of document (9) in order to improve the selectivity to ethylene oxide.

5.5. Documents (3) and (3a) relate to packing materials which are used in particular for distillation. Different kinds of packing materials such as spheres, Raschig rings, Pall rings, Berl saddles, Intalox saddles, Torus saddles, Super saddles, Novolax saddles are disclosed, as well as the dimensions in which they are available. According to (3a) Berl saddles exhibit the most perfect mathematical configuration with the correspondingly favourable effect on the performance in the distillation and rectification of mixture of compounds with close boiling ranges. Intalox saddles are said to have a lower resistance to passage than the Berl saddles (cf. page 1199). These packing materials can be used in the field of catalysis and catalysts can be deposited thereon (cf. (3) page 2231). In document (4) which exclusively concerns distillation, there are also references to Raschig rings, Pall rings, Berl saddles, Intalox saddles and Torus saddles.

These documents do not contain a reference to the catalytic production of ethylene oxide nor do they deal with the problem of improving the selectivity of the silver catalysts used in the said reaction. Therefore, they would be of no assistance to the skilled person confronted with the problem of how to improve the selectivity of the catalysts of (9), even in combination with the teaching of document (2), since the latter indeed mentions the possible use of saddles or rings instead of spherical pellets but not for improving the selectivity to ethylene oxide.

5.6. The Appellant alleged for the first time at the oral proceedings that a decrease of the pressure drop results in a shorter contact time of the gases with the catalyst and thus in an increase of the selectivity. The Respondent's representative pointed out that this relationship was not derivable from the cited documents. The Board also has doubts as regards the alleged predictable effect on the selectivity since in the case of the decrease in pressure drop being due to a different geometrical configuration, in particular a more sophisticated shape such as saddles, not only the gas velocity is changed but also other parameters which depend upon the shape of the carrier and may have an influence on the selectivity. Furthermore, the Appellant did not consider the effect on the conversion. It should be noted in this respect that the improvement of selectivity is achieved at the same ethylene conversion in the examples of the patent in suit. In these circumstances and taking into account that the Opponent's allegation was not supported by any evidence, the Board has to decide in favour of the Patentee on whom the burden of proof does not rest.

5.7. Document (5) relates to the influence of the catalyst shape and catalyst arrangement on the conditions governing the reaction in tubular reactors. Reference is made to reactions such as the production of phthalic anhydride, ethylene oxide, maleic anhydride or methanol in fixed-bed tubular reactors. The part of this article submitted (i.e. the introduction) contains only general considerations. There is disclosed that an increase of the flow velocity improves the dissipation of heat produced by the exothermic reaction, that a reduction of the pressure drop in the bed would be of interest in order to make possible an increase of the flow velocity without raising the energy costs and that, consequently, catalyst shapes and arrangements which are more favourable to the flow have been discussed from time to time (cf. page 2, first paragraph). Although the reactor-bed heat transfer is a factor which may affect the selectivity, the latter is not discussed at all in (5) let alone other factors which depend upon the carrier shape and may also influence the selectivity. Therefore, the general teaching of (5) considered in combination with documents (2), (3), (3a) and (4) would not give the skilled person an incentive to replace the rings of the catalyst of (9) by Berl saddles or Intalox saddles as defined in Claim 1 in order to improve the selectivity to ethylene oxide.

The two remaining documents (6) and (7) which, like (5), were cited after the opposition period are less relevant than the preceding documents. They only disclose spheres, cylinders or rings as catalyst shapes and give their diameter as well as the reactor diameter. Selectively is only mentioned in (7) in connection with the use of a chlorinated inhibitor (cf. page 223). Therefore the teaching of these documents cannot change the preceding findings.

5.8. It follows from the above that it was not obvious to arrive at the claimed catalyst in view of the cited prior art. Therefore, the subject-matter of Claim 1 is considered to meet the requirements of inventive step set out in Article 52(1) and 56 EPC.

6. The methods for the preparation of this catalyst as defined in Claims 7 and 8 derive their patentability from that of the product claim. Claim 1 being allowable, the same applies to the dependent Claims 2 to 6 whose patentability is supported by that of Claim 1.