In re Mattox

461 F.2d 826, 59 C.C.P.A. 1272, 174 U.S.P.Q. (BNA) 155, 1972 CCPA LEXIS 305
CourtCourt of Customs and Patent Appeals
DecidedJune 15, 1972
DocketNo. 8723
StatusPublished
Cited by2 cases

This text of 461 F.2d 826 (In re Mattox) is published on Counsel Stack Legal Research, covering Court of Customs and Patent Appeals primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
In re Mattox, 461 F.2d 826, 59 C.C.P.A. 1272, 174 U.S.P.Q. (BNA) 155, 1972 CCPA LEXIS 305 (ccpa 1972).

Opinion

Bich, Actmg Ghief Judge.

This appeal is from the decision of the Patent Office Board of Appeals affirming the rejection of claims 1-19 in appellants’ application serial No. 469,895, filed July 6, 1965, as a continuation-in-part of their application serial No. 168,548, filed January 24, 1962. We affirm.

The Subject Matter Claimed

Appellants claim certain hydrocarbon cracking processes employing “dual-exchanged,” crystalline, aluminosilicate zeolites as catalysts. The word “dual-exchanged” means that the zeolites, or “molecular sieves,” used in these processes have had most of their initial alkali-metal.-cation content replaced'by means-of base exchange with both (1) hydrogen ions and/or hydrogen ion precursors, such as ammonium ions and (2) cations of metals from groups IB through YIII of the Periodic Table. Claim 1, which we have subdivided for clarity, is illustrative:

1. In the catalytic cracking of a hydrocarbon oil to produce hydrocarbons of lower boiling range, the improvement of
contacting said oil under cracking conditions with a crystalline alumino-silicate
having an ordered crystalline'structure-'having' from 0.5' to 1.0 equivalent per gram atom of aluminum of ions of positive valence of which no more than 0.25 equivalent are alkali metal cations and
[1273]*1273baving associated with said crystalline aluminosilicate both hydrogen ions and ions capable of conversion to hydrogen ions and
cations of metals selected from Group IB through Group VIII of the Periodic Table,
said metal cations, hydrogen ions and ions capable of convension to hydrogen ions being associated with the aluminosilicate as a result of base exchange.

Claims 4-8 recite only ammonium ions for the first-recited base exchange, and claims 9-19 recite that the first-recited base exchange is made with hydrogen ions or ions capable of conversion to hydrogen ions. The metal cations are more specifically recited in claims 3, 6r 10, and 19 as alkaline earth metal cations, in claims 9, 11, 12, and 17 as “metal cations other than alkali metal cations,” in claims 13-16 as magnesium, zinc, strontium, and calcium ions, respectively, and in claim 18 as “selected from the group consisting of alkaline earth metals and zinc.” Claim 11 specifies a silica-to-alumina mol ratio “greater than 3,” claim 12 a silica-to-alumina mol ratio “greater than 4 to 6,” and claims 18 and 19 a silica-to-alumina mol ratio “between 3 and 6.” Claim 17 recites that “said zeolite has uniform pore openings; between 6 and 15 Angstrom units,” and claims 18 and 19 recite that the zeolite has “uniform pore openings between about 6 and 15' Angstrom units.”

Claims 1, 2, 4, '5, 7, and 8 were copied verbatim from the Frilette et al. patent No. 3,140,252 for purposes of interference. Claims 3 and 6 were “substantially copied in modified form” from the same patent • for the same purpose, according to appellants’ declaration under Rule-205 (b). Also according to that declaration,

* * * the remaining claim of the instant application, i.e. claims 9 through 19, are directed, to substantially the same invention claimed in U.S. Patent 3,140,252: [1] and are submitted" as alternates to the above claims for purposes of interference.

The Rejections

The prosecution history of this case, in which a multiplicity of rejections, have been made, has been unusually confused. However, the-solicitor has commendably volunteered to “simplify the issues” by regarding certain of the bases for the rejections made below as “cumulative.”

The references are:

Urilette et al. No. 3,140,252, issued July 7, 1964, on application serial No. 343^489, filed Feb. 10,1964, purporting to be a division of serial No. 161, 242, filed Dee. 21, 1961.
Prilette et al. No. 3,140,322, issued July 7, 1964, on application serial No. 754,915, filed Aug. 14,1958.

[1274]*1274We shall refer to these references as the ’252 and ’322 patents.

The two rejections which the solicitor now asks us to sustain are of claims .1-19 as obvious in view of the ’322 patent, under 35 USC 103, and of claims 1-19 as anticipated by the ’252 patent under 35 XJSO102. The determinative issue as far as the second ground of rejection is con-; cerned is whether appellants’ claims are supported by their parent application, serial Ho. 168, 548, for the solicitor has conceded that, if they are,

* * * the Rule 204(b) affidavit [which appellants submitted] * * * which alleges completion of the claimed invention prior to December 21, 1961, should be sufficient to remove ’252 as a reference under Section 102. [2]

Both the ’322 patent and the ’252 patent were assigned to Socony Mobil Oil Company, Inc. Appellants’ application appears to be assigned to Esso Research and Engineering Company.

Opinion

I. OBVIOUSNESS IN VIEW OP THE ’322 PATENT

The ’322 patent sets forth processes for selectively conducting organic chemical reactions by employing a crystalline, aluminosilicate zeolite containing an added catalyst. In other words, it is basically concerned with single-exchanged zeolites. However, it discloses' that “molecular sieve[s] of the ‘A’ series [i.e., those having pore diameters-of approximately 4 and 5 angstroms] are ordinarily prepared initially in the sodium form of the crystal” and that “the sodium ions * * * - may be replaced partially or completely by other cations,” including, inter1 alia, calcium, magnesium,strontium, and zinc, prior to addition of the added catalyst. It also discloses that “Molecular sieves of the ‘X’ séries [i:e., those having pore diameters of approximately 10 to 13 angstroms] [1275]*1275are prepared in a manner similar to that described hereinabove for preparation of molecular sieves of the ‘A’ series” and explains the differences in the manufacture of the two. The exact pore size of both series will differ depending upon which ion is used to replace the sod-dium ion, a fact which can be exploited in the processes disclosed in the ’322 patent. In particular, the patent discloses that the calcium-replaced sieves of both series were commercially available at the time of the filing of the application from which the ’322 patent matured, and two of the examples given in the ’322 patent employ such a zeolite having a 5 angstrom pore diameter as a starting material. In the first of these, 66.5 grams of the calcium-containing zeolite were “treated with an aqueous solution of 26.6 grams of PHfiSiOa dissolved in 1 gallon of water * * * [in order] to introduce catalytically active acidity to replace calciiun.” However, the “replacement” was actually only a reduction, from 9.95% calcium in the starting material to 9.08% in the final product. The ammonium ion was then converted to a hydrogen ion and ammonia gas, if we and the solicitor read the disclosure correctly. The dual-exchanged zeolite so obtained was then used in the second example to crack normal hexene.

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Bluebook (online)
461 F.2d 826, 59 C.C.P.A. 1272, 174 U.S.P.Q. (BNA) 155, 1972 CCPA LEXIS 305, Counsel Stack Legal Research, https://law.counselstack.com/opinion/in-re-mattox-ccpa-1972.