Application of Vincent J. Frilette and Paul B. Weisz

423 F.2d 1397, 57 C.C.P.A. 991
CourtCourt of Customs and Patent Appeals
DecidedApril 9, 1970
DocketPatent Appeal 8267
StatusPublished
Cited by3 cases

This text of 423 F.2d 1397 (Application of Vincent J. Frilette and Paul B. Weisz) 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
Application of Vincent J. Frilette and Paul B. Weisz, 423 F.2d 1397, 57 C.C.P.A. 991 (ccpa 1970).

Opinion

ALMOND, Judge.

This is an appeal from the decision of the Patent Office Board of Appeals affirming the examiner’s rejection of all of the claims of appellants’ application. 1

The invention relates to a catalytic conversion process and more particularly to a method for selectively conducting a chemical reaction by bringing an organic compound having a linear aliphatic structure into contact with a solid crystalline acid aluminosilicate having a structure of specific intracrystalline dimensions. By virtue of such dimensions, the catalyst allows the passage into or out of its crystalline cavities of only certain molecules, hence reference to them as “molecular sieves.” The catalyst is prepared by treating a precursor zeolite, such as chabazite or analeite, having an atomic ratio of silicon to aluminum of at least 1.8 and a pore size of about 5 Angstrom units (A.) with a fluid medium containing a source of hydrogen ions or ions capable of conversion thereto, for example ammonium ions, to produce the corresponding acid aluminosilicate. The catalyst may be used per se or admixed' with a “porous matrix.” The catalytic processing operations include reactant-selective systems as well as product-selective systems.

Claims 1, 5 and 14 are illustrative:

1. A method for selectively conducting a chemical reaction which comprises bringing an organic compound having a linear aliphatic structure into contact with a crystalline acid aluminosilicate having a pore size of about 5 Angstrom units and a silicon to aluminum ratio of at least 1.8.
5. A continuous method for selectively cracking normal aliphatic hydrocarbons from a mixture of the same with at least one other hydrocarbon selected from the group consisting of isoaliphatie hydrocarbons, naphthenic hydrocarbons, and aromatic hydrocarbons which comprises bringing said mixture at catalytic cracking conditions into contact with a crystalline acid aluminosilicate having a pore size of about 5 Angstrom units and a silicon to aluminum ratio of at least 1.8 wherein the normal aliphatic hydrocarbon component is admitted into the interior of said aluminosilicate to the exclusion of the other hydrocarbon components and removing the resulting products of cracking said normal aliphatic hydrocarbon component iron, said aluminosilicate.
14. A method for selectively hydro-cracking an organic compound having a linear aliphatic structure which comprises contacting said compound and hydrogen under hydrocracking conditions with a crystalline acid aluminosilicate having a pore size of from 4 to 6 Angstrom units and a silicon to aluminum ratio of at least 1.8.

Claims 2-4 are similar to claim 1 and call for a mixture of reactants. Claims 6-13 depend from claim 5 and further define the aluminosilicate. Claim 15 is similar to claim 14 and recites hydro-cracking a mixture of compounds. Claims 16-23 depend from claim 15 and further define the catalyst. Claims 3, 4, 12, 13, 22 and 23 are directed to embodiments wherein the aluminosilicate catalyst is used in combination with a porous matrix.

The prior art reference relied upon is:

Fleck and Wight (Fleck) 2,962,435 November 29, 1960

*1399 Fleck discloses the addition of a porous matrix, such as an inorganic oxide, to a crystalline aluminosilicate.

Appellants’ own patent, No. 3,140,322, noted supra, discloses aluminosilicate catalysts having an atomic ratio of silicon to aluminum of 1 to 5 and pore sizes including 5, 10 and 13 Angstrom units. The ammonium form of the aluminosilicate is disclosed along with various other forms based on ions such as silver, hydrogen, zinc and lithium. Natural zeolites, such as chabazite and analcite among others, are shown along with synthetic zeolites. Illustrative of the claimed subject matter is claim 2:

2. A process for selectively conducting an organic chemical reaction which comprises passing a reaction mixture consisting of components of different molecular shapes over a crystalline aluminosilicate zeolite molecular sieve material having uniform interstitial dimensions sufficiently large to admit at least one of said components but sufficiently small to exclude at least one remaining component and bearing within the interior thereof an added catalyst, active in promoting said reaction, introduced into the zeolite subsequent to formation thereof, effecting a catalytic conversion of the component material admitted to contact with said catalyst within the interior of said zeolite to convert the same to chemical species distinct from said admitted component and of a molecular shape capable of passing from the interior of said zeolite and simultaneously withdrawing, without substantial change in pressure of the system, said chemical species from the effluent stream passed over said zeolite.

Claim 3 of the patent depends from 2 and limits the reaction to catalytic cracking of a hydrocarbon mixture.

Dependent claim 4 requires that the aluminosilicate have catalytically active acidity in its interior. Claim 7 also depends from claim 2 and specifies a pore size of 5 A. Claim 16, dependent upon claim 2, limits the reaction mixture to one of hydrogenatable organic compounds and hydrogen.

The examiner rejected claims 1-23 as “within the scope of the patent claims * * * alone or in view of Fleck * * *,” presumably on the basis of double patenting. In making the rejection, the examiner felt that “recourse to the specification” was proper in interpreting the patent claims and that a terminal disclaimer would be ineffective to avoid the rejection. Claims 1 and 2 were also rejected as too broad on the ground that since no reaction conditions had been recited, it was probable “that no chemical reaction would occur at low temperatures and pressures.”

The board affirmed the double patenting rejection and compared the claims involved, making recourse, as did the examiner, to the patent specification. Although acknowledging that appellants filed a disclaimer limiting the term of any patent granted on the application to that of the parent patent, the board felt that

* * * since the differences between the claims on appeal and those of the patent are no more than minor differences in scope, the law in In re Siu, 42 CCPA 864; * * * 222 F.2d 267;
* * * 105 USPQ 428 is applicable herein and the terminal disclaimer is ineffective to overcome the rejection on double patenting.

The board also affirmed the undue breadth rejection of claims 1 and 2 and extended it to cover claims 3 and 4. Indicating that the statutory basis was 35 U.S.C. § 112, the board added that

* * * it is not apparent that all organic compounds having a linear aliphatic structure, regardless of molecular size, could enter pores of this size [5 Angstrom units] and contact the catalyst located therein.

The parties agree that this court’s most recent decisions in the area of double patenting make it clear that the *1400

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Bluebook (online)
423 F.2d 1397, 57 C.C.P.A. 991, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-vincent-j-frilette-and-paul-b-weisz-ccpa-1970.