Application of Karl Ziegler, Heinz Breil, Heinz Martin and Erhard Holzkamp

363 F.2d 888, 53 C.C.P.A. 1457, 150 U.S.P.Q. (BNA) 619, 1966 CCPA LEXIS 332
CourtCourt of Customs and Patent Appeals
DecidedAugust 4, 1966
DocketPatent Appeal 7485
StatusPublished
Cited by2 cases

This text of 363 F.2d 888 (Application of Karl Ziegler, Heinz Breil, Heinz Martin and Erhard Holzkamp) 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 Karl Ziegler, Heinz Breil, Heinz Martin and Erhard Holzkamp, 363 F.2d 888, 53 C.C.P.A. 1457, 150 U.S.P.Q. (BNA) 619, 1966 CCPA LEXIS 332 (ccpa 1966).

Opinion

MARTIN, Judge.

Appellants copied a claim in modified form from a patent of Weber et al. (Weber) for the purpose of provoking an interference on a catalyzed process for producing polyethylene. During the motion period of the resultant interference appellants’ motion to add counts corresponding to Weber’s other two claims, also modified by the omission of temperature and pressure limitations, was denied on the grounds that appellants had no right to make. The interference was eventually dissolved upon disclaimer by Weber. We are involved here in subsequent ex parte proceedings on claims 28 and 29 that correspond to the proposed counts which were not permitted in the interference. 1 Those two claims were rejected by the examiner on the ground of insufficient support in the present application, 35 U.S.C. § 112. Appellants have appealed the board’s decision affirming the rejection; we affirm.

Appellants disclose a process for controlling the degree of polymerization of a polyethylene formed by the reaction of gaseous ethylene in the presence of two-component Ziegler-type catalysts. Such catalysts are well known as a mixture of a metal organic compound and a compound of a heavy metal.

Appellants have discovered that the degree of polymerization, measured in terms of the average molecular weight of the resultant polyethylene, may be controlled by adjusting the molar ratio of the two catalyst components. So far as is pertinent here, appellants disclose that the organic metal compound catalyst component may be an organic aluminum compound of the general formula RA1XY, wherein R is H or a hydrocarbon radical, X is R or OR", Y is R, a halogen atom or OR', and R' is a hydrocarbon radical. It is preferred to use dialkyl aluminum monohalides. Titanium tetrachloride is the most frequently mentioned example of the heavy metal catalyst component. Starting from a molar ratio of organic aluminum compound to titanium tetrachloride (referred to by appellants as Al : Ti) as an initially large value of about 12, the influence of reductions in the ratio on the molecular weight of the polymers is initially slight. Only a slight increase is observed by a reduction to a 3 : 1 ratio, but a reduction to 2 : 1 increases the molecular weight more strongly to a value of about 320,000. Appellants disclose that:

* * * A zone then follows in which extraordinarily small changes in the *890 conditions referred to exerts quite an unusually strong influence on the molecular weight of the polymers obtained. If a ratio of 2 Al : 1 Ti is initially used and if the ratio is changed to 1 : 1 to 0.5 : 1, this causes a drop in the molecular weight from 320,000 to 20,000, so that it is possible to obtain any desired molecular weight between about 20,000 and 320,000 by a fine adjustment of the ratio between the organic aluminium compound and the titanium tetrachloride within this sensitive range.

Appellants also disclose that the commencement of the “sensitive range” or “zone” depends somewhat on polymerization conditions. The application continues :

* * * The essential feature of the present invention does not consist so much in determining the accurate numerical limits of these sensitive zones for each conceivable combination, as in the fundamental discovery that there is in fact such a sensitive zone. The position of this zone can extremely easily be determined by the expert interested in this matter, after he has acquired this knowledge, by a small series of experiments and plotting t[he] experiments by means of curves.

The molar ratio A1 : Ti is broadly stated to be within the range of from 8 : 1 to 0.2 : 1, although the “sensitive range” limits are noted to be different and narrower for each catalyst combination. For diethyl aluminum chloride and titanium tetrachloride the “sensitive range” is from 3 :1 to 0.67 : 1 and for diisobutyl aluminum chloride the range is from 8 : 1 to 0.5 : 1.

Appealed claim 28 reads:

28. A process for the polymerization of gaseous ethylene in the presence of a polymerization catalyst which comprises polymerizing the gaseous ethylene in the presence of a catalytic amount of a mixed catalyst of ethyl aluminum sesquichloride and titanium tetrachloride having a ratio of about 0.5-0.8 mol of titanium tetrachloride per mol of ethyl aluminum sesqui-chloride.

Claim 29 differs therefrom only in specifying a mole ratio range of “about 0.3-2.5” Ti to Al. 2

The appealed claims are specific to TiCL and ethyl aluminum sesquichloride. The sesquichloride is a mixture of diethyl aluminum chloride with ethyl aluminum dichloride. Appellants do not contend that either the sesquichloride or the molar ratios therefor find specific support in the present application taken alone. Rather, appellants base their contention for support of the limitations on another application, serial No. 482,412 (hereinafter “412”) filed January 17, 1955, which is referred to in the appealed application. Applicants contend that the “412” application is referred to in the appealed application in such a manner as to be incorporated by reference therein. That manner of reference comprises part of the following background discussion of three applications, including the “412” application, relating to processes for the production of polyethylene:

This invention relates to a process for the production of polyethylenes with predetermined degrees of polymerization.
Specifications application Serial No. 569,059, filed Nov. 15, 1954, application Ser. No. 482, 412, filed Jan. 17, 1955, and application Ser. No. 482,413, filed Jan. 17, 1955, relate to processes for the production of valuable plastic-like polyethylenes of high molecular weight by polymerization of ethylene under comparatively very gentle conditions of temperature and pressure in the presence of catalysts which are obtained from organic metal compounds together with compounds of the heavy *891 metals of the sub-groups of the 4th-6th groups of the Periodic System. * *
*****
According to Specification application Ser. No. 482,412, filed Jan. 17, 1955, the organic metal compounds used are aluminium compounds of the general formula R2A1X, in which R is a hydrogen atom or a hydrocarbon radical and X is inter alia a hydrogen or halogen atom, a hydroxyalkyl group or a hydroxyaryl group. Dialkyl alu-minium monohalides or diaryl alumi-nium monohalides are preferably used as the organic aluminium compounds. When these compounds are used, compounds of the 8th sub-group of the Periodic System or compounds of manganese can be used as the heavy metal compounds instead of or in addition to the compounds of the metals of the 4th-6th sub-group of the Periodic System, including thorium and uranium.

Following that discussion, the appealed application states that “it has now been found that in the processes set forth * * * ” (emphasis added) a “sensitive range” of catalyst component mole ratios has been discovered. “Processes set forth” is a clear reference to the processes in the three applications.

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363 F.2d 888, 53 C.C.P.A. 1457, 150 U.S.P.Q. (BNA) 619, 1966 CCPA LEXIS 332, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-karl-ziegler-heinz-breil-heinz-martin-and-erhard-holzkamp-ccpa-1966.