Meitzner v. Corte

537 F.2d 524, 190 U.S.P.Q. (BNA) 407
CourtCourt of Customs and Patent Appeals
DecidedJuly 15, 1976
DocketPatent Appeal No. 76-554
StatusPublished
Cited by4 cases

This text of 537 F.2d 524 (Meitzner v. Corte) 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
Meitzner v. Corte, 537 F.2d 524, 190 U.S.P.Q. (BNA) 407 (ccpa 1976).

Opinion

BALDWIN, Judge.

This appeal is from a decision of the Patent and Trademark Office Board of Patent Interferences1 (board) awarding priority to the senior party Corte et al.2 over the junior party Meitzner et al.3 on all twelve counts in interference. We affirm in part and reverse in part.

The Counts

Counts 6 through 9 and 12 are directed generally to cation exchange resin compositions and counts 1 through 5,10, and 11 are directed to processes for preparing such resins. The resins comprise a water-insoluble matrix having bonded thereto cation exchange groups including, for instance, sulfonic acid or carboxylic acid groups. The matrix is prepared by copolymerizing a monoethylenically unsaturated monomer, such as styrene, and a polyethylenically unsaturated monomer, such as divinyl benzene. Polymerization is carried out in an organic liquid which is a solvent for the monomers but a non-solvent for linear arpmatic vinyl polymers. The matrix is described in all counts as having a “spongy” structure which is permeated by small veins into which liquids may penetrate.

Counts 1 and 6 are typical of the process and product counts, respectively, and are reproduced below:

1. In a process for preparing a cation exchange resin having a water-insoluble matrix and cation exchange groups bonded thereto which are selected from the group consisting of sulfonic acid, carboxylic acid, phosphoric acid, and phosphonic acid groups, the improvement comprising employing as said matrix a solid copolymer of spongy structure which is permeated by small veins into which liquids are able to penetrate, which matrix is prepared by copolymerizing a mixture consisting essentially of (1) a monoethylenically unsaturated monomer selected from the group consisting of a monovinyl carbocyclic aromatic compound, a monoethylenically unsaturated carboxylic acid, a monoester of a lower aliphatic alcohol and a monoethylenically unsaturated polycarboxylic acid, a completely esterified monoethylenically unsaturated polycarboxylic acid, and an anhydride of a monoethylenically unsaturated polycarboxylic acid, with (2) a polyethylenically unsaturated monomer selected from the group consisting of a polyvinyl carbocyclic aromatic compound, an ester of a dihydric alcohol and an cc-p -ethylenically unsaturated carboxylic acid, diallyl maleate, divinyl ether, and divinyl ketone; the aforesaid copolymerization being conducted while the monomers are dissolved in 10 to 300% by weight, based on monomer weight, of an organic liquid which is a solvent for said monomers but is unable to dissolve linear aromatic vinyl polymers.

6. A cation exchange resin consisting of a water insoluble matrix and cation exchange groups bonded thereto which are selected from the group consisting of sulfonic acid, carboxylic acid, phosphoric acid, and phosphonic acid groups, wherein as said matrix there is employed a solid opaque copolymer of spongy structure [526]*526which is permeated by small veins into which liquids are able to penetrate, which matrix is prepared by copolymerizing a mixture consisting essentially of (1) a monoethylenically unsaturated monomer selected from the group consisting of a monovinyl carbocyclic aromatic compound, a monoethylenically unsaturated carboxylic acid, a monoester of a lower aliphatic alcohol and a monoethylenically unsaturated polycarboxylic acid, a completely esterified monoethylenically unsaturated polycarboxylic acid, and an an-hydride of a monoethylenically unsaturated polycarboxylic acid, with (2) a polyethylenically unsaturated monomer selected from the group consisting of a polyvinyl carbocyclic aromatic compound, an ester of a dihydric alcohol and an cc - p -ethylenically unsaturated carboxylic acid, diallyl maleate, divinyl ether, and divinyl ketone, the aforesaid copolymerization being conducted while the monomers are dissolved in 10 to 300% by weight, based on monomer weight, of an organic liquid which is a solvent for said monomers but is unable to dissolve linear carbocyclic aromatic vinyl polymers.

Findings of Fact by the Board

The board made certain undisputed findings of fact which are relevant to Meitzner et al.’s case for an actual reduction to practice and which are summarized below.

The cation exchange resins involved in this interference possess a spongy or macro-reticular structure as opposed to a gel-type structure. A macroreticular structure may be compared with a ball of tough, rigid sponge having large discrete pores. Macro-reticular resins offer advantages over gel-type resins, which are not spongy and which do not have any true porosity, since (1) high molecular weight ions may be more completely removed, and (2) the open structure of the macroreticular resins permits the use of tough copolymers which would be too dense to effectively act as ion exchange resins if they were used in a gel-type system.

During March of 1957, while working as an employee of the Rohm and Haas Company (hereinafter R & H), under the direction of Oline, Sigafoos prepared raw beads by copolymerizing styrene and divinyl benzene in 35% tertiary amyl alcohol using standard aqueous suspension polymerization techniques. These raw beads were milky white and floated on the surface of the suspension polymerization medium. They had an ethylene dichloride (EDC) swelling ratio of 1.5. The EDC swelling ratio is an indication of the increase in volume of an EDC filled raw bead following immersion of the raw bead in EDC. It is determined by dividing the volume of an EDC filled raw bead by the volume of a dry raw bead.

On March 18, 1957, Sigafoos sulfonated the raw beads. The sulfonation process proceeded rapidly as evidenced by the high volume capacity of the sulfonated raw beads obtained within 2lh hours. On March 25, 1957, Sigafoos determined that the sulfonated raw beads could be used to neutralize sodium hydroxide.

On April 4, 1957, the sulfonated raw beads produced by Sigafoos were submitted to the appropriate R & H laboratory for a “standard” evaluation. Oline requested the evaluation and Meitzner approved the request, which states, inter alia :

We are submitting for your evaluation a sample of IR-120 type resin prepared by extending a styrene-20% DVB [divinyl benzene] formulation with'35% t-amyl alcohol. Although the raw beads were sulfonated with tech [technical] H2S04 [sulfuric acid], their bead integrity is exceptionally good (even though the beads are on the small side). The solids content of the sulfonated resin in the H + form is 48.2% which indicates a porosity similar to that for IR-120. Stability tests may be interesting.

The IR-120 referred to in Oline’s request was a commercial ion exchange resin marketed during March and April of 1957 under the registered trademark Amberlite IR-120. It is a gel-type ion exchange resin having a matrix comprising a copolymer of styrene and divinyl benzene.

[527]*527Dr. Robert Kunin, employed by R & H as head of the Ion Exchange Evaluation Laboratory, testified, as summarized by the board, that he was aware of the work being done by Sigafoos during February through April of 1957, and that he was also aware of the following:

(a) The milky white character of the raw beads obtained by Sigafoos suggested that the beads had a spongy structure which was permeated by small veins * * *

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537 F.2d 524, 190 U.S.P.Q. (BNA) 407, Counsel Stack Legal Research, https://law.counselstack.com/opinion/meitzner-v-corte-ccpa-1976.