In re Geerdes

491 F.2d 1260, 180 U.S.P.Q. (BNA) 789, 1974 CCPA LEXIS 198
CourtCourt of Customs and Patent Appeals
DecidedFebruary 21, 1974
DocketPatent Appeal No. 9118
StatusPublished
Cited by11 cases

This text of 491 F.2d 1260 (In re Geerdes) 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 Geerdes, 491 F.2d 1260, 180 U.S.P.Q. (BNA) 789, 1974 CCPA LEXIS 198 (ccpa 1974).

Opinion

MILLER, Judge.

This appeal is from the decision of the Patent Office Board of Appeals affirming the rejection of claims 2-4, 7, 8, 19, and 20 of application serial No. 689,787, filed December 12, 1967, for “Expanded Composite Materials.” We reverse.

INVENTION

The invention is a method of producing expanded or foamed polymer compositions in the absence of recognized blowing agents by milling, under high [1261]*1261impact and energy conditions, particles of a polymer together with submicro particles of an additive material which is essentially nonvolatile at a temperature at which said polymeric material is fluid. The mixture is confined in a mold cavity under pressure and heat sufficient to render the polymeric material fluid; and the pressure is then released, permitting the mixture to foam and solidify.

Appellant’s specification states:

The present invention relates to expanded or foamed polymer compositions. Expanded polymer compositions are well known; they are commonly formed by incorporating a blowing agent in a body of polymer material. The blowing agent may be a gas releasing solid material, or a solid or liquid material that converts to a gas under the conditions of treatment. For example, a blowing agent may be mixed and dispersed in a polymeric molding powder. When this mixture is treated under a confining pressure so as to convert the blowing agent to a gas and the polymer to a plastic or viscous fluid stage, and the pressure is then released, the pockets of compressed gas formed by conversion of the blowing agent expand, causing an expansion of the mixture as a whole. The foamed polymer then is caused to solidify in expanded state to provide the foamed structure.

The specification further states that the expanding or foaming steps may be accomplished in various environments, in particular, extrusion. In the case of extrusion the specification reads:

As the molten material exits from the die orifice, the pressure on the material is suddenly released, and it expands before the resin sets. Continuous operation of the extruder will produce a continuous rod, ribbon or filament of foamed polymer whose cross-section shape is controlled by the shape of the die orifice. As is well understood in the art, the temperature at various stages of the extruder and at the die orifice are [sic] controlled to affect the foam properties, and secondary expansion dies may be located adjacent the extrusion orifice to control the degree of expansion of the ex-trudate, its cross-sectional size, and its cross-sectional shape.

After describing the milling step performed under high impact and compression energy conditions, the specification continues:

In accordance with the present invention, it is found that particularly after the latter level of energy has been imparted to the system, the composite material can be caused to foam with a uniform and controlled expansion when treated in a manner conventionally used for generating foamed polymers by control of heat and pressure. This foam generation is obtained in the absence of any recognized blowing agent, although the foaming action of the inert filler can be supplemented by the addition to the composite of a conventional blowing agent. Despite the foam generation, the filler or additive material is still present in the composite material and performs the same function for which it would be normally used in the absence of the foaming aspect.

The following portion of appellant’s specification was particularly noted by the board in its opinion:

In practicing the present invention, the composite material was extruded using a die comprising an outlet or orifice which was extended beyond the normal heated head and with control of the temperature of the extended section.

All the claims are method claims. Claim 19 is the only independent claim (letters, paragraphing, and emphasis added):

19. A method of forming an expanded polymeric material comprising,
A milling together particles of a thermoplastic polymeric material and submicro particles of an additive material, both said materials [1262]*1262being essentially non-volatile at a temperature at which said polymeric material is fluid, said milling being effected by a rotary impact mill having impactors traveling at a velocity of at least about 600 linear feet per second, to form a composite of said two materials, said composite consisting essentially of said two materials,
B confining said composite in a mold cavity under pressure and heating said composite to said temperature to render said polymeric material fluid,
C releasing said pressure while said polymeric material is fluid and permitting said composite to expand as a foam, and
D solidifying the foamed polymeric material with said additive particles retained therein.

Dependent claims 2-4, 7, 8, and 20 present preferred process conditions and materials.

PRIOR ART

Many references were cited by the examiner, and appellant’s brief concedes their teachings as follows:

Appellant has, and does acknowledge that the high energy milling [step A] of plastic and submicro additive particles to form a composite of the two materials is prior art to Appellant, this process per se being an earlier development of Appellant’s assignee. Appellant has, and does acknowledge that the molding process [steps B, C, and D] is also per se prior art, it being the conventional process of forming a foamed plastic with a blowing agent (although the Examiner has not cited such prior art).

It is to be noted that the prior art references cited by the examiner with respect to the claimed molding steps involve solid extrusion processes, which differ from foam extrusion processes in that they are designed to solidify the ex-trudate by the time it leaves the orifice die.

REJECTIONS

The board’s reasons for affirming the examiner’s rejection of all the claims under 35 U.S.C. § 103 were that “the claims on appeal permit the .presence of a blowing agent,” and that “the prior art clearly suggests the combination of the here claimed milling procedure with the molding procedure.” It added that “The nature of the article obtained is not determinative of the patentability of the process.”

The board also affirmed the examiner’s rejection of the claims under the first and second paragraphs of 35 U.S.C. § 112, saying that “The specification appears to indicate that the success of appellant’s process depends upon the use of special equipment and/or processing temperatures.” It also stated that the specification “does not adequately set forth any manner, other than experimentation,” of selecting both the proportions of additive to polymer (“to obtain any desired degree of expansion”) and the size of the particles and the effect thereof on the properties of the product.

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Bluebook (online)
491 F.2d 1260, 180 U.S.P.Q. (BNA) 789, 1974 CCPA LEXIS 198, Counsel Stack Legal Research, https://law.counselstack.com/opinion/in-re-geerdes-ccpa-1974.