In re Priest

582 F.2d 33, 199 U.S.P.Q. (BNA) 11, 1978 CCPA LEXIS 255
CourtCourt of Customs and Patent Appeals
DecidedAugust 17, 1978
DocketAppeal No. 78-511
StatusPublished
Cited by3 cases

This text of 582 F.2d 33 (In re Priest) 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 Priest, 582 F.2d 33, 199 U.S.P.Q. (BNA) 11, 1978 CCPA LEXIS 255 (ccpa 1978).

Opinion

BALDWIN, Judge.

This appeal is from the decision of the Patent and Trademark Office (PTO) Board of Appeals (board) conditionally “reversing” the rejection of claims 11-16, 21 and 22 in appellant’s application serial No. 417,487, filed November 20, 1973, for “Polymer/Polyols and Process for Production Thereof.” The action taken by the board is modified.

Invention

The inventions in the claims before us are “fluid polymer/polyol” compositions which [34]*34are convertible to polyurethane foams “having reduced scorch” or discoloration. The compositions are “free radical catalyst-catalyzed reaction produces] formed by polymerizing” certain mixtures of acrylonitriles and styrene dissolved or dispersed in a denominated polyol.

Claim 11 is illustrative:

11. A fluid polymer/polyol composition which is convertible to a polyurethane foam having reduced scorch by reaction with water and an organic polyisocyanate and which is the free radical catalyst-catalyzed reaction product formed by polymerizing (1) from 10 to 30 weight percent of a mixture of (a) from 33 to 75 weight percent of acrylonitrile or methacrylonitrile and (b) from 25 to 67 weight percent styrene or alpha-methyl styrene, said weight percents of the nitrile and the styrene or alpha-methyl styrene being based on the total weight of those materials dissolved or dispersed in (2) from 70 to 90 weight percent of a normally liquid polyol having a hydroxyl number from 20 to 150, said weight percent of the mixture and polyol being based on the total weight of the monomers and the polyol and said polymer consisting essentially of polymer particles having diameters less than one micron suspended in the polyol.

Background

The application as filed presented eighteen claims. Claims 1-10 were drawn to a process for the preparation of polymer/polyol compositions, claims 11-16 were drawn to the compositions per se, and claims 17 and 18 recited a method of producing a polyurethane foam by reacting and foaming the polymer/polyol compositions of claim 11 with an organic polyisocyanate.

In the first Office Action, claims 17 and 18 were withdrawn from consideration by the examiner pursuant to a telephone restriction requirement. Claims 1-17 [sic 16?] were rejected under 35 U.S.C. § 112, paragraph 1, for failing to recite a temperature of operation which was said by the examiner to be, in accordance with the specification, a “critical limitation.” The examiner further stated that because “of the absence of this important limitation, product-by-process claims 11-16 are also improper.” The claims were similarly rejected for failure to recite the type of “polyol” required, the reaction apparatus, and the maintenance of a low monomer to polyol ratio. The claims were also rejected on prior art.

Appellant’s first amendment presented additional process claims (19 and 20) and composition claims (21 and 22). In response to the rejection under 35 U.S.C. § 112, the appellant indicated that:

The Examiner correctly states that the temperature at which the instant process is performed is a critical limitation. However, this limitation is already effectively present in the instant process claims in view of the recitation therein that the process is conducted “while maintaining a low monomer to polyol ratio throughout the reaction mixture during the polymerization.”

However, appellant questioned the examiner’s characterization of the composition claims and the necessity of inserting a temperature limitation.

With particular reference to claims 11 to 16, those claims are not strictly “product by process” claims. Rather, those claims define the compositions as reaction products having compositional features, particularly the recited particle size. As so defined, the claimed compositions are clearly distinguished from the only art (Scharf) applied against the instant claims.
Accordingly, it would be redundant to insert a specific temperature limitation in the instant independent process claims and unnecessary to insert such a limitation in the instant independent composition claims.

Similar responses were made to the remaining rejections under 35 U.S.C. § 112. The prior art was discussed.

In the second and final rejection, the examiner adhered to each of the rejections found in the first Office Action and expanded upon the § 112 rejection stating:

[35]*35B. Neither of the limitations as to temperature and apparatus is considered to be unnecessary or reduntant [sic] by the Examiner. These important limitations are the means used to achieve the desired and result, i. e. low monomer to polyol ratio. In this sense, these parameters should be included in the claims.
C. The instant composition claims are truly product by process claims. A material recited as the reaction product of certain ingredients is described in terms of a process. The presence of physical characteristics in the claim cannot change the nature of the claim as being a product by process.
D. The instant specification gives no indication as to the presence of any unsaturation in the polyols. The references cited by applicant do not persuade the Examiner in that purification procedures may be used to remove impurities. Most importantly, it appears that unsaturation is necessary in order to obtain grafting. The instant specification gives no indication of the degree of unsaturation which may be present or whether or not unsaturation is present at all. In this respect, the instant specification is clearly defective and insufficient.

Appellant submitted a further amendment which provided for the inclusion of a “back-mixed reactor” and a functional temperature in process claim 1. The § 112 rejections were reargued. An affidavit under 37 CFR 1.131 to antedate the prior art was offered and later submitted.

The examiner issued two Advisory Actions indicating, respectively, that appellant’s arguments did not overcome the final rejection although the amendment would be entered upon the filing of an appeal and, the affidavit under 37 CFR 1.131 had been entered.

Appellant’s Brief was filed and treated each of the points found in the Final Rejection.

In the Examiner’s Answer, all prior grounds of rejection were withdrawn and process claims 1-10, 19 and 20 allowed. A new rejection was made:

Claims 11-16, 21, and 22 are rejected under 35 U.S.C. § 112, second paragraph as failing to particularly point out and distinctly claim the subject matter which applicant considers to be his invention and also under 35 U.S.C. § 112

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Bluebook (online)
582 F.2d 33, 199 U.S.P.Q. (BNA) 11, 1978 CCPA LEXIS 255, Counsel Stack Legal Research, https://law.counselstack.com/opinion/in-re-priest-ccpa-1978.