Application of Lambert

212 F.2d 594, 41 C.C.P.A. 875
CourtCourt of Customs and Patent Appeals
DecidedMay 24, 1954
DocketPatent Appeal 6037
StatusPublished

This text of 212 F.2d 594 (Application of Lambert) 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 Lambert, 212 F.2d 594, 41 C.C.P.A. 875 (ccpa 1954).

Opinion

COLE, Judge.

The appellants herein seek a reversal of the decision of the Board of Appeals of the United States Patent Office which affirmed the action of the Primary Examiner in rejecting all but one claim of appellants’ patent application for certain allegedly inventive improvements relating to a method and tank furnace for the making of glass.

Appealed claims 1, 3, 18, 20, 21, 23, 24, 29, and 34 are drawn to a method of glass manufacture while claims 17, 28, 30, and 31 are directed to a tank furnace *595 apparatus. These claims were rejected as being unpatentable over the prior art of record as evidenced by the following:

Drake 1,759,228 May 20, 1930; Wadman 1,880,541 Oct. 4, 1932; Wadman 1,944,855 Jan. 23, 1934; McAlpine 2,254,079 Aug. 26, 1941; Batchell 2,294,373 Sept. 1, 1942.

The remaining claims 2, 4-15 inclusive, 32 and 33, were rejected as not being readable on the elected species.

Representative claims 1 and 17 read as follows:

“1. Method of making glass in a tank type of furnace which comprises causing the glass, whilst still full of bubbles, to flow in a unidirectional shallow stream from the surface of the batch melting compartment, to a fining compartment, increasing the temperature of the glass during its passage from the melting compartment to the fining compartment, and in the fining compartment heating the upper portion of the glass so transferred to fine the glass by causing an electric current to flow across the fining compartment in the said upper portion of the glass, which fined glass is then allowed to settle in the fining compartment and is then withdrawn from the lower portion of the fining compartment into a working compartment, whereby unfined glass is prevented from reaching the working compartment.
“17. Tank furnace for the manufacture of glass comprising a melting compartment, a fining compartment, a shallow channel constructed and arranged to lead from the surface of the glass in the melting compartment to the fining compartment, an electrode in the fining compartment contructed and arranged to be submerged and to heat the upper portion of the glass in the fining compartment, the channel being provided with a recess, deeper than the channel, in which at least another electrode is located to supply electric current to the glass flowing from the melting compartment to the fining compartment, the crown of the fining compartment being prolonged above the recess provided in the channel, a working compartment and a duct connecting the lower portion of the fining and working compartments.”

Preliminary to detailed discussion of the claims in controversy, it is essential to note that the basic concept of a three compartment tank furnace is set forth in the claims, said compartments being respectively designated as the melting, fining (refining), and working compartments. The solid glass making materials, sometimes referred to as the “glass batch,” are first introduced into the melting compartment wherein they are fused and reduced to a molten state. Subsequent to this phase of the operation, the melted glass flows along the furnace and passes into the fining compartment where it is “fined” by the application of additional heat at greater temperature so that impurities, such as bubbles, may be removed from the glass. Thereafter, the glass enters the working compartment for thorough cooling prior to aetual use. The aforegoing broad characterization of the operation of a continuous type glass furnace is fundamental in the art.

The principal objective of the claimed invention is to produce a more uniform glass product at less operational expense than heretofore accomplished by prior art processes or apparatus. In this respect, the essence of appellants’ alleged contribution to the art lies in the particular method of heating the glass materials as they flow through the furnace, and more specifically relates to the application of heat to the molten glass during its passage from the melting to the refining compartments.

In its opinion, the Board of Appeals concisely summarized the subject matter of appellant’s application as follows:

“The appealed claims are directed to a process of and a tank furnace structure for making glass wherein *596 melted glass, whilst still full of bubbles, is transferred in a unidirectional shallow stream from the surface of a melting compartment to a fining compartment. In the fining compartment, the upper portion of the glass so transferred is rapidly heated by an electric current which flows across the fining compartment through the upper portion of the glass to cause the release of bubbles through a relatively thin upper layer and thus fine the glass. The fined glass settles in the fining compartment due to its increased density and is withdrawn from the lower portion of the fining compartment into a working compartment.
“For purposes of fuel economy, appellants contemplate operating the melting compartment at a somewhat reduced temperature but have found that glass entering the fining compartment at too low a temperature will be of relatively high density notwithstanding the contained bubbles and will settle substantially immediately to the lower part of the fining compartment instead of remaining at the upper part where it might be more readily refined. To prevent such a downstream, the temperature of the glass is increased while it passes from the melting compartment to the fining compartment, this being accomplished by the passage of an electric current through the aforementioned shallow stream of glass that flows from the surface of the melting compartment to the fining compartment.”

The step of increasing the temperature of the molten glass during the interval between its transfer from the surface of the melting compartment to the fining compartment, is of critical significance to the patentability of the claims in issue, and it is this vital feature, in particular, which is reputedly anticipated by the principal reference of record, Wadman 1,944,855.

A two chamber tank furnace structure for the making of glass is shown in Figure 2 of Wadman 1,944,855, hereinafter referred to as Wadman ’855. That structure is reproduced herewith.

The principal chambers, designated by the numerals 10 and 11, are substantially separated from each other by a ■compartment 19. Rising from the floor ■of the tank to the glass level in chamber 10 is a baffle 21 which is positioned at the entrance to compartment 19. In chamber 11 is a bridge wall which extends almost to the bottom of the tank in that ■chamber. A passage 12 leads from compartment 19 into chamber 11 so that the flow of glass in the tank is from chamber 10, over the baffle, vertically into compartment 19, horizontally along the passage 12, beneath the bridge wall, and into chamber 11. The usual combustion heating means are found in chamber 10 of the furnace. Electrodes 18 are localized in compartment 19 for passing electric current through the glass in that compartment. No heating means are shown in chamber 11 although the pat-entee, in his specification, states that “the glass in the chamber 11 may be further refined or planed in any suitable or desired manner * *

*597

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Bluebook (online)
212 F.2d 594, 41 C.C.P.A. 875, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-lambert-ccpa-1954.