In Re Draeger

150 F.2d 572, 32 C.C.P.A. 1217, 66 U.S.P.Q. (BNA) 247, 1945 CCPA LEXIS 470
CourtCourt of Customs and Patent Appeals
DecidedJune 25, 1945
DocketPatent Appeals 5041
StatusPublished
Cited by19 cases

This text of 150 F.2d 572 (In Re Draeger) 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 Draeger, 150 F.2d 572, 32 C.C.P.A. 1217, 66 U.S.P.Q. (BNA) 247, 1945 CCPA LEXIS 470 (ccpa 1945).

Opinion

BLAND, Associate Judge.

From a decision by the Board of Appeals of the United States Patent Office affirming the action of the Primary Examiner in finally rejecting claims 22 to 31, inclusive, of appellants’ application for a patent, on the ground that the claims are not supported by appellants’ application, appeal has been taken here.

Appellants’ application relates to a method for continuously reacting saturated tertiary hydrocarbons and olefins. Claims 22 to 26, inclusive, were copied from the patent to Altshuler et al., No. 2,238,802, issued April IS, 1941. Claims 27 to 31, inclusive, correspond to claims 22 to 26, respectively, except for slight differences which are clearly immaterial and which were so regarded by the tribunals below and not claimed otherwise by the appellants. The Allowance of the instant claims is sought for the purpose of provoking an interference with the said Altshuler et al. patent.

Claim 22 is regarded as illustrative of the appealed subject matter and reads: “22. In a process of alkylation in which olefinic and isoparaffinic hydrocarbons are reacted in the presence of a condensation catalyst while flowing in a circuit comprising a reaction zone into which reaction zone the iso-paraffinic and olefinic hydrocarbons are introduced in a feed in which the molar quantity of the iso-paraffinic hydrocarbon is greater than the molar quantity of the olefinic hydrocarbon, the improvement which comprises increasing the molar ratio of the iso-paraffinic hydrocarbon to the olefinic hydrocarbon in the reaction zone in excess of one hundred to one by increasing the rate of flow of the materials in the circuit such that they traverse said circuit in less than 70 seconds.”

It will be observed from the claim and from portions of the examiner’s statement quoted infra that the instant subject matter is highly technical, involving the chem *573 istry of the elaborate process as well as the structure of the alkylation machinery ■with which the process is carried out.

The examiner has, we think, properly described the Altshuler et al. patent in the following manner:

“Both the present application and the patent to Altshuler et al relate to the alkylation of isoparaffins such as isobutane by means of olefins such as butene in the presence of an alkylation catalyst such as concentrated sulfuric acid.

“According to Altshuler et al, their process is conducted in such a way that they obtain in their reaction zone an isoparaffin to olefin ratio, in effect, in excess of 100 to 1 by the expedient of controlling the rate of circulation of the mixture of hydrocarbons and acid catalyst within their reaction zone. When the feed contains an increased amount of isoparaffinic hydrocarbon, they may reduce the circulation rate and when the amount of isoparaffinic hydrocarbon is reduced, the rate of circulation may be increased. They have found that they obtained certain desirable results by maintaining the rate of flow in the closed circuit within the reaction zone so that the reactants will traverse the circuit once in 45 seconds or in less than 70 seconds.

* * * * * *

"As the examiner understands the Altshuler et al patent, by means of the foregoing apparatus and mode of operation the patentees are enabled to get an effect of very high ratios of isoparaffin to olefin within the reaction zone. This is due to the fact that the feed to the reaction zone contains an excess of isoparaffin over olefin and since the reaction between isoparaffin and olefin is on a mol for mol basis, there is a large amount of accumulated unreacted isoparaffin passing the point of introduction of olefin feed at any one moment and- the amount of isoparaffin passing such point is dependent upon the rate of circulation which in the patented claims is given in the time in seconds it takes to complete the circuit in the reaction zone.”

Then, referring to appellants’ disclosure, he, by commenting upon the drawings and the specification, points out the following:

“* * * Applicants practice one other control and that is the regulation of the length and/or the velocity of the stream so as to provide a contact time under reaction conditions of from about 30 minutes to 2 hours.”

He then calls attention to the fact that some of the appealed claims call for a rate of flow of the materials in the circuit, as for instance in claim 1, in less than 70 seconds, while in other claims the limit is 45 seconds.

In holding that the appealed claims were not supported by appellants’ disclosure and in denying the requested interference, the examiner in part said (omitting immaterial numerals, dates, etc.) :

“As has been pointed out in the foregoing, applicants disclose * * * ratios of recycle stock to fresh feed in excess of about 15:1 and preferably between 35:1 and 65 to 1, * * * overall ratio of acid to hydrocarbons in the circulating system of between 1:3 and 3:1, and * * * the regulation of the length and/or the velocity of the stream so as to provide a contact time under reaction conditions of from about thirty minutes to one hundred and twenty minutes.

“A careful study of the original disclosure does not show any instruction by applicants of any manner in which the three different variables are to be correlated with each other. There is no instruction that the lower limit of any one variable or the lower limit of the preferred range of any one variable be used with the lower limits of the other variable or with the lower limit of the second and the upper limit of the third variable or that the lower limit of one be used with some intermediate value of the other variables. The charts or curves presented with the amendment * * * appear to show * * * a. very minor portion of the possible correlations may satisfy the terms of the claims (with no support shown for the particular correlations). One chart shows that substantially only for a correlation of 30 minutes contact time, 1:3 acid to hydrocarbons ratio, and ratios between 35 and 65 of recycle stock to fresh feed will the terms of the claims be met. The second chart shows that only the specific correlation (not disclosed originally) of 30 to 60 minutes contact time, 1 to 3 acid to hydrocarbon ratio, and 65:1 recycle ratio will substantially meet the claims.

“The calculations presented * * * are on the basis of a 30 minute contact time, 65 :1 recycle ratio, and acid to hydrocarbon ratio of 1:3. This gives a traverse time of 36.9 seconds. Why this particular correlation? The examiner feels justified, for example, to consider the contact *574 time 120 minutes. This gives a time of 147 seconds which is way above less than 70 seconds’ or ‘less than 45 seconds’.”

The question presented to the Patent Office tribunals and here is: the appellants having disclosed a rate of flow resulting in a traverse time of between 36.9 seconds and 147 seconds (assumed but not determined by us), are they entitled now to have claims limiting the traverse time to less than 70 seconds and less than 45 seconds, respectively ?

It is the contention of appellants that the said traverse time claimed, though not specifically mentioned by them in the application, is inherent in the process disclosed therein.

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Bluebook (online)
150 F.2d 572, 32 C.C.P.A. 1217, 66 U.S.P.Q. (BNA) 247, 1945 CCPA LEXIS 470, Counsel Stack Legal Research, https://law.counselstack.com/opinion/in-re-draeger-ccpa-1945.