Beatie v. Pollock

71 F.2d 306, 21 C.C.P.A. 1150, 1934 CCPA LEXIS 87
CourtCourt of Customs and Patent Appeals
DecidedJune 12, 1934
DocketNo. 3320
StatusPublished

This text of 71 F.2d 306 (Beatie v. Pollock) 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
Beatie v. Pollock, 71 F.2d 306, 21 C.C.P.A. 1150, 1934 CCPA LEXIS 87 (ccpa 1934).

Opinion

Geaham, Presiding Judge,

delivered the opinion of the court:

An interference j)roceeding' was instituted in the United States Patent Office between the application of Cecil E. Beatie, No. 400531, filed July 31,1920, and the patent of the appellee, Bobert T. Pollock, 1783259, issued December 2, 1930, on an application filed November 14, 1929. The subject matter of the interference was expressed in two counts, which are as follows :

1. The process of converting heavy hydrocarbon oils into oils of lower boiling point which comprises subjecting oil to a cracking temperature and pressure in a pressure zone, separating the high boiling fraction of the evolved vapors from the lo& boiling fractious in the form of a condensate, then sub[1151]*1151jecting the condensate while still hot to increased cracking temperature and pressure, simultaneously distilling another independent body of oil, separating the evolved vapors according to their boiling points, and co-mingling the condensate thus formed with the oil in one of the pressure zones.
2. The process of converting heavy hydrocarbons into oils of low boiling point which comprises subjecting oil to a temperature and pressure sufficient to effect cracking thereof, separating the high boiling fractions of the evolved vapors from the low boiling fractions in the form of condensate, forcing the condensate so separated into a succeeding zone for further cracking at an increased temperature and pressure, and mixing with the condensate an 'additional charge of preliminarily treated oil substantially lighter than said oil initially subjected to temperature and pressure sufficient to effect cracking thereof and obtained from a source other than said evolved vapors.

The counts of the interference correspond to claims 1 and 4 of said Pollock patent. Pollock was previously in interference with an earlier issued patent to Gray No. 1724:760, issued August 13, 1929. Count 1 of this interference did not originate with Pollock, but was claim 1 of the Gray patent, was copied by Pollock and became claim 1 of the Pollock patent. Gray disclaimed said claim 1 on November 10,1931, through his assignee, the Texas Company, and an award of priority was made to Pollock of the subject matter of said Gray-Pollock interference. Claim 4 was originally paralleled by claim 6 of the Gray patent, but was afterward changed by amendment, in the prosecution of the Pollock application.

A motion was made by Pollock to dissolve the interference on the grounds that the application of the party Beatie fails to support the counts, and that said application is inoperative in disclosure to carry out the process defined by the counts. The Examiner of Interferences, after an exhaustive discussion of the matter, denied the motion. Pollock electing not to take testimony, priority was duly awarded to Beatie on both counts. On appeal, the Board of Appeals reversed the decision of the Examiner of Interferences, and priority was awarded to Pollock, from which decision the party Beatie has appealed.

The subject matter of the interference consists of a process of converting heavy hydrocarbon oils into oils of lower boiling point by heat and pressure, and is, generally speaking, carried out by subjecting such oils and their distillates to treatment in a succession of cracking units.

The Beatie disclosure, which was held by the Board of Appeals to not support the counts of the interference, is shown by the drawings and specification to include three units, each comprising a cracking coil, a separating chamber, and a dephlegmator. Crude oil is forced into a pipe still, where it is subjected to cracking heat and pressure. The highly heated products from the coil are led to a vapor-liquid separating chamber. Vapors are drawn from this sepa[1152]*1152rator into a dephlegmator, in which a reflux condensate is produced therefrom. The uncondensed low boiling point vapors from this dephlegmator are condensed in a final condenser and withdrawn. The liquid from this vapor-liquid separating chamber is withdrawn and fed into a second pipe still, where it is subjected to a lower temperature and pressure. The products from this still go to another vapor-liquid separating chamber, from which the vapors go to a second dephlegmator. The liquid portion of this distillate is withdrawn and is fed to a third coil still, where lower temperature and pressure is maintained. The reflux condensate from this second still is withdrawn and is conducted back to the first still, in which the highest temperature and pressure are maintained. In the third still the remaining oil, or result of the previous processes, is subjected to a lower cracking temperature, and the heated products go to a third liquid-vapor separator, the liquid content thereof being withdrawn and taken out of the system. The vapor from this separator goes into a third dephlegmator, where a reflux condensate is produced, which is pumped, together with liquids from the first still, into the second still of the system. The light or gasoline content from the third dephlegmator is condensed and withdrawn from the system.

It will thus be seen that Beatie shows a system by which he takes the crude oil, subjects it to a high temperature and pressure, and in succeeding processes subjects the residue of this oil to succeeding lower temperatures and pressures. The reflux condensate is treated by withdrawing it and feeding it backward through the system so that it is successively treated with higher temperatures and pressures.

There has been much discussion in this case as to the method of operation of the Pollock process and the process of the appellant Beatie. A reference to the Beatie application leaves no doubt in the mind as to the nature of his disclosure. This disclosure is, in brief, as stated by him:

Another object of the invention is to provide a process of cracking oil in stages in which the residuum oil from one stage advances to a succeeding stage for treatment at a lower temperature and heavier condensates of vapors formed in one stage advance to a preceding stage or in a direction counter-current to the advance of the residuum.

Again, he states :

Another object of the invention is to provide a process of cracking oil in stages by which the carbon which is formed in each of the stages is continuously and progressively carried forward through the stages to the point of discharge by a stream of fresh incoming oil advancing successively through the stages.

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Bluebook (online)
71 F.2d 306, 21 C.C.P.A. 1150, 1934 CCPA LEXIS 87, Counsel Stack Legal Research, https://law.counselstack.com/opinion/beatie-v-pollock-ccpa-1934.