Boston Metals Co. v. Air Products Inc.

193 F.2d 535, 92 U.S.P.Q. (BNA) 80, 1952 U.S. App. LEXIS 4344
CourtCourt of Appeals for the Fourth Circuit
DecidedJanuary 4, 1952
Docket6347_1
StatusPublished
Cited by3 cases

This text of 193 F.2d 535 (Boston Metals Co. v. Air Products Inc.) is published on Counsel Stack Legal Research, covering Court of Appeals for the Fourth Circuit primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Boston Metals Co. v. Air Products Inc., 193 F.2d 535, 92 U.S.P.Q. (BNA) 80, 1952 U.S. App. LEXIS 4344 (4th Cir. 1952).

Opinion

DOBIE, Circuit Judge.

Air Products, Incorporated, instituted a civil action, in the United States District Court for the District of Maryland, against Boston Metals Company (hereinafter called Boston), alleging infringement by'Boston of the Anderson patent No. 2,480,093 relating to the manufacture of oxygen and entitled “method of and apparatus for pumping liquid oxygen.” 98 F.Supp. page 720. The opinion of the District Court is reported in 98 F.Supp. 719, 729 and thus concludes: “Summarizing our conclusions, they are as follows: (1) method claims 11, 13 and 19 of the Anderson patent No. 2,480,093 are valid; (2) the method of pumping liquid oxygen employed by the defendant infringes these claims; and (3) the plaintiff has seasonably and adequately purged itself of any violation, and has removed the effects of any violation of the *536 patent or anti-trust laws which it may have committed.” Boston has duly appealed.

We append the first six paragraphs of the specifications of the Anderson patent, and claims 11, 13 and 19:

“This invention relates to a method of pumping liquefied gases and to an apparatus adapted to that use.

“An object of the invention is to provide a method and means for withdrawing a liquefied gas from a vessel in which it is stored or is being collected, in such manner as to avoid the possibility of gas locking the pump.

“An object of the invention is to provide a method and means for withdrawing a stream of liquefied gas of any desired constant quantity from a collecting pool in a gas fractionating column.

“An object of the invention is to provide a method and means for withdrawing a stream of gas from a fractionating tower and of reducing the gas to liquid form for delivery under pressure by means adapted to the pumping of liquids.

“An object of the invention is to provide a method and -means for pumping liquefied oxygen directly from a pool of -commercially pure oxygen in a fractionating tower to cylinders or pipe lines in which -gaseous oxygen is transported under high pressure, thereby avoiding the requirement for an oxygen storage tank and a gaseous oxygen compressing system. :

“An object of the invention is to provide a method and means for withdrawing oxygen in’ gaseous form from the pure oxygen vapor space in a fractionating tower, for liquefying the gaseous stream and for delivering the oxygen into pressure cylinders or pipe lines, thereby retaining in the tower any 'lubricating oil or other combustible substances which may enter the tower with the air 'stream.”

“11. In a method of producing oxygen and conditioning it for delivery to receiving means, in which air after compression andcooling is rectified at a relatively low temperature and reduced pressure thereby producing a cold nitrogen product and a liquid oxygen product having a temperature corresponding to its boiling point at said reduced pressure; the set of steps comprising subjecting fluid from said oxygen product to heat exchange with a colder fluid derived from said rectification and thereby forming a sub-cooled liquid oxygen product; pumping such sub-cooled liquid oxygen product to a desired higher pressure, said sub-cooling reducing the liquid oxygen temperature at least sufficiently to prevent the same from flashing into vapor during such pumping;, and converting the liquid oxygen at said higher pressure into a gas by heat exchange with the compressed air to be liquefied.”

“13. In a method of producing oxygen and conditioning it for delivery to receiving means, in which air after compression and cooling is rectified at a relatively low temperature and reduced pressure thereby producing a cold nitrogen product and a liquid oxygen product having a temperature corresponding to its boiling point at said reduced pressure; the set of steps comprising subjecting fluid from said oxygen product to-heat interchange with a stream of gaseous nitrogen obtained as one of the final products of said rectification and thereby forming a sub-cooled liquid oxygen product; pumping such sub-cooled liquid oxygen product to a desired higher pressure, said sub-cooling reducing the liquid oxygen ’temperature at least sufficiently to prevent the same from flashing into vapor during said pumping; and converting the liquid oxygen at said higher pressure into a gas. by heat exchange with the compressed air to thereby cool the air.”

“19. The method of transferring liquefied product of a fractionating operation, in which operation a mixture of -component gases having boiling points substantially below atmospheric temperature is compressed and cooled, the compressed and cooled mixture expanded and the effluent of the expansion step subjected to the fractionating operation to produce a liquefied higher boiling point fraction and a gaseous lower ’boiling point fraction, comprising withdrawing a stream of the liquefied higher boiling point fraction from the fractionating operation, subcooling the stream of liquefied higher boiling point fraction by heat exchange with a relatively colder product from the fractionating operation to reduce the temp *537 erature of the higher boiling point fraction to a point below the boiling point of the higher boiling point fraction at the minimum momentary pressure reached in an ensuing pumping step', pumping the sub-cooled higher boiling point fraction in liquid phase to a relatively high pressure and heat exchanging the higher boiling point fraction from the pump with the mixture of gases going to the fractionating operation to cool the mixture and vaporize the higher boiling point fraction.”

It seems quite clear that the accused device of Boston infringes the Anderson patent. We, therefore, discuss only the Anderson patent’s validity. Since we think the claims in suit of Anderson, Nos. 11, 13 and 19, are invalid for lack of invention, the judgment of the District Court must be reversed.

Of the patents in the prior art, we attribute particular importance to two German patents, Polard No. 495,795, and Messer & Grassman No. 712,480, and to Eichelman No. 1,976,388, Messer No. 2,133,105 and Hansen No. 2,292,375. These patents, in their relation to Anderson, we now discuss.

The Polard patent discloses the essential elements of Anderson, particularly the prevention of vapor-lock in the pumping by sub-cooling with nitrogen, and the pumping of oxygen gas directly into the cylinders, ready for use by the consumer. Polard mentions apparatus for pumping liquid oxygen from a pool in “a container;” Anderson mentions pumping liquid oxygen from a pool in the “column.” It is open to question whether Polard is limited to pumping from a particular type of container; also whether Anderson is strictly limited to pumping from the column. In any event, this difference, if it exists, is neither vital nor sufficient to constitute patentable invention.

There are many points of similarity between Eichelman and Anderson, even if (as appellee alleges) Eichelman was a paper patent and would be subject to vapor-lock in the pump; for the problem of vapor-lock had been solved by Polard, Hansen and Messer and Grassman. Unlike Anderson, Eichelman does not sub-cool his liquid oxygen in advance of the pump.

Hansen clearly shows sub-cooling to prevent vapor-lock of the pump.

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Bluebook (online)
193 F.2d 535, 92 U.S.P.Q. (BNA) 80, 1952 U.S. App. LEXIS 4344, Counsel Stack Legal Research, https://law.counselstack.com/opinion/boston-metals-co-v-air-products-inc-ca4-1952.