McGill Incorporated v. John Zink Company, McGill Incorporated, Cross-Appellant v. John Zink Company, Cross-Appellee

736 F.2d 666, 221 U.S.P.Q. (BNA) 944, 1984 U.S. App. LEXIS 15008
CourtCourt of Appeals for the Federal Circuit
DecidedApril 27, 1984
DocketAppeal 83-1198, 83-1217
StatusPublished
Cited by139 cases

This text of 736 F.2d 666 (McGill Incorporated v. John Zink Company, McGill Incorporated, Cross-Appellant v. John Zink Company, Cross-Appellee) is published on Counsel Stack Legal Research, covering Court of Appeals for the Federal Circuit primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

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McGill Incorporated v. John Zink Company, McGill Incorporated, Cross-Appellant v. John Zink Company, Cross-Appellee, 736 F.2d 666, 221 U.S.P.Q. (BNA) 944, 1984 U.S. App. LEXIS 15008 (Fed. Cir. 1984).

Opinion

KASHIWA, Circuit Judge.

This is a consolidated appeal from a judgment of the United States District Court for the Northern District of Oklahoma (No. 80-C-17-E), entered December 7, 1982, and from a post-trial order entered June 22, 1983. The judgment was in favor of appellee, owner of U.S. Patent No. 4,066,423 (the “423 patent”), and the district court awarded damages of $8,000,000. We affirm in part and reverse in part.

The Invention

The patented invention relates to a process for recovering hydrocarbon vapors from an air-hydrocarbon mixture. It is a pollution-prevention process for recovering hydrocarbon vapors that have been vented from a storage tank. Appellee’s invention is best described by its claim at issue:

2. A process for recovering hydrocarbon from an air-hydrocarbon mixture, comprising:
passing the air-hydrocarbon mixture through a solid adsorbent bed at slightly above atmospheric pressure, which bed is capable of selectively adsorbing the hydrocarbon components from the mixture to leave substantially hydrocarbon free air;
venting the substantially hydrocarbon free air to the atmosphere;
subjecting the Hydrocarbon laden solid adsorbent bed to a near vacuum with a liquid ring vacuum pump to desorb the hydrocarbon components therefrom and produce a rich air-hydrocarbon vapor mixture containing a liquid from the liquid ring vacuum pump and a recovered liquid hydrocarbon;
• separating the liquid from the liquid ring vacuum pump and the recovered liquid hydrocarbon from the rich air-hydrocarbon vapor mixture;
absorbing substantially all of the hydrocarbon components from the rich air-hydrocarbon vapor mixture with recovered liquid hydrocarbon absorbent in an absorber operating with a sufficiently high L/V ratio to produce a constant composition absorber overhead gas and a recovered liquid hydrocarbon mixed with said absorbent;
recycling the absorber overhead gas from the absorption step to a second solid adsorbent bed, capable of selectively absorbing the hydrocarbon therein to leave a substantially free hydrocarbon recycle air;
venting the substantially free hydrocarbon recycle air to the atmosphere;
separating the liquid ring vacuum pump liquid from the recovered liquid hydrocarbon produced in the separation step;
cooling the liquid ring vacuum pump liquid; and
recycling said liquid ring vacuum pump liquid for use in the liquid ring vacuum pump.

[Emphasis added.]

*669

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736 F.2d 666, 221 U.S.P.Q. (BNA) 944, 1984 U.S. App. LEXIS 15008, Counsel Stack Legal Research, https://law.counselstack.com/opinion/mcgill-incorporated-v-john-zink-company-mcgill-incorporated-cafc-1984.