Talbert Fuel Systems Patents Co. v. Unocal Corporation, Union Oil Company of California, and Tosco Corporation

275 F.3d 1371, 61 U.S.P.Q. 2d (BNA) 1363, 2002 U.S. App. LEXIS 241, 2002 WL 21739
CourtCourt of Appeals for the Federal Circuit
DecidedJanuary 8, 2002
Docket99-1421
StatusPublished
Cited by16 cases

This text of 275 F.3d 1371 (Talbert Fuel Systems Patents Co. v. Unocal Corporation, Union Oil Company of California, and Tosco Corporation) 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.

Bluebook
Talbert Fuel Systems Patents Co. v. Unocal Corporation, Union Oil Company of California, and Tosco Corporation, 275 F.3d 1371, 61 U.S.P.Q. 2d (BNA) 1363, 2002 U.S. App. LEXIS 241, 2002 WL 21739 (Fed. Cir. 2002).

Opinion

PAULINE NEWMAN, Circuit Judge.

Talbert Fuel Systems Patents Co. is the owner of United States Patent No. 5,015,-356 (the '356 patent) entitled “Hydrocarbon Fuel Systems,” inventor William Tal-bert. Defendant Union Oil Company of California (herein “Unocal” collectively with Unocal Corporation) owns United States Patent No. 5,288,393 (the '393 patent) entitled “Gasoline Fuel.” Defendant Tosco is licensed under the '393 patent. Talbert appeals the district court’s grant of summary judgment of noninfringement. Talbert also appeals the dismissal of its requested interference proceeding with the '393 patent under 35 U.S.C. § 291. We affirm the district court’s dispositions. 1

DISCUSSION

Talbert’s '356 patent is directed to certain reformulated gasolines that reduce emissions while preserving key gasoline performance parameters. Gasolines are produced by refining crude petroleum, a process that includes distilling (fractionating) hydrocarbon mixtures that have been obtained by treating petroleum in various ways not here relevant. The characteristics of the resultant gasoline fractions are affected by their hydrocarbon composition. Conventional gasolines are complex mixtures of hydrocarbons having mostly four to twelve carbon atoms. Gasoline hydrocarbons are conventionally described in three groups or “cuts” based on the number of carbon atoms in the hydrocarbon molecules: C4 and C5 (low-end or front-end) hydrocarbons, C6 to C10 (middle-cut), and Cn and C12 (high-end). The “cut” relates to the separation of hydrocarbon streams in the fractionation process.

The low-end and high-end hydrocarbons are of concern as sources of pollution, for low-end hydrocarbons vaporize readily and can enter the atmosphere uncombusted, for example at the gas pump, and high-end hydrocarbons may be incompletely combusted in the engine, thus polluting the atmosphere through the exhaust. It was known that reduction of these components in gasoline is environmentally desirable. However, low-end hydrocarbons aid effective ignition, and high-end hydrocarbons provide fuel energy. Talbert’s '356 patent is directed to reformulated gasolines that are substantially free of both low-end and high-end hydrocarbons, but with a calculated amount of low-end hydrocarbons added or retained as a “priming agent” to facilitate ignition.

*1374 Claim Construction

Claim construction is a matter of law, see Markman v. Westview Instruments, Inc., 52 F.3d 967, 970-71, 34 USPQ2d 1321, 1322 (Fed.Cir.1995) (en banc), aff'd, 517 U.S. 370, 116 S.Ct. 1384, 134 L.Ed.2d 577 (1996), and receives plenary review on appeal. Cybor Corp. v. FAS Technologies, Inc., 138 F.3d 1448, 1456, 46 USPQ2d 1169, 1172 (Fed.Cir. 1998) (en banc).

Claim 1 of the '356 patent is representative, with emphases added to indicate the terms whose construction is material to the issues of infringement:

1. A low Reid Vapor Pressure 2 liquid gasoline for use in a standard carburet-ed internal combustion engine; said gasoline comprising a priming agent and a hydrocarbon mixture having an intermediate carbon range relative to C4 -C12 fuel; said intermediate carbon range consisting essentially of C6-C10 hydrocarbons with C9 and C10 paraf-finic hydrocarbons being present in the mixture; said gasoline having a boiling point range of 121-345F at 1 atmosphere pressure; and said priming agent consisting of a hydrocarbon selected from the group consisting of C4 and C5 hydrocarbons and mixtures thereof and said priming agent being present in a minimum effective amount for raising the front end volatility of the gasoline to a minimum level for cold engine starting with said minimum effective amount being less than that required for C4-C12 gasoline.

The district court focused on the boiling point range of 121F-345F. The '356 patent explains that 121F is the boiling point of the lowestdooiling C6 component, 2,2-dime-thylbutane (C6H14), and 345F is the boiling point of decane, C10H22, the highest-boiling C10 component. The district court construed claim 1 as limited to gasolines having a final boiling point of 345F, and excluding gasolines having a higher final boiling point.

Talbert argues that the district court erred in defining 345F as a final boiling point, pointing out that the word “final” does not appear in claim 1. Talbert argues that some higher boiling hydrocarbons can be present, such as Cn and C12 hydrocarbons, due to the generally recognized imprecision of the refining process, which does not produce gasolines of specific hydrocarbon composition with precise end points. Talbert explains that refinery distillation produces cuts of distillate which may include hydrocarbon components that when pure boil above or below the range of the refinery cut. The '393 patent explains that a refinery stream cut at 345F will contain “a small amount” of hydrocarbons boiling above 345F and having 11-12 carbons.

Talbert states that the claim term “consisting essentially of C6-C10” recognizes that gasoline in the 121-345F boiling range contains mostly C6 to C10 hydrocarbons, but that some hydrocarbons outside that range can be present. Talbert argues that since some hydrocarbons higher than C10 can be present, they necessarily would raise the final boiling point of the gasoline above 345F. Talbert argues that claim 1 is not limited to gasolines whose final boiling point is 345F because even traces of hydrocarbons above C10 will raise the final boiling point above 345F, without significantly altering the fuel’s performance for standard carbureted engines. Thus Tal-bert urges that when reading the claim as a whole including its preamble, taking cognizance of the imprecision of refinery methods, a claim construction is required *1375 that does not limit the boiling point of the gasoline to 345F.

The basic tools of claim construction are the words of the claim, understood in light of the specification and the prosecution history, in accordance with the usage and knowledge in the field of the invention. A term of technical art, unless defined otherwise, by the patentee, has the meaning by which it would be understood by persons experienced in the field of the invention. See, e.g., Multiform Dessicants v. Medzam, 133 F.3d 1473, 1477, 45 USPQ2d 1429, 1432 (Fed.Cir.1998).

The district court, rejecting Talbert’s proposed construction, ruled that claim 1 is limited to gasolines whose final boiling point is 345F.

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275 F.3d 1371, 61 U.S.P.Q. 2d (BNA) 1363, 2002 U.S. App. LEXIS 241, 2002 WL 21739, Counsel Stack Legal Research, https://law.counselstack.com/opinion/talbert-fuel-systems-patents-co-v-unocal-corporation-union-oil-company-cafc-2002.