W.R. Grace & Co.-Conn. v. Intercat, Inc.

7 F. Supp. 2d 425, 1997 U.S. Dist. LEXIS 22586, 1997 WL 889708
CourtDistrict Court, D. Delaware
DecidedSeptember 8, 1997
DocketCivil Action 93-522 LON
StatusPublished
Cited by5 cases

This text of 7 F. Supp. 2d 425 (W.R. Grace & Co.-Conn. v. Intercat, Inc.) is published on Counsel Stack Legal Research, covering District Court, D. Delaware primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
W.R. Grace & Co.-Conn. v. Intercat, Inc., 7 F. Supp. 2d 425, 1997 U.S. Dist. LEXIS 22586, 1997 WL 889708 (D. Del. 1997).

Opinion

OPINION

LONGOBARDI, Senior District Judge.

I. NATURE AND STAGE OF THE PROCEEDINGS

W.R. Grace & Co. — Conn. (“Grace”) is the owner of five patents relating to a composition, or the use of a composition, to reduce sulfur oxide (“SOx”) emissions from hydrocarbon conversion processes, such as fluid catalytic cracking (“FCC”) processes. The five patents-in-suit are U.S. Patents 4,469,589 (“’589 Patent”), 4,472,267 (“’267 Patent”), 4,495,305 (“’305 Patent”), 4,495,304 (“’304 Patent”), and 4,790,982 (“ ’982 Patent”).

By stipulation, this case was tried on the basis of sixteen representative claims: claims 7, 21, 33, and 34 of the ’589 Patent; claims 5, 23, 31 and 39 of the ’267 patent; claims 3,15, 30, and 35 of the ’305 Patent; claims 6, 20, and 40 of the ’304 Patent; and claim 32 of the ’982 Patent. The ’304 and ’305 Patents cover compositions of spinel-containing SOx-reducing additives that are combined with hydrocarbon conversion catalysts, such as crystalline aluminosilicates (e.g., zeolites). The ’589 and ’267 Patents address the catalytic process through which the introduction of particular additives is used to reduce the level of SOx that is emitted from FCC units. The ’305 and ’267 Patents differ from the ’304 and ’589 Patents in that the ’305 and ’267 Patents require the SOx-redueing additive to contain a rare earth metal (e.g., cerium) in order to promote the oxidation of sulfur dioxide to sulfur trioxide as part of the SOx removal function of the additive.

The asserted claims of the ’304, .’305, ’267, and ’589 Patents arise from two related patent applications filed simultaneously on July 29,1980. The ’982 Patent came later. Claim 32, the only claim from the ’982 Patent that is at issue in this ease, requires that the composition contain not only spinel and a rare earth metal such as cerium, but also a fourth metal component to promote (or catalyze) the sulfate reduction step of the additive’s operational cycle.-

Grace alleges that Intercat, Inc. (“Inter-cat”) has contributed to and induced the direct infringement by Conoco, Inc. (“Conoco”) of the patents-in-suit. Intercat sold Conoco additives called NO-SOX and NO-SOX-PC. Conoco then introduced those additives to its FCC units, where the NO-SOX products allegedly combined with the cracking catalyst to form the claimed compositions and to perform the claimed SOx-removal process. In its defense, Intercat contends that its NO-SOx products do not infringe any of the patents-in-suit and that the patents are invalid for obviousness, for failing to distinctly claim the subject matter of the invention, and for inequitable conduct before the Patent and Trademark Office (“PTO”).

At the close of Grace’s ease, Intercat and Conoco moved under Fed.R.Civ.P. 52(c) for judgment as a matter of law (“JMOL”) on the question of infringement. At the close of Defendants’ case, Grace moved under Fed. R.Civ.P. 52(c) for JMOL on each of the inequitable conduct defenses. In addition to addressing these two JMOL motions, this Court will resolve all questions relating to infringement and invalidity. This Opinion represents this Court’s findings of fact and conclusions of law.

This Court has jurisdiction over the subject matter of this action under 28 U.S.C. § 1331 and § 1338. Venue is proper under 28 U.S.C. § 1391 and § 1400.

II. BACKGROUND FACTS

A. FCC UNITS

Fluid catalytic cracking is a refinery process that converts heavy molecular weight compounds in crude oil into lighter weight compounds such as gasoline, diesel fuel, and-jet fuel. (Tr. 55). In the FCC process, the catalyst circulates through the regenerator where it comes into contact with the gas-oil feed, which is the feedstock to an FCC Unit. (UF-8; Tr. 743). This gas oil commonly *431 contains sulfur, usually between .5% and 3% by weight and in all events between .1% and 5% by weight. (Tr. 748). The gas oil comes into contact and mixes with the FCC cracking catalyst that is circulating within the FCC unit. (UF-9). That contact occurs at a high temperature, in the range of 1,250 to 1,350 degrees Fahrenheit. (Tr. 743).

In the United States, the active component of the cracking catalyst is crystalline alumi-nosilicate, also known as zeolite. (Tr. 744). The cracking catalyst looks like talcum powder and has a particle size of 20 to 120 microns in diameter. (Tr. 82). Although the catalyst is a solid, FCC units are referred to as “fluidized” because the catalysts behave like liquids when gases are passed through them. The FCC unit constantly recirculates the catalyst between the regenerator and the riser reactor sections of the FCC unit.

Unwanted byproducts of this FCC process include sulfur oxides, which are considered so harmful to the environment that they are restricted by our nation’s environmental laws. (Tr. 56). There are three primary methods used to reduce the SOx emissions coming from an FCC unit. In the first, called “hydroprocessing” or “hydrotreating,” the sulfur is removed from the gas-oil feed itself. Although efficient, this method of removal is extremely expensive, requiring a capital investment of $50 million or more. A second method of SOx removal is “flue gas scrubbing” in which SOx is removed from the flue gas before it enters the atmosphere. Flue gas scrubbing also requires significant capital investment. The third method is the use of a sulfur reduction additive. (Tr. 56-57).

In this third method, the SOx-reducing additive admixes with the cracking catalyst in the regenerator section of the FCC unit, is fluidized, and circulates through the FCC unit along with the catalyst. The entire process is completed in three steps. First, the SOx-reducing additive oxidizes the sulfur dioxide to sulfur trioxide. Once the sulfur trioxide is formed, the additive then captures it as a metal sulfate within the regenerator. The metal sulfate formed on the additive is stable under the conditions of the regenerator and circulates along with the cracking catalyst to the riser reactor. In the final step, the metal sulfate is reduced within the riser reactor, and the sulfur is released' from the FCC unit in the form of hydrogen sulfide. (Tr. 83-85) Then the process begins anew.

Although the use of a SOx-reducing additive is not, in the long run, a cheap alternative to hydroprocessing or flue gas scrubbing, the use of an additive does not require any significant capital investment. Moreover, it offers a refiner a certain flexibility in that the refiner can adjust the amount of additive based on the sulfur content of the gas-oil feedstock. (Tr. 58-59).

B. DEVELOPMENT OF THE SOx-RE-DUCING ADDITIVE INDUSTRY

In the late-1970’s, Atlantic Richfield Company (“ARCO”) was operating an FCC unit near Los Angeles, California. This FCC facility was known as the Watson unit.

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Bluebook (online)
7 F. Supp. 2d 425, 1997 U.S. Dist. LEXIS 22586, 1997 WL 889708, Counsel Stack Legal Research, https://law.counselstack.com/opinion/wr-grace-co-conn-v-intercat-inc-ded-1997.