Basf Corporation v. Johnson Matthey Inc.

875 F.3d 1360
CourtCourt of Appeals for the Federal Circuit
DecidedNovember 20, 2017
Docket2016-1770
StatusPublished
Cited by141 cases

This text of 875 F.3d 1360 (Basf Corporation v. Johnson Matthey Inc.) 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
Basf Corporation v. Johnson Matthey Inc., 875 F.3d 1360 (Fed. Cir. 2017).

Opinion

TARANTO, Circuit Judge.

BASF Corporation owns U.S. -Patent No. 8,524,185, which describes and claims systems, for performing catalytic conversion of nitrogen oxides (NOx) ⅛ an exhaust gas stream. As relevant here, the patent claims a partly-dual-layer arrangement of coatings on a substrate over which exhaust gas passes—a coat along the full length of the substrate containing “a material composition B effective to catalyze selective catalytic reduction (SCR) of NOx”; and beneath part of that coat, on the outlet end of the gas passage, a partial-substrate undercoat containing “a material composition A effective for catalyzing NH3 oxidation” (ammonia oxidation, or AMOx). ’185 patent, col. 19, lines 40-55- (claim 1); see also id., col. 20, lines 3-5 (dependent claim 5, similar); id., col. 20, lines 42-62 (independent claim 17; similar, but adding restrictions concerning precious metals). Iii 2014, BASF sued its competitor, Johnson Mat-they Inc., for. infringement of the ’185 patent. The district court held that the “effective for catalyzing”/“effective to catalyze” language is indefinite and entered judgment of invalidity of all claims on -that basis. ¡

BASF appeals. We have jurisdiction under 28.U.S.C. § 1295(a)(1).-We reverse the judgment of invalidity for indefiniteness. We remand for further , proceedings in accordance with this opinion.

I

A

The ’185 patent claims a partly-dual-layer arrangement of catalytic coatings on a substrate over which exhaust gas passes, e.g., the walls of a flow-through chamber having a honeycomb structure,, whose function is to remove NOx from a stream of exhaust gas while minimizing the amount of ammonia that ends up being released from the system. Claim 1 is representative:

A catalyst system for treating an exhaust gas stream containing. NOx, the system comprising:
at least one monolithic catalyst substrate having an inlet end and an outlet end; an undercoat washcoat. layer coated on one the outlet end of the monolithic substrate and which covers less than 100% of the total length of the monolithic Substrate, and containing a material composition A. effective .for catalyzing NH3 oxidation;
an overcoat washcoat layer coated over a total length of. .the monolithic substrate from the inlet end to the outlet end sufficient to overlay the undercoat wash-coat layer, and containing a material composition B effective to catalyze selective catalytic ■ reduction (SCR) of NOx; and ■ -
wherein material composition A- and material composition B are maintained as physically separate catalytic compositions.

’185 patent, col. 19, lines 40-55. Relevantly similar language about effective catalysis appears in claims 5 and 17, as already noted. The parties have not suggested any distinction among the claims or their language that is material to the point at issue. We focus on the language, “composition .'.. effective to catalyze,” but our analysis applies equally to “composition ... effective for catalyzing.”

The specification describes the generally contemplated two-phase operation of a partly-dual-layer, two-zone coating system, which involves a full-length coating that is the sole coat for part of the substrate (the first zone) and that lies atop another layer on part of the substrate, toward the outlet of the gas stream (the second zone). The gas stream travels along the substrate from the inlet to the outlet and is exposed, along the full length of the substrate, to “material composition B,” which removes NOx by catalyzing an SCR reaction between NOx and ammonia. Id., col. 11, lines 40-47, The ammonia for the reaction may be injected into the gas upstream of the catalysts. Id., col. 3, lines 28-29. That SCR process, however, can leave unreacted ammonia, which, if untreated, might escape through the outlet of the system along with the treated gas stream. Id,, col. 1, lines 41-48. The ’-185 patent’s system addresses that problem (so-called “ammonia slip,” id., col, 1, line 41) by use of an undercoat layer, beneath a part of the full-length layer of SCR catalyst, toward the outlet end of the substrate. At that dual-layer end of the substrate, the ammonia is exposed to the undercoat, which contains a “material composition A” effective to catalyze an AMOx reaction, reducing the residual, ammonia, see id., col. 11, lines 47-52; and the overcoat continues -to minimize NOx via SCR, id., col. 12, lines 37-45.

When referring to compositions A and B, the specification uses the language of “composition ..: effective to catalyze” (or comparable “effective” terminology), e.g., id., col, 2, lines 5, 9, 22, 24; col. 3, lines 9, 14, 33, 38-39; col. 5, lines 40, 48, 55-58, and, in ways that are interchangeable for present purposes, the names “SCR catalyst” and “ammonia oxidation [or AMOx] catalyst,” e.g., id., col,-1, lines 30-58; col. 5, lines 38-49; col. 6, lines 48-55; col. 8, lines 4-14, 37-41; col. 10, lines 56-61; col. 11, lines 9-20; col-11, line 65 through col. 12, line 3; col. 12, lines 13-26. (It also uses certain other terms, such as “SCR composition” and “NHS oxidation composition.” E.g., id., col. 7, line 58; col. 8, line 48.) The specification sets' out the- specific-'stoi-chiometric chemical reactions for the catalysts. Id., col. 5, lines' 33-49. It identifies a variety of materials that can be used for “material composition A” {e.g.,- “refractory metal oxide[s] containing ■ alumina, silica, zirconia, titania, ceria”) and “material composition B” (e.g,, an “aluminosilicate molecular sieve [with] one of the crystal framework types FAU, MFI, MOR, BEA”). Id., col. 2, lines 29-58. And it includes various examples-of how catalyst layers are prepared and how they -perform under practical engine conditions in comparison to the prior art. Id., col. 13, line 54 through col. 19, line 14.

B

In its opening'brief on claim construction in this case, BASF urged that the “composition ... effective to catalyze” phrases have a plain and ordinary.meaning, so it proposed simply using those phrases followed by the qualification, “as understood in the art of exhaust systems.” J.A. 105. BASF also argued that the phrases are not indefinite, contrary to the contention Johnson had stated in advance of claim construction.

Johnson responded that the phrases are indefinite, because the “effective to catalyze” language used to identify the claim compositions is functional, and there are no “objective boundaries on (1) what amount of effectiveness is required, or (2) how to measure the effectiveness.” J.A. 380; see id. at 379-93. Johnson’s expert, Dr. William S. Epling, filed a declaration in support. He stated that there are effectively a “limitless number” of materials that can catalyze ammonia oxidation or SCR reactions. J.A. 953, 955. Regarding SCR catalysts, he stated that the materials listed in the ’185 patent specification were known in the art to be effective catalysts for SCR of NOx. Regarding AMOx catalysts, Dr. Epling listed various materials he considered to be known in the art as effective catalysts. He also stated that “objective standards,” such as “percent conversion,” exist in the field of catalysis to test and quantify catalytic function. J.A. 957.

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875 F.3d 1360, Counsel Stack Legal Research, https://law.counselstack.com/opinion/basf-corporation-v-johnson-matthey-inc-cafc-2017.