Standard Havens Products, Inc. v. Gencor Industries, Inc.

953 F.2d 1360, 1991 WL 279385
CourtCourt of Appeals for the Federal Circuit
DecidedMarch 20, 1992
Docket90-1048
StatusPublished
Cited by113 cases

This text of 953 F.2d 1360 (Standard Havens Products, Inc. v. Gencor Industries, 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
Standard Havens Products, Inc. v. Gencor Industries, Inc., 953 F.2d 1360, 1991 WL 279385 (Fed. Cir. 1992).

Opinion

ARCHER, Circuit Judge.

Gencor Industries, Inc. (Gencor) appeals from a judgment of the United States District Court for the Western District of Missouri, No. 88-1209-CV-W-3, August 8, 1989, holding, inter alia, that: (1) U.S. Patent No. 4,787,938 (’938 patent) is not invalid and was infringed by Gencor; (2) Standard Havens Products, Inc. (Standard Havens) is entitled to damages for patent infringement of $5,931,000; and (3) Standard Havens is entitled to damages of $2,284,000 on its breach of contract claim. We affirm-in-part, vacate-in-part, and remand.

I

BACKGROUND

A. The Technology

The ’938 patent, issued to Michael R. Hawkins on November 29, 1988 and assigned to Standard Havens, is directed to a method of producing asphalt compositions.

Asphalt compositions were often produced in a large horizontal rotating drum. Water-laden aggregate (e.g., crushed rock) was introduced at one end of the drum, was heated and dried by a stream of hot gases produced by a burner flame. The dried aggregate was then combined with liquid asphalt, mineral binder or fines (i.e., crushed materials to impart thickness or body), and in some instances recycled as-phaltic material removed from road surfaces, to produce an asphalt composition.

In one method, known as a co-current or parallel flow system, the hot gases produced by a burner flame flowed in the same direction as the aggregate and other ingredients to be mixed to the opposite end of the drum. In another method, styled counter-flow or countercurrent, the aggregate and other ingredients to be mixed flowed in a direction opposite that of the hot gas stream.

In those systems, the asphalt industry faced problems with pollution and product degradation. Exposing the liquid asphalt and recycled asphaltic material to excessive temperatures within the drum or in close *1364 proximity to the burner flame caused serious product degradation and produced hazardous pollutants known as “blue smoke.”

B. The ’938 Patent

Hawkins, in his invention as disclosed in the ’938 patent, attempted to solve the product degradation and pollution problems by isolating the liquid asphalt (and recycled asphaltic material, when used) from the radiant heat flux of the burner flame and from the hot gases produced therefrom. He did so by creating within the drum a zone for mixing the aggregate and liquid asphalt (and any other materials to be mixed) and keeping that zone away from the flame and its hot gases. An exterior view (Figure 1) and an interior view (Figure 3) of the Hawkins’ drum mixer, as described in the patent specification, follow:

[[Image here]]

Like much of the prior art, Hawkins’ described embodiment uses a rotating, inclined drum for mixing the asphalt composition. Aggregate, delivered at a first end 22, rotates toward the opposite end 36 by force of gravity due to an incline. (The incline is not shown here.) Initially, the aggregate is heated and dried by hot gases in a first zone, to the left of the burner head 46. Then, the aggregate enters a second zone — the annular area to the right of the burner head, particularly past the recycle feed assembly 60 (which allows introduction of recycled asphalt material into the drum) and between the combustion assembly 40 and the drum cylinder 10. In the second zone, aggregate is mixed with hot liquid asphalt and any other needed materials. The hot, mixed asphalt composition is then discharged via a mouth 36.

A gas stream is heated at the burner head and flows in a countercurrent manner through the drum to the first end (where the aggregate is introduced). Figure 3 shows the burner head fed by fuel line 45. The burner head and fuel line are part of the combustion assembly. The combustion assembly also includes a secondary air tube 42 which surrounds the primary tube 44. Fuel and primary air forced by the blower 48 are sent through the primary tube to the burner head. Secondary air, in the space between the primary tube and the secondary air tube (see the arrows in Figure 3), supports combustion at the burner head.

The ’938 patent has these four method claims:

1. A method for continuously producing an asphaltic composition from as *1365 phalt and aggregates, the steps of said method comprising:
introducing aggregate material inte-riorly of a first end of an inclined, horizontal rotating drum to flow generally from said first end to the second end of said drum;
generating a hot gas stream within said drum to flow through said drum to said first end in countercurrent relation to said aggregate material;
isolating a zone of said rotating drum from said hot gas stream;
delivering said heated and dried aggregate material to said zone isolated from said hot gas stream;
mixing said aggregate material with liquid asphalt within said zone isolated from said hot gas stream to produce an asphaltic composition; and
discharging said asphaltic composition from said rotating drum.
2. The method as set forth in claim 1, including the step of adding recycle asphalt material directly to said zone isolated from said hot gas stream.
3. The method as set forth in claim 1, including the steps of creating a curtain of falling aggregate material within said rotating drum and flowing said hot gas stream through said curtain of falling aggregate material.
4. The method as set forth in claim 1, including the step of blending a fine binder material with said liquid asphalt and aggregate material within said zone isolated from said hot gas stream.

C. Confidentiality Agreement

The contract involved in this case is a nondisclosure agreement for consulting and technical services dated May 13, 1986. Prior thereto, Standard Havens had contacted General Combustion Corporation, a wholly owned subsidiary of Gencor, to obtain consulting services in the design and manufacture of a burner for Standard Havens’ proposed counterflow asphalt plant based upon the method described in the Hawkins ’938 patent. The nondisclosure agreement required Gencor to maintain as confidential the information obtained from Standard Havens.

D. Litigation

Standard Havens initially sued Gencor for breach of the nondisclosure agreement. Gencor counterclaimed, seeking a declaratory judgment that the Hawkins patent was invalid. In response, Standard Havens charged Gencor with contributing to or inducing infringement of the ’938 patent, particularly via production of its asphalt-producing “Ultraplant.”

Trial was conducted for thirteen days before a jury. The jury answered a special verdict form, finding that the claimed invention was neither anticipated nor would have been obvious, see 35 U.S.C.

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Bluebook (online)
953 F.2d 1360, 1991 WL 279385, Counsel Stack Legal Research, https://law.counselstack.com/opinion/standard-havens-products-inc-v-gencor-industries-inc-cafc-1992.