Trinseo, S.A. v. Harper

District Court, S.D. Texas·Decided December 12, 2023·No. 4:20-cv-00478·Unknown

Opinion

Southern District of Texas ENTERED IN THE UNITED STATES DISTRICT COURT Neco □ FOR THE SOUTHERN DISTRICT OF TEXAS HOUSTON DIVISION TRINSEO, S.A., § Plaintiff, v. CIVIL ACTION NO. 4:20-CV-0478 STEPHEN HARPER, et al., : Defendants. ORDER Before the Court is Defendant Kellogg Brown & Root, LLC (“KBR”)’s Motion for Summary Judgment (Doc. No. 129). Defendants Steve Harper, Steve Harper Consulting, Inc., Polycarbonate Consulting Services, Inc., William Davis, and Polycarbonate Resins Consulting, LLC (collectively, “Defendants”) join KBR’s motion. (Doc. No. 129 at 6). Plaintiff Trinseo Europe GmbH □□ (“Trinseo” or “Plaintiff”) filed a response (Doc. No. 143). KBR filed a reply, and Trinseo filed a sur-reply. (Doc. Nos. 172, 190). After reviewing the briefings, evidence, and relevant law, the Court hereby GRANTS IN PART and DENIES IN PART Defendants’ motion (Doc. No. 129). I. Background This case involves the alleged theft of trade secrets used in the manufacturing of polycarbonate (“PC”). PC is a thermoplastic used to make eyeglasses, glass, and a variety of other products. PC has been made by a number of companies over the years. Historically, one of the major players in the PC industry was Dow Chemical Company (“Dow”). At some point in time, Dow placed its PC assets into a subsidiary named “Styron.” In 2010, Dow sold Styron (along with its related intellectual property) to an affiliate of Bain Capital (“Bain”). Bain changed Styron’s

name to “Trinseo,” and the subsidiary Trinseo Europe GmbH became the eventual recipient of those assets. Trinseo Europe GmbH operates in the PC industry today. It is the Plaintiff herein. Dow developed an interfacial process for developing PC and chose to patent this technology. Defendant Harper worked at Dow in the PC department and, along with other Dow PC employees, left Dow some years ago. After leaving, Harper began his own PC consulting business. In 2011, Defendants admit that Harper disclosed alleged trade secrets to Pete Pavlechko, an employee of SRI International (“SRI”). Pavlechko published the information in a 2011 SRI Report titled Polycarbonate via Dow Phosgenation Process. (Doc. 129-1, Ex. 4). Following the publication, Trinseo contacted SRI expressing concern that the report contained trade secrets that were not publicly available. SRI disclosed to Trinseo that it had worked with “various consultants” in writing the report. (Doc. No. 129-1 ex. 2 at 51:10-52:6). Ultimately, it appears that SRI published an updated version of the 2011 SRI Report with the blessing of a Trinseo employee, Jerry Duane (“Duane”). Then, in 2014, Trinseo and KBR crossed paths. KBR was either already performing or seeking to perform certain services in China. In support of KBR’s operations there, it made the decision that it wanted to be able to offer its Chinese clients a complete package that would enable them to design, build, and operate PC plants. To further this goal, KBR began to search for individuals or an existing PC company to provide it with the expertise it lacked. It approached a number of individuals and entities, including Trinseo. The talks between KBR and Trinseo progressed far enough that in 2014 the two entities signed a confidentiality agreement to cover their negotiations. During these discussions, KBR told Trinseo’s representatives that it had heard rumors that former Dow employees were “consulting” for third parties. The exact extent of this

disclosure is not exactly clear. Soon thereafter it was decided that the parties would not be going forward in any joint business venture. In 2017, KBR hired the co-defendants as consultants for their knowledge of the interfacial PC process. KBR allegedly used an improved version of Dow’s original technology and licensed it to two clients before this litigation. (Doc. No. 129 at 8). In the present litigation, Trinseo alleges that the following items, (a) through (m), comprise trade secrets misappropriated by Defendants: (a) preliminary design packages (“PDPs”), design drawings of manufacturing plants, process flow diagrams, equipment specifications, operating conditions for optimal polycarbonate production in the polymerization or “wet” side of a polycarbonate plant; (b) product formulations and recipes for different grades of high quality polycarbonate flake with differing melt flows specifically for Trinseo’s Calibre™ line of polycarbonate, including specific information about the composition of each product grade with acceptable ranges of composition (including, among others, the optimal combination of tints, dyes, pigments, mold release and thermal stabilizers, UV stabilizers, and ignition resistant additives for desired product grade and performance characteristics); (c) [omitted from the pleadings] (d) the concept, design, materials, specifications, operating instructions, software, control algorithms and plans to safely and efficiently design, build, and operate interfacial polycarbonate flake manufacturing facilities; (e) the design of polycarbonate manufacturing plant components, such as the phosgene reactor, phosgene scrubber, dryers, devolatilization columns, piping and instrument design, wastewater stripping columns, along with the operating discipline, operating ranges, operating conditions, and flowrates that are part of the operating code for such components; (f) the components contained within the continuous pipe reactor’s pressure vessel containment system; (g) specially designed atomization nozzles (also called mixing nozzles) used to atomize the polymer solution with high pressure steam without fouling or clogging the nozzle with polymer (including materials of construction, dimensions, tolerances, finishes, and optimal operating conditions and settings); (h) the design and optimal operating conditions for the “snake” and loop process used in the devolatilizing drying process, with associated critical venturi, drying tubes and collection header, all of which are crucial to the efficient production of high-quality flake polycarbonate with a minimum of fines; (i) the design of the MeCl12 stripper column that separates the polymer flake from the devolatilized methylene chloride solvent and devolatilizing steam; (j) the design of the unique steam devolatilization process used to recover polymer from the washed polymer/solvent solution;

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