Eltech Systems Corp. v. PPG Industries, Inc.

710 F. Supp. 622, 11 U.S.P.Q. 2d (BNA) 1174, 1988 U.S. Dist. LEXIS 16031, 1988 WL 151639
CourtDistrict Court, W.D. Louisiana
DecidedDecember 15, 1988
DocketCiv. A. 85-1533-LC
StatusPublished
Cited by11 cases

This text of 710 F. Supp. 622 (Eltech Systems Corp. v. PPG Industries, Inc.) is published on Counsel Stack Legal Research, covering District Court, W.D. Louisiana primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Eltech Systems Corp. v. PPG Industries, Inc., 710 F. Supp. 622, 11 U.S.P.Q. 2d (BNA) 1174, 1988 U.S. Dist. LEXIS 16031, 1988 WL 151639 (W.D. La. 1988).

Opinion

*624 OPINION

VERON, District Judge.

This is a patent suit brought by plaintiffs ELTECH SYSTEMS CORPORATION and OXYTECH SYSTEMS INCORPORATED, (hereinafter referred to collectively as “Ox-yTech”) under the Patent Laws, Title 35, United States Code to enforce U.S. Patent Nos. 4,489,025 and 4,410,411 (hereinafter the ’025 and ’411 patents, respectively) against defendant PPG Industries, Inc. (hereinafter referred to as “PPG”).

This Court has jurisdiction of the parties and of the subject matter of this action by virtue of Title 28, United States Code, Section 1338.

Venue is proper and uncontested. 28 U.S.C. § 1400(b).

OxyTech is the present owner of the entire right, title and interest in and to each of the patents in suit, and the owner of all rights to recover damages for infringement of said patents. As the owner of the entire right, title and interest, Oxy-Tech has the right to invoke the power of the state in order to exclude others from utilizing the patentee’s discovery without its consent. Zenith Radio Corp. v. Hazeltine Research, 395 U.S. 100, 89 S.Ct. 1562, 23 L.Ed.2d 129 (1969).

The validity and enforceability of all claims of both the ’025 and '411 patents are uncontested in this action.

BACKGROUND

A. The Chlor-Alkali Cell

Chlorine and sodium hydroxide are sold as commodity chemicals. Chlorine is used in making numerous petrochemical products and intermediates and for other industrial purposes. Sodium hydroxide is widely used in the aluminum industry and for dyes and soaps. PPG’s Lake Charles plant produces chlorine gas at a capacity rate of over 3,000 tons a day. Chlorine is produced by the electrolysis of salt brine obtained from local salt deposits. The electrolysis process involves passing an electric current of up to 75,000 amps through the aqueous salt solution (brine). The electric current separates the positively charged sodium ion (Na+) from the negatively charged chlorine ion (Cl — ) in the salt solution (NaCl). The salt compound thus decomposes, freeing the chlorine and sodium ions.

This electrolysis process takes place in banks of large electrolytic cells. The electrolytic cell is a tank-like structure containing a metal mesh anode (positive plate) and a metal mesh cathode (negative plate). These two plates are separated by a small gap of about one-quarter inch. The narrower the gap, the greater the current efficiency of the system. Brine is continuously fed between the anode and cathode plates and the electric current flows from the anode to the cathode through this aqueous salt solution. In the process, the negatively charged Cl— ions are attracted to the positive anode plate and recovered as chlorine gas. Likewise, the positively charged Na+ ions are attracted to the negative cathode plate where they mix with the OH + ions in water to form sodium hydroxide (NaOH) which is then recovered from the cell. Because they generate chlorine and sodium hydroxide, these electrolytic cells are sometimes referred to as chlor-alkali cells. 1

B. The Diaphragm

Between the anode and cathode mesh plates lies the third major and critical component of the chlor-alkali cell — the diaphragm. The diaphragm separates the anode and its surrounding anolyte fluid and gases (the anolyte chamber) from the cathode and its surrounding catholyte fluid and gasses (the catholyte chamber). This *625 diaphragm is hydraulically permeable. It allows the brine to flow from the anolyte chamber to the catholyte chamber at a controlled rate and at the same time permits the passage of select ions.

The diaphragm must also be resistant to the chemically corrosive acid, caustic, and hypochlorite environment of the cell, and it must be able to withstand the turbulent, abrasive, erosive, tearing and swelling physical forces generated by the electrolysis process in the cell. To date, asbestos is the material which has been found to have the best combination of necessary properties for the cell diaphragm and is the material employed by PPG in its diaphragms.

The asbestos diaphragm is deposited directly onto the face of the cathode mesh plate by vacuum deposition from a slurry which is formed by dispersing asbestos fibers in cell liquor. Cell liquor is obtained directly from the catholyte chamber of operating chlor-alkali cells and thus contains both salt and sodium hydroxide (caustic) dissolved in water.

When the cathode mesh plate is immersed in the asbestos-containing cell liquor slurry, a vacuum pulls the slurry liquid through the mesh drawing the asbestos fibers tightly against the cathode, forming a compacted layer. When the deposited asbestos fibers have reached a thickness of about one-eighth of an inch on the cathode, the vacuum is turned off and the cathode is removed from the slurry. These deposition steps are old in the art of diaphragm technology and form no part of the invention here in suit.

Once the asbestos diaphragm is deposited onto the cathode, it is placed in a cell where it acts both as a separator and a filter. The diaphragm is located on the surface of the cathode which faces the anode and thus is between the anode and the cathode. At this point, the gap between the anode face and the asbestos diaphragm deposited on the cathode is about one-eighth inch. The in-place diaphragm serves to separate the anolyte chamber from the catholyte chamber because it is relatively impervious to the passage of brine, and to the chlorine and hydrogen gases generated in the anolyte and catho-lyte chambers, respectively. At the same time, the diaphragm must permit the passage of some brine and sodium ions from the anolyte chamber to the catholyte chamber at a controlled rate of flow.

The rate of flow of the incoming brine feedstock to the anolyte chamber of the chlor-alkali cell is adjusted to be slightly more than the rate of flow through the diaphragm. This causes a differential level (head) of brine to be built-up in the anolyte chamber. This differential level provides the driving force for the flow through the diaphragm into the catholyte chamber.

C. Developments in Diaphragm Technology

In the early 1970’s, a new anode technology called Dimensionally Stable Anodes based upon the use of titanium metal replaced graphite anodes. The new, long life, metal anodes eliminated plugging of the diaphragm due to graphite particles, substantially extended the useful diaphragm life, and made the development of a dimensionally stable asbestos diaphragm economically attractive.

Further development of titanium metal anode technology led to the invention and introduction of the expandable anode in the early 1970’s. The expandable anode gave the potential for diaphragm cells to be more electrically efficient and to perform at high current density for long periods of time.

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710 F. Supp. 622, 11 U.S.P.Q. 2d (BNA) 1174, 1988 U.S. Dist. LEXIS 16031, 1988 WL 151639, Counsel Stack Legal Research, https://law.counselstack.com/opinion/eltech-systems-corp-v-ppg-industries-inc-lawd-1988.