Plax Corp. v. Elmer E. Mills Corp.

106 F. Supp. 399, 93 U.S.P.Q. (BNA) 496, 1952 U.S. Dist. LEXIS 4016
CourtDistrict Court, N.D. Illinois
DecidedJune 6, 1952
DocketNo. 50 C 234
StatusPublished
Cited by7 cases

This text of 106 F. Supp. 399 (Plax Corp. v. Elmer E. Mills Corp.) is published on Counsel Stack Legal Research, covering District Court, N.D. Illinois primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Plax Corp. v. Elmer E. Mills Corp., 106 F. Supp. 399, 93 U.S.P.Q. (BNA) 496, 1952 U.S. Dist. LEXIS 4016 (N.D. Ill. 1952).

Opinion

BARNES, Chief Judge.

This is a suit by Plax Corporation, a corporation of Delaware having a regular and established place of business at Hart[400]*400ford, Connecticut, against Elmer E. Mills Corporation, a corporation of Illinois having a regular and established place of business at Chicago, Illinois, wherein the plaintiff charges that it owns and that the defendant has infringed four letters patent of the United States, as follows:

Letters Patent No. 2,128,239, issued August 30, 1938, to E. T. Ferngren on an application filed February 25, 1933, for a process of molding plastic materials;

Letters Patent No. 2,175,053, issued October 3, 1939, to E. T. Ferngren, on an application filed August 18, 1936, for a process and apparatus for working organic plastic material and producing containers therefrom;

Letters Patent No. 2,230,188, issued January 28, 1941, to E. T. Ferngren, on an application filed March 29, 1938, on a process of and apparatus for forming articles from plastic material; and

Letters Patent No. 2,349,177, issued May 16, 1944, to W. H. Kopitke on an application filed May 9, 1941, on a method of and apparatus for making blown plastic articles.

Ferngren Patent No-. 2,128,239 states:

(page 1, column 1, line 1) “This invention relates to a process of blowing bottles and various other types of containers and shapes from materials in a plastic state.
“The material used may be of any nature, but preferably it should be in a viscous deformable plastic state, and have physical properties such as are possessed by certain molten materials, semi-solid solutions of matter and many organic materials dispersed in solvents and the like, and by plastic pastes, gels or sols, or by thermoplastic materials in general, by themselves, or when compounded and by many natural gums and synthetic products.
“The method itself is partly an extrusion procedure and partly a synchronized distending operation on the extruding material while the same is received in, or is caused to cover the walls of a mold element, or is otherwise formatively restrained, or caused to assume a given shape.
“The extruding process is capable of many modifications but as herein practiced, consists of advancing the plastic material as a hollow cylindrical stream, which stream is first caused to move confluently or to unite at a focus or point to form a tube closed at a point adjacent to the lower end of a receiving element or mold, and preferably near the bottom end of the mold cavity. By this means a predetermined mass of the plastic may be delivered upon the lower inner face of the mold used.
“The extruding material is also moved lengthwise of the mold cavity in such fashion that the extruding point of the annular stream is progressively moved or caused to register with successive points of the mold cavity, the movement being continuous, or intermittent, or variable, as required. Following this action the hollow cylindrical stream or body is extruded at a rate which may vary depending upon the wall thickness desired for different parts of the article being formed.
“In this connection if the girth or diameter at any one point or level of a mold cavity is more or less than at another point or level of the mold, the extruding stream velocity and its quantity may be suitably governed to-insure proper thickness- or strength of the -container wall at all points or levels along the inner faces of the mold cavity. For example, in case of a bottle, the neck diameter is much less than-the body diameter.
“The distending operation by the-introduction of compressed air or the like within the hollow extruding material takes place after the extruded annular mass has been closed at its end and assists in the subsequent and continuous extrusion of the material to-progressively expand it to conformity with the walls of the mold. As the emitting point of the progressively extruding tubular body traverses the entire mold cavity and, as in case of a bottle mold, arrives at the neck and mouth forming section of the mold, the walls of the hollow extrusion are [401]*401normally progressively forced outwardly and laid against the walls of the mold cavity thus forming the walls of a completed bottle.
“The distending or blowing agent may consist of a liquid or a gaseous medium under pressure, or it may 'be any fluid suitable for use with the material employed.
******
(page 2, column 1/ line 36) ’ “The plastics now available, ranging from coal-tar and petroleum derivatives to casein and sugar derivatives, may be supplied from a compression chamber under suitable control as to direction, and at such speed and amount as desired or necessary, the equipment used for this purpose not being shown. The movement of the plastic material may also be reversed as may be necessary in carrying out the process.
* * * * * *
(page 3, column 1, line 62) “The plastic material introduced into the mold as herein described, if of the cellulose derivative type, may be compounded with many synthetic resins and plasticizers such as tricresyl phosphate. The material is heated to a point of having fluid mobility under pressure before it is advanced from a supply chamber through the passage of the tube, which normally should be kept at a temperature sufficiently elevated to prevent chilling of the material. Benzyl cellulose may be thus prepared and used for extrusion when heated.
******
(page 4, column 1, line 16) “The step of causing or producing a confluent closing of the forward end of the extruding tubular stream by aid of suction from the tube (passage) inside of the tube or by any other means can be brought about before the tube reaches the lower position shown in figure 1, and in fact at almost any point during the downward movement of the tube through the opening and while it is passing' downwardly through the mold cavity.
“The gathering into a body of the walls of the extruding (plastic) tube may then be brought about by reducing the air pressure in the passage at any predetermined instant, while simultaneously extruding the plastic material from the passage; both actions being caused to occur at the same moment the tube is moving downwardly or upwardly through the mold cavity. In some operations it is advantageous to cause this initial closing of the forward end of the hollow extruding body in the space above or outside the mold ring, at which time the tube may be stationary in the outside position relative to the mold or moving toward or away from the same.

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Related

Application of John G. Miller
311 F.2d 955 (Customs and Patent Appeals, 1963)
Eversharp, Inc. v. Fisher Pen Co.
204 F. Supp. 649 (N.D. Illinois, 1961)
Plax Corp. v. Flexcel Container Co.
154 F. Supp. 704 (W.D. Missouri, 1957)
Plax Corp. v. Precision Extruders, Inc.
137 F. Supp. 495 (D. New Jersey, 1956)
Application of Ralph G. H. Siu
222 F.2d 267 (Customs and Patent Appeals, 1955)
In re Siu
222 F.2d 267 (Customs and Patent Appeals, 1955)

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Bluebook (online)
106 F. Supp. 399, 93 U.S.P.Q. (BNA) 496, 1952 U.S. Dist. LEXIS 4016, Counsel Stack Legal Research, https://law.counselstack.com/opinion/plax-corp-v-elmer-e-mills-corp-ilnd-1952.