Frederick Iron & Steel Co. v. Sanford Riley Stoker Co.

287 F. 495, 1923 U.S. App. LEXIS 2345
CourtCourt of Appeals for the Fourth Circuit
DecidedFebruary 6, 1923
DocketNo. 1951
StatusPublished
Cited by5 cases

This text of 287 F. 495 (Frederick Iron & Steel Co. v. Sanford Riley Stoker Co.) is published on Counsel Stack Legal Research, covering Court of Appeals for the Fourth Circuit primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Frederick Iron & Steel Co. v. Sanford Riley Stoker Co., 287 F. 495, 1923 U.S. App. LEXIS 2345 (4th Cir. 1923).

Opinion

KNAPP, Circuit Judge.

The appellants were defendants in the court below, and they so will be designated in this opinion. The suit was brought for alleged infringement of two patents owned by the plaintiff company, namely, No. 1,152,222, issued August 31, 1915, and No. 1,090,651, issued March 17, 1914, both for improvements in underfeed stokers. The latter patent was withdrawn at the trial, and therefore has not been considered. The bill charges infringement of claims 3, 9, and 10 of patent No. 1,152,222, herein referred to as the Riley patent, and they, are the only claims in controversy. The trial court held these claims valid and infringed, and entered the usual decree for an injunction and accounting. 274 Fed. 864. From this decree the defendants appeal.

The Riley patent, No. 1,152,222, contains a statement to the effect that it is founded on a stoking apparatus of the type shown and described in the patent to Taylor, No. 792,862, and has for its object, among other things, the obtaining of a more complete combustion of the fuel used, and thus avoiding loss of fuel in the ash, which was found to be incidental to the operation of the Taylor stoker. Both the Taylor and Riley patents are fundamentally coking underfeed stokers, and the first of the kind that appears is shown in the patent to Jones, No. 470,052, which was followed by the Daley patent, No. 644,664.

In both the Jones and Daley stokers coal was introduced into a receptacle or retort, which had an open top, was closed at the sides and one end, and had the other end open to permit the entrance of coal. Into the lower part of the receptacle coal was forced through the open end by rams or pushers; the introduction of successive charges acting to force the fuel previously fed into the receptacle to the top of the latter. The upper portion of the body of coal as it emerged from the receptacle was ignited, and combustion of the fuel maintained and promoted, by forcing air under pressure across the fuel, through pipes in the Jones construction, arranged along the sides of the receptacle, and through twyer blocks, similarly arranged, in the Daley construction. In both of these structures the effect of maintaining combustion on the top of the mass of confined coal, from which air of an amount to cause combustion was excluded, was wholly or partially to coke the coal in the retort below the air supply. Consequently volatile gases were liberated from the coal, and these in rising mingled with [497]*497the air at the top of the retort and were burned. The ámoke also passed upward through the burning fuel bed at the top of the retort and was to a great extent consumed. By this economical use of1 fuel, as compared with the old method of introducing fresh green coal upon the top of a burning bed, enormous saving was accomplished.

The practical defect in the Jones and Daley stokers was that an uninterrupted uniform burning of the fuel to maintain a constant heat could not be carried on, because at frequent intervals it was necessary to expose the fire bed to outside cold air during the removal of ashes. As fresh coal- was fed into the lower part of the retort, the coal previously received was coked, forced upward, and burned. Consequently the ashes from the burning fuel at the top were spread out from tiie sides of the retort and received upon dead plates extending laterally from the sides of the retort, and when the quantity of ashes was such as to interfere with the operation of the furnace rakes introduced through apertures opening into the outer air were used for their removal.

The admission of air in this manner cooled the interior of the furnace and required a large consumption of fuel to bring the temperature back to the required point after each ash removal. Besides, the ash was necessarily raked by hand, and this involved exhausting and expensive labor. The area of the dead plates which could be raked was limited, and consequently the size of the furnace was much restricted, and because of the location of the dead plates,' and the necessity for free access to them, it was impracticable to arrange the retorts in groups.

In the Taylor construction, retorts open at each end, and twyer blocks arranged on' both sides of the retorts for directing air under pressure, which is received from an air trunk, extending beneath and transversely of the retort to the fuel forced upward to the tops of the retorts by successive charges, and dump ash plates, arranged at the rear or discharge ends of the retorts and twyer blocks, are employed. The advantageous and distinguishing feature of the Taylor device is that the retorts and twyer block's are inclined downward from their feed to their discharge ends, and that therefore the fuel is moved from the point of introduction, through the combustion zone and to the point of its discharge upon the dump plates, by the combined action of the pushers and gravity. Moreover, the twyer blocks are of such form and arrangement in respect to the retorts that their upper faces form lateral extensions of the tops of the retorts. Consequently, as the coal is forced into the lower portions of the retorts, the burning coke at their tops flows out over and covers the twyer blocks, resulting in the maintenance of a continuous fire bed extending over the retorts and twyer blocks during the operation of the stoker. This construction permits of unlimited duplication of retorts and twyer blocks, thus allowing *the installation of a furnace of any desired size. The dump plates are inclosed by the walls of the furnace, and are operated from outside the latter, so that, of course, there is no cooling of the furnace incident to ash dumping.

[498]*498The Taylor stoker was found to operate successfully under ordinary working conditions, but it developed in practice that when a substantial increase of boiler pressure was periodically necessary, and largely increased quantities of coal were introduced to secure it, there was a failure to reach the desired end. The introduction of increased quantities of coal caused large amounts of úncoked coal and unconsumed coke to be moved to and deposited upon the dump plates, on which little burning took place, and where it' rapidly accumulated and checked discharge from the retorts and twyer blocks. The necessity for keeping the dump plates clear, by frequent dumping of the -partly burned fuel, which was wasted, involved prohibitive expense, and the net result of the attempt to supply the fuel in quantities sufficient for the purpose mentioned was a failure to maintain the required heat and a great waste of fuel.

In 1908 several of the Taylor stokers were placed with the Electric Corporation, of Lowell, Mass., and were used in connection with its plant for generating electricity for lighting purposes, etc., where the requirement for increased power at certain times of the day was imperative, Failure of the stokers properly to function under excess load conditions naturally led to the serious consideration of means for curing their inherent defects.

Riley, who was employed by the then owners of the Taylor patent, had several conferences with'representatives of-the Electric Corporation, among them James H. Wood, who was the engineer in charge of the plant of the corporation, at which conferences the defects of the stoker were discussed. Numerous suggestions as to changes , and additions were made, but, 'as the problem presented was difficult of solution, no remedy was quickly found. The requirements were many. A mere lengthening of the retorts ajid of the coacting elements would not avail, because in the end, under feed of large amounts of fuel, clogging would ensue.

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287 F. 495, 1923 U.S. App. LEXIS 2345, Counsel Stack Legal Research, https://law.counselstack.com/opinion/frederick-iron-steel-co-v-sanford-riley-stoker-co-ca4-1923.