Frankfort Wihsky Process Co. v. Mill Creek Distilling Co.

37 F. 533, 1889 U.S. App. LEXIS 2098

This text of 37 F. 533 (Frankfort Wihsky Process Co. v. Mill Creek Distilling Co.) is published on Counsel Stack Legal Research, covering U.S. Circuit Court for the District of Southern New York primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Frankfort Wihsky Process Co. v. Mill Creek Distilling Co., 37 F. 533, 1889 U.S. App. LEXIS 2098 (circtsdny 1889).

Opinion

Wallace, J.

This suit is founded upon letters patent No. 263,087, •granted August 22, 1882, to Marshall J. Allen and William E. Bradley, upon an application filed April 29, 1882, for “process of making whisky.”' The complainant alleges that the defendants infringe the first, second, and fourth claims of the patent. The defendants interpose nearly all the statutory defenses. The patent in suit is one of three patents granted to the same patentees for improvements in the process of making whisky., A proper understanding of the case requires some consideration of each of these patents. The first was granted July 6, 1880, and the invention therein as stated in the specification, consists “in freeing the slop or spent beer of bran and other solid particles, and employing the remaining liquid portion in place of water in the succeeding operations with the-fresh grain.” The succeeding operations are “thinning down the mash, mashing the grain, and filling up the fermenting vats.” The advantages of using the liquid of the slop after the solid particles have been eliminated are stated in the specification as follows:

“The-Starch and sugar in the slop or spent beer, which it is the object of this process to save, are nearly all retained in the liquid portion after separation. As only this liquid portion is used in this process, there is obtained by the separation of the bran, chaif, and coarse particles of grain a greatly reduced bulk of materia], thus making it possible to get into the fermenting vats with the mash the maximum quantity of the starch and sugar contained in the slop or spént beer. It would be impossible to use the slop or spen(t, beer with the bran, chaif, and coarse particles of grain in it in sufficient quantity to obtain the results reached by this process; viz., the saving of the starch and sugar in the slop, and their conversion into alcohol, for the reason that a few repetitions of the process would cause such an accumulation of .bran, chaff, and.coarse particles of grain in the fermenting vats, that the beer will become’thick, and it- would be impossible to work it. By this process, there[535]*535fore, the starch and sugar in the slop or spent beer which were not converted into alcohol by the first fermentation, are introduced into the fermenting vats with the mixed mash, and thus are subjected to a second fermentation, producing a large percentage of alcohol which has heretofore been lost.”

Mo mode of treatment of the slop in order to etf'ect a separation of the liquid from the solid particles, or to use it in the subsequent processes, is pointed out in the patent; and the claim is broadly for the process of freeing the slop and introducing the liquid obtained in place of water in the succeeding processes of fermentation. This patent was worthless. There was no novelty in the broad process described and claimed. This sufficiently appears by a reference to the treatise of Dnbrufaut on the Art of Distillation, published in Paris in 1824. He says:

“ In a continuous operation tiie spent liquor or swill which is drawn from tiie still ought to be stored in hogsheads, or in a cistern constructed for tiie purpose. There the solid matter is deposited and tiie clear liquid floats above. This liquor may he profitably employed in succeeding operations to dilute the ' mash. It is found that this practice has the advantage of bringing to tlio fermentation a liquor which still contains fermentable matters which have escaped in the previous separation. This course may bo continued through many successive operations. * * We should cease to use the clear portion of the spent liquor when, after many operations, it has become so acid as to injure, rather than support, the vinous fermentation.”

The material parts of the specification of the patent in suit are as follows:

"The object of our invention is to increase the yield of whisky from a given amount of grain by utilizing in subsequent processes the refuse product of previous processes; and this we do by first preparing the refuse product, and bringing it into a condition in which it may be advantageously used, and secondly by introducing such prepared product into the subsequent processes of wliisky-making. By our improvement we separate from tiie slop or spent beer the bran, chaff, and refuse particles by mechanical means, and then so operate with the strained slop as to preserve it from acetic, lactic, or putrid fermentation, and utilize it in the process of making whisky, returning with it all the useful bodies which it contains. It is well known that tiie spent beer contains, in suspension, in the first place, a considerable amount of refuse material of comparatively large size, such as the chaff; bran, and larger particles of grain, and in the second place, minute particles of sugar or glucose, starch, and yeast. This second class of particles it is very important to preserve and introduce into the subsequent operations of wliisky-making. This class of particles are so minute as that they will pass through the meshes of a fine sieve, and yet are sufficiently solid and separate from the liquid to form a deposit in any vessel in which the liquid may remain at rest. The purpose of our invention is to retain these fine or valuable particles in the liquid-which is to be returned, and to separate from this liquid the coarse or refuse particles, while at the same time the liquid is maintained in a sweet condition. In carrying out our process practically the slop or spent beer as it is blown from the still is run through a straining apparatus similar to the bolting machine in a tlour-miii, provided with a copper wire straining cloth of about thirty wires to the inch. The thick'portion strained out is rejected, and may be used as food for cattle, and the liquid portion is run through a coil in a tank of cold water, or some equivalent apparatus. In this way it is rapidly cooled from a temperature near the boiling point down to a point as low as the water will produce. It should be below 80 deg. This cool liquid slop is [536]*536then stored ready for use in a tank supplied with suitable agitators to keep the small particles which it may contain in suspension, orto stir them up previous to the further utilization of the slop. It is absolutely necessary for the best results of our process that all of the sugar, starch, and yeast particles be returned with the spent beer, and utilized in the subsequent operation of making whisky. Having so mechanically strained or Altered and cooled our spent beer, we add this cold slop to the liquid in the mash-tub at the end of the mashing, for the purpose of cooling and thinning down the mash, and when the mash is run into the fermenting vats we also use the cold, thin slop or spent beer to complete the filling up of the fermenters, instead of water. We find as the result of this process a greatly increased yield, which we cannot obtain in any other way known to us. The special points to be observed in carrying out our process successfully are—First, the sieving or separation by mechanical means—preferably an ordinary sieve—of the coarse or refuse particles; secondly, the cooling of the slop or spent beer quickly, by suitable means, in order to prevent the increase and accumulation of acid in the.same; and, thirdly, the returning of this slop, together with the valuable particles which it contains, and its utilization in the subsequent processes of whiskymaking.”

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Bluebook (online)
37 F. 533, 1889 U.S. App. LEXIS 2098, Counsel Stack Legal Research, https://law.counselstack.com/opinion/frankfort-wihsky-process-co-v-mill-creek-distilling-co-circtsdny-1889.