US580568A - Process of manufacturing fuel - Google Patents

Process of manufacturing fuel Download PDF

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US580568A
US580568A US580568DA US580568A US 580568 A US580568 A US 580568A US 580568D A US580568D A US 580568DA US 580568 A US580568 A US 580568A
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tar
manufacturing fuel
mass
fuel
oil
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/10Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
    • C10L5/14Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders

Description

(No Model.)
F. BATTER. PROCESS OF MANUFACTURING FUEL.
Patented Apr. 13, 1897.
Wwnmw,
FRANK BATTER, OF MARSHFIELD, OREGON.
PROCESS OF MANUFACTURING FUEL.
sPECIFIG'ATIO N forming part of Letters Patent N 0. 580,568, dated April 13, 1897.
Applicatioh filed March 16, 1896. Serial No. 583,347.
To all whom, it may concern.-
Be it known that I, FRANK BATTER, a citizen of the United States, residing at Marshfield, county of Coos, State of Oregon, have invented an Improvement in the Process of Manufacturing Fuel; and I hereby declare the following to be a full, clear, and exact description of the same. 1
My invention relates to the manufacture of fuel; and it consists of the process hereinafter described and claimed.
In the accompanying drawing I have shown an apparatusby which my process can be carried out.
In carrying out my process I first place the coal or lignite to be treated in retorts A, such as are ordinarily employed in gas-works, or of any other. suitable construction. torts are subjected to a low temperature which is suflicient to drive off the moisture, which often amounts to fifteen or more per cent. and the volatile products, which may amount to between thirty and forty per cent, and if there is a percentage of sulfur this will also be volatilized and driven off. All this volatilized material is passed through condensers B of a pattern similar to those employed in gas-works, and the tar and any oil or substance which can be condensed will be condensed at this point. IVhatever gas is formed passes on to a washing tank or chamber and is finally returned to be burned in the retortfurnaces. The tar sinks to the bottom and the oily prod ucts rise to the surface in the condenser, and these products are drawn off by means of a tar-well a and by a pump or other suitable means. From the retorts the residue remainingis withdrawn and is delivered into a grinding-mill C of any suitable description, which reduces this residue to a sufficiently fine powder or fine particles. from the condenser are then mixed with this pulverized material and the whole is delivered into a press D, which in the present case is illustrated as a screw-press, where it is compacted into a solid form, and while the material is still hot as it comes from the retort and the tai well. Afterbein g thus compacted it is removedfrom the press and allowed to stand in mass for some time, during which the ingredients appear to become more intimately united, and any tar and oil that have been These re- (N0 specimens.)
brought to the surface by pressure are reabsorbed by the solid material. After this compound has cooled off the mass will have been found to have absorbed the tar and oil, so as to form with the coked part of the coal a body having a large increase in the percentage of solid carbon and free from moisture, sulfur, etc. The mass is then placed in a furnace, such as illustrated at E, and there heated in a close oven until it becomes a soft or friable mass and any remaining volatile portion is driven off. In this condition it is placed in molds or dies of any suitable form, such as illustrated at F, and these dies are placed under...a. .steem :.11a1nmer9r p rful .PIIQSS.-J,
which will compress the or blocks of convenient size for use. The heating in the second furnace or oven drives off any oil or lighter product which would otherwise interfere with the permanent solidity of the blocks when burned. By this process I am enabled to utilize all the valuable portion of lignites and coals carrying a low The tapandoilpercentage of fixed carbon by first separating from the solid portion all moisture, sulfur, &c., and driving out the oily product-s and coal-tar, the latter two being again recovered to a large extent from the condensers.
In connection with the condenser I have shown a fan or blower G, which acts to withdraw a low quality of gas and any non-c011- densable volatile products, and after passing through another washing-chamber, (shown at 1-1,) which serves to arrest any particles of oil or tar which may have been carried thus far, the gas will be returned from this condenser or washer and delivered into the furnaces b-e neath the retorts, to be used as a fuel, by means of a pipe I.
Having thus described my invention, what I-claim as new, and desire to secure by Letters Patent, is
The process of manufacturing fuel from lignites and coal containing a low percentage of fixed carbon, consisting in subjecting the material to alow temperature in a closed retort to drive off the moisture and volatile products; then collecting and condensing the volatile products and allowing the gases therefrom to ,return to the retort-furnaces to be used as a fuel, after being first subjected to a washing action; then withdrawing the residue material into ingots from the retorts and reducing it to fine particles or powder and Withdrawing the tar and oil resulting from the conden sation of the volatile products driven from the retort and mixing them with the reduced residue from the retort; then subjecting the mass to pressure While it is in a heated condition and allowing it to cool to reabsorb the tar and oil brought to the surface by pressure; then baking the 10' mass of compressed material to render it friable and drive off any volatile portions it contains; then separating the mass into blocks or ingots, in molds, and subjecting it to pressure to form permanent blocks.
In witness whereof I have hereunto set my 15 hand.
FRANK BATTER. WVitnesses:
S. H. NOURSE, JESSIE O. BRODIE.
US580568D Process of manufacturing fuel Expired - Lifetime US580568A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080200924A1 (en) * 2000-04-21 2008-08-21 Vascular Control Systems, Inc. Methods for minimally invasive, non-permanent occlusion of a uterine artery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080200924A1 (en) * 2000-04-21 2008-08-21 Vascular Control Systems, Inc. Methods for minimally invasive, non-permanent occlusion of a uterine artery

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