US1390233A - Method of increasing the specific gravity and flash-point of liquids - Google Patents

Method of increasing the specific gravity and flash-point of liquids Download PDF

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Publication number
US1390233A
US1390233A US389461A US38946120A US1390233A US 1390233 A US1390233 A US 1390233A US 389461 A US389461 A US 389461A US 38946120 A US38946120 A US 38946120A US 1390233 A US1390233 A US 1390233A
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specific gravity
particles
liquids
flash
liquid
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US389461A
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Lindon W Bates
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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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/322Coal-oil suspensions

Definitions

  • nnrnon or rncnnasme ran srncrrrc enavrrr Ann mass-norm or mourns.
  • This application is a division of my copending applicationSerial Number 336,918, filed November 6th, 1919. It refers to a process for increasingthe safety of a liquid fuel against fire by raising its specific gravity so that it will support a waterseal or layer and by raising its flash point, in some cases above the preheat temperature necessary for proper atomization.
  • the process consists in combining with one or more liquid hydrocarbons particles of artificially pulverized solid carbonaceous substance in such amount as will raise the specific gravity of the composite above unity and in such a fashion as will elevate the flash point and stabilize the particles in the liquid.
  • the flash point of liquid combustibles varies within wide limits. It is frequently lower than 180 F. On the other hand the requisite preheat to atomize may exceed even 200 F. in the case of liquids of high viscosity.
  • the amount of carbonaceous substance used to elevate the specific gravity has also a perceptible efi'ect upon the dash point when the mixture is duly made, as hereinafter described.
  • Tn order to facilitate the stabilization of the coals in oil or tar or both, it is desirable to reduce the solid carbons to the form of particles by artificial means such as mechanical pulveriza-tion, or electrical or/chemical reduction.
  • the size should be such that about 85% of the particles would pass a- EZOO-mesh screen.
  • the treatment to obtain C. and 95 stability presented in this divisional application involves the peptization of the partlcles.
  • Certain liquid or liquefiable coal products are usable to peptize coal particles in oil or other liquid hydrocarbon. F or example, one may mention coal tar, creosote, naphthalene, solvent naphtha tar and partlally or completely dehydrated water gas tar.
  • distillate From 5% to 20% distillate will produce adequate stability under proper .conditions of application. These substances are not equally effective. Some are active peptizers and in others the quality is so to spealz latent, to be brought out by heat or time in storage to render the substance operative on the particles.
  • the carbonaceous substance should be pulverized in liquid hydrocarbon. It is possible however to obtain the desired results by blending with the liquids already pulverized material.
  • the heat treatment to induce peptization or to a-ccel crate it consists in heating the composite for over and hour at a temperature between G, more or less. Proper heat treatment may take a. considerable time, up to about three hours, when certain tars are used whose peptizing qualities are less active than those of other liquids or when anthracite coal is employed which is more diflicult than bituminous to peptize.
  • peptizing is meant partial dissolving of the particles by the peptizer and to some extent spongifymg, pitting and cavitating the individual particles, thereby promoting stability. H the particles are over peptized a less stable product may be formed. Stability is obtained by such action upon the particles and not by modify.
  • duration and degree of stability may bev as upon peptiza'tion the liquids enter into pores and seams of the coal.
  • Absorption, occlusion and adsorption may account for the phenomenon, and the volatiles in the oil may have a preferential aflinity for coal, which is brought into operative play in a suitably homogenized composite.
  • An ordinary mixture of coal and oil would not display so much higher a flash point than that of the original oil as the fuel herein described.
  • That method of raising the specific gravity and flash point of liquid hydrocarbon so that a fluid composite is formed which will support a layer of water and will atomize at a temperature below its flash point which consists in adding solid carbonaceous particles. to liquid hydrocarbon in an amount which will give the mixture a specific gravity heavier than that of water and a flash point above the temperature of preheat necessary for proper atomization. uniting therewith coal distillate having qualities which will peptize the particles and stabilize them, and peptizing therein the particles to form a stable liquid fuel of such elevated flash point and gravity.
  • That method of causing a composite fluid comprising a liquid hydrocarbon to sink in water instead of floating thereupon which consists in raising the specific gravity of the hydrocarbon above that of water by combining therewith pulverized solid carbonaceous substance in an amount which will raise the specific gravity above unity, and in maintaining the particles in dispersed and suspended condition throughout the liquid by peptizing them therein with partially or completely dehydrated water gas tar.
  • That method of raising the specific gravity and flash point of liquid hydrocarbon which consists in converting the same into av fluid composite containing solid carbonaceous substance and coal distillate having peptizing qualities upon such substance, pulverizing the carbonaceous substance in the liquid'hydrocarbon in the presence of the coal distillate and applying heat thereto until the solid substance is reduced so that about 85% would pass a QOO-mesh screen and the particles are peptized and stabilized and the flash point and gravity are elevated.

Description

. stares rArsNroi-"Fic LINDON W BATES, 01E MOUNT LEBANON, NEW YUBK. I
nnrnon or rncnnasme ran srncrrrc enavrrr Ann mass-norm or mourns.
aaaeaa.
Specification of Letters Patent.
Patented Sept. c, rear.
Ito Drawing. Original application filed November 6, 1919, Serial No. 336,918. Divided and this application filed June 16, 1920. Serial No. 389,461.
To all whom it may concern:
Be it known that T, LINnoN W. BATES, a citizen of the United States, residing at Mount Lebanon, in the county of Columbia and State of New York, have invented certain new and useful Improvements in Methods of Increasing the Specific Gravity and Flash-Point of Liquids, of which the following is a specification.
This application is a division of my copending applicationSerial Number 336,918, filed November 6th, 1919. Itrefers to a process for increasingthe safety of a liquid fuel against fire by raising its specific gravity so that it will support a waterseal or layer and by raising its flash point, in some cases above the preheat temperature necessary for proper atomization. The process consists in combining with one or more liquid hydrocarbons particles of artificially pulverized solid carbonaceous substance in such amount as will raise the specific gravity of the composite above unity and in such a fashion as will elevate the flash point and stabilize the particles in the liquid.
Most liquid fuels, such as oils and tars, have a specific gravity between about .85 and .98, although the gravity of certain tars exceeds unity. The gravity of coals lies between about 1.2 and 1.6. In order to raise the specific gravity of the oils and tars lighter than water, it is necessary to add thereto amounts of coal between about 10% and 35% by weight, depending upon the gravity of the liquid base. Anthracite, b1- tuminous and lignite coals are usable for this purpose.
The flash point of liquid combustibles varies within wide limits. It is frequently lower than 180 F. On the other hand the requisite preheat to atomize may exceed even 200 F. in the case of liquids of high viscosity. The amount of carbonaceous substance used to elevate the specific gravity has also a perceptible efi'ect upon the dash point when the mixture is duly made, as hereinafter described.
Tn order to facilitate the stabilization of the coals in oil or tar or both, it is desirable to reduce the solid carbons to the form of particles by artificial means such as mechanical pulveriza-tion, or electrical or/chemical reduction. The size should be such that about 85% of the particles would pass a- EZOO-mesh screen. The treatment to obtain C. and 95 stability presented in this divisional application involves the peptization of the partlcles. Certain liquid or liquefiable coal products are usable to peptize coal particles in oil or other liquid hydrocarbon. F or example, one may mention coal tar, creosote, naphthalene, solvent naphtha tar and partlally or completely dehydrated water gas tar. From 5% to 20% distillate will produce adequate stability under proper .conditions of application. These substances are not equally effective. Some are active peptizers and in others the quality is so to spealz latent, to be brought out by heat or time in storage to render the substance operative on the particles.
In order to obtain a homogeneous mixture and to elevate the flash point as much as possible or desired, the carbonaceous substance should be pulverized in liquid hydrocarbon. It is possible however to obtain the desired results by blending with the liquids already pulverized material. The heat treatment to induce peptization or to a-ccel crate it consists in heating the composite for over and hour at a temperature between G, more or less. Proper heat treatment may take a. considerable time, up to about three hours, when certain tars are used whose peptizing qualities are less active than those of other liquids or when anthracite coal is employed which is more diflicult than bituminous to peptize.
By peptizing is meant partial dissolving of the particles by the peptizer and to some extent spongifymg, pitting and cavitating the individual particles, thereby promoting stability. H the particles are over peptized a less stable product may be formed. Stability is obtained by such action upon the particles and not by modify.
mg the nature of the dispersion medium.-
No principal or chief reliance is placed upon increasing the viscosity of the medium to obtain stability. A product of low or by weight of a coal lltl congest the pipe system or prevent the use of the fuel in ordinary liquid fuel installations. During the period of adequate stability the liquid and particles do not separate to a disadvantageous extent. During the period of life the components form a composite whose specific gravity remains practically and sufficiently uniform and whose flash point remains elevated. The
duration and degree of stability may bev as upon peptiza'tion the liquids enter into pores and seams of the coal. Absorption, occlusion and adsorption may account for the phenomenon, and the volatiles in the oil may have a preferential aflinity for coal, which is brought into operative play in a suitably homogenized composite. An ordinary mixture of coal and oil would not display so much higher a flash point than that of the original oil as the fuel herein described.
Having thus presented my invention, what I claim in this divisional case is: V
1. That method of raising the specific gravity and flash point of liquid hydrocarbon so that a fluid composite is formed which will support a layer of water and will atomize at a temperature below its flash point, which consists in adding solid carbonaceous particles. to liquid hydrocarbon in an amount which will give the mixture a specific gravity heavier than that of water and a flash point above the temperature of preheat necessary for proper atomization. uniting therewith coal distillate having qualities which will peptize the particles and stabilize them, and peptizing therein the particles to form a stable liquid fuel of such elevated flash point and gravity.
2. That method of causing a composite fluid comprising a liquid hydrocarbon to sink in water instead of floating thereupon, which consists in raising the specific gravity of the hydrocarbon above that of water by combining therewith pulverized solid carbonaceous substance in an amount which will raise the specific gravity above unity, and in maintaining the particles in dispersed and suspended condition throughout the liquid by peptizing them therein with partially or completely dehydrated water gas tar. v
3. That method of raising the specific gravity and flash point of liquid hydrocarbon, which consists in converting the same into av fluid composite containing solid carbonaceous substance and coal distillate having peptizing qualities upon such substance, pulverizing the carbonaceous substance in the liquid'hydrocarbon in the presence of the coal distillate and applying heat thereto until the solid substance is reduced so that about 85% would pass a QOO-mesh screen and the particles are peptized and stabilized and the flash point and gravity are elevated.
In testimony whereof I have signed my name to this specification.
LINDON W. BATES.
US389461A 1919-11-10 1920-06-16 Method of increasing the specific gravity and flash-point of liquids Expired - Lifetime US1390233A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4121995A (en) * 1976-10-07 1978-10-24 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Surfactant-assisted liquefaction of particulate carbonaceous substances
US4153421A (en) * 1976-05-17 1979-05-08 Interlake, Inc. Stabilized fuel slurry

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4153421A (en) * 1976-05-17 1979-05-08 Interlake, Inc. Stabilized fuel slurry
US4121995A (en) * 1976-10-07 1978-10-24 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Surfactant-assisted liquefaction of particulate carbonaceous substances

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