US2128913A - Coal handling - Google Patents

Coal handling Download PDF

Info

Publication number
US2128913A
US2128913A US62135A US6213536A US2128913A US 2128913 A US2128913 A US 2128913A US 62135 A US62135 A US 62135A US 6213536 A US6213536 A US 6213536A US 2128913 A US2128913 A US 2128913A
Authority
US
United States
Prior art keywords
coal
water
suspension
oil
instance
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US62135A
Inventor
Robert E Burk
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Co
Original Assignee
Standard Oil Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Standard Oil Co filed Critical Standard Oil Co
Priority to US62135A priority Critical patent/US2128913A/en
Application granted granted Critical
Publication of US2128913A publication Critical patent/US2128913A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/30Conveying materials in bulk through pipes or tubes by liquid pressure

Definitions

  • the coal, bituminous or anthracite, etc. is, in accordance with the invention, finely divided or ground. This can be done at a convenient location, for instance at or near the mine.
  • the disas integrated coal is mixed with a carrier liquid, and with suitable conditions therefor, as more particularly hereinafter detailed, is then handled as a liquid, asby being pumped through a pipe line, or transported in tanks, etc.
  • a. combustible liquid as carrier such for instance as a petroleum liquid, more conveniently a cheap fraction thereof, the entire material may be directly amenable to combustion usage as such.
  • gas oil, fluent residuums, etc. may be so applied.
  • I employ an aqueous liquid as carrier, this making possible certain features not applicable otherwise.
  • a means for maintaining the suspension safely under all conditions is preferable, and for this I incorpo- 45 rate a small amount of a stabilizing agent, such as a soap of a base of sodium, potassium, ammonium, ethanolamine, etc., with an acid radical, as for instance oleic, palmitic, stearic, lauric,
  • the amount of stabilizing agent in general may bev quite small, as for instance 0.005 to 0.5 per cent or more, amounts above 1 per cent being in general unnecessary or waste.
  • the finely divided coal in amount such as ii to form slurries of pumpable limits, as for in- To the accomplishment of the foregoing and stance 5 to 50 per cent, and the stabilizing agent thus in suspension form, such liquid is capable of indefinite handling and transportation, as indicated, and may be transported from point of preparation, as for instance the mine, through long distance pipe lines to point of usage, as desired.
  • air may be mixed with the coal and water before transportation, and pine oil or cresylic acid or the like, and additionally if preferred xanthates or thiocarbanilide or the like, 1 in amounts from 0.003 per cent upward.
  • xanthates or thiocarbanilide or the like 1 in amounts from 0.003 per cent upward.
  • the product may of course be directly fed to a furnace in suitable atomizing burners, or may be applied for utilization of the carbonaceous material otherwise as desired.
  • the carrier liquid is aqueous, it is then more 20 feasible to effect a separation for usage.
  • the stable suspension may be broken, as by admixture of an electrolyte to neutralize ionic adsorption charges on the coal particles, or where the stabilizer is a water-soluble snap, the coagulating agent may be such as to precipitate an insoluble form of soap therefrom.
  • convenient coagulating agents may be aluminum sulphate,
  • the amount of coagulating agent is in general such as to neutralize or precipitate as required, and may be for instance 0.00001 mol. per cent to any economic high concentration.
  • coagulating agent 8,150,111 some instances preferable to the foregoing, Imay employ a small amount of oil, this being admixed with the suspension where an aqueous liquid is used, and the oil will then selectively wet the coal andqdlsplace its surface-action relative to the water, and cause separation from the water.
  • Ash a small amount of oil
  • oil suitable for this are small, as for instance 0.005 per cent to quantities suflicient to form a second layer of oil containing powdered coal.
  • the oil for such purpose may advantageously be a cheap form of petroleum, as for instance gas oil, residuum, etc. When larger amounts of oil are employed mixtures of directly combustible character may be so obtained.
  • the solid coal With the stable suspension broken, as at the' point of usage, and the coal separated, as by settlingor skimming or flotation, by bubble flotation using traces of cresylic acid, pine oil, or like agents, the solid coal may be separated or flltered conveniently, and the water having been eliminated, by suitable means the coal may be employed directly for firing, or it may be formed into compressed blocks as better suited for some furnace usages.
  • a process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble soap, pumping a stream of such suspension to point of use, admixing lime and collecting the coal separated.
  • a process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of an easily precipitated suspending agent, pumping a stream of such suspension to point of use, and coagulating the suspending agent to recover the coal.
  • a process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble soap, pumping a stream of such suspension to point of use, and precipitating the soap to collect the coal.
  • a process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and suspending the disintegrated coal in an aqueous carrier liquid with a small amount of a water-soluble soap, admixing air and pumping a stream of such suspension to point 01' use, and coagulating the soap to separate the coal.
  • a process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble dispersing agent having the precipitable characteristics of soap, pumping a stream of such suspension to point of use, and precipitating the dispersing agent and separating the coal from I the carrier water.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

Patented Sept. 6, 193a UNITED STATES COAL HANDLING RobertE. Burk, Cleveland, Ohio, assignor to The Standard Oil Company, Cleveland, Ohio, a corporation of Ohio No Drawing. Application February 3, 1936, Serial No. 62,135
6 Claims.
related ends, the invention, then,comprlses the features hereinafter fully described, and particularly pointed out in the claims, the following description setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
The coal, bituminous or anthracite, etc., is, in accordance with the invention, finely divided or ground. This can be done at a convenient location, for instance at or near the mine. The disas integrated coal is mixed with a carrier liquid, and with suitable conditions therefor, as more particularly hereinafter detailed, is then handled as a liquid, asby being pumped through a pipe line, or transported in tanks, etc. By em- 30 ploying a. combustible liquid as carrier, such for instance as a petroleum liquid, more conveniently a cheap fraction thereof, the entire material may be directly amenable to combustion usage as such. Thus, for instance gas oil, fluent residuums, etc., may be so applied. Preferably however, I employ an aqueous liquid as carrier, this making possible certain features not applicable otherwise. I
While, in some situations, the agitation of the finely divided coal in the carriermedium is such in the pumping and handling operations as to prevent serious separation or. settling, a means for maintaining the suspension safely under all conditions is preferable, and for this I incorpo- 45 rate a small amount of a stabilizing agent, such as a soap of a base of sodium, potassium, ammonium, ethanolamine, etc., with an acid radical, as for instance oleic, palmitic, stearic, lauric,
or acids obtained from the oxidation of petrole-' 50 um or paraflin, etc. The amount of stabilizing agent in general may bev quite small, as for instance 0.005 to 0.5 per cent or more, amounts above 1 per cent being in general unnecessary or waste. With the finely divided coal in amount such as ii to form slurries of pumpable limits, as for in- To the accomplishment of the foregoing and stance 5 to 50 per cent, and the stabilizing agent thus in suspension form, such liquid is capable of indefinite handling and transportation, as indicated, and may be transported from point of preparation, as for instance the mine, through long distance pipe lines to point of usage, as desired. If desired, air may be mixed with the coal and water before transportation, and pine oil or cresylic acid or the like, and additionally if preferred xanthates or thiocarbanilide or the like, 1 in amounts from 0.003 per cent upward. Such may be availed of in addition to or instead of the other stabilizers, as a buoyant effect is had from minute air bubbles engaging the coal par ticles. Where employing a combustible liquid as 1 carrier, the product may of course be directly fed to a furnace in suitable atomizing burners, or may be applied for utilization of the carbonaceous material otherwise as desired. Where the carrier liquid is aqueous, it is then more 20 feasible to effect a separation for usage. For this, the stable suspension may be broken, as by admixture of an electrolyte to neutralize ionic adsorption charges on the coal particles, or where the stabilizer is a water-soluble snap, the coagulating agent may be such as to precipitate an insoluble form of soap therefrom. Thus, convenient coagulating agents may be aluminum sulphate,
alum, lime, 'etc. The amount of coagulating agent is in general such as to neutralize or precipitate as required, and may be for instance 0.00001 mol. per cent to any economic high concentration. For coagulating agent 8,150,111 some instances preferable to the foregoing, Imay employ a small amount of oil, this being admixed with the suspension where an aqueous liquid is used, and the oil will then selectively wet the coal andqdlsplace its surface-action relative to the water, and cause separation from the water. Ash
in the coal is not wetted and sinks. Amounts of oil suitable for this are small, as for instance 0.005 per cent to quantities suflicient to form a second layer of oil containing powdered coal. The oil for such purpose may advantageously be a cheap form of petroleum, as for instance gas oil, residuum, etc. When larger amounts of oil are employed mixtures of directly combustible character may be so obtained.
With the stable suspension broken, as at the' point of usage, and the coal separated, as by settlingor skimming or flotation, by bubble flotation using traces of cresylic acid, pine oil, or like agents, the solid coal may be separated or flltered conveniently, and the water having been eliminated, by suitable means the coal may be employed directly for firing, or it may be formed into compressed blocks as better suited for some furnace usages.
Other modes of applying the principle of the invention may be employed, change being made as regards the details described, provided the features stated in any of the following claims, or the equivalent of such, be employed.
I therefore particularly point out and distinctly claim as my invention:-
1. A process of transporting coal, which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble soap, pumping a stream of such suspension to point of use, admixing lime and collecting the coal separated.
2. A process of transporting coal, which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of an easily precipitated suspending agent, pumping a stream of such suspension to point of use, and coagulating the suspending agent to recover the coal.
3. A process of transporting coal, which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble soap, pumping a stream of such suspension to point of use, and precipitating the soap to collect the coal.
4. A process of transporting coal, which comprises changing its state to a pumpable fluid by grinding the coal and suspending the disintegrated coal in an aqueous carrier liquid with a small amount of a water-soluble soap, admixing air and pumping a stream of such suspension to point 01' use, and coagulating the soap to separate the coal.
5. A process of transporting coal which comprises changing its state to a pumpable fluid by grinding the coal and mixing the disintegrated coal with water and a small amount of a watersoluble dispersing agent having the precipitable characteristics of soap, pumping a stream of such suspension to point of use, and precipitating the dispersing agent and separating the coal from I the carrier water.
6. The process set forth in claim 5 in which air is used'additionally as a stabilizing agent.
ROBERT E. BURK.
US62135A 1936-02-03 1936-02-03 Coal handling Expired - Lifetime US2128913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US62135A US2128913A (en) 1936-02-03 1936-02-03 Coal handling

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US62135A US2128913A (en) 1936-02-03 1936-02-03 Coal handling

Publications (1)

Publication Number Publication Date
US2128913A true US2128913A (en) 1938-09-06

Family

ID=22040427

Family Applications (1)

Application Number Title Priority Date Filing Date
US62135A Expired - Lifetime US2128913A (en) 1936-02-03 1936-02-03 Coal handling

Country Status (1)

Country Link
US (1) US2128913A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2421968A (en) * 1941-08-30 1947-06-10 Lummus Co Method of conveying fluids
US2610901A (en) * 1948-02-13 1952-09-16 Kansas City Testing Lab Pipeline transportation of solid materials
US2610900A (en) * 1948-02-13 1952-09-16 Kansas City Testing Lab Pipeline transportation of solid materials and petroleum products
US2686085A (en) * 1950-07-15 1954-08-10 William W Odell Method of conveying or transporting small-size solids
US2835536A (en) * 1952-09-18 1958-05-20 Lorraine Houilleres Plant for conveying granular or solid products, notably coal sludges, through hydraulic means
US2894788A (en) * 1956-10-22 1959-07-14 Nat Distillers Chem Corp Handling of sodium dispersions
US3180691A (en) * 1959-10-15 1965-04-27 Ruhrgas Ag Method of transporting solid and viscous material in pipe lines
US3206256A (en) * 1963-07-15 1965-09-14 Shell Oil Co Transportation of dispersed solid particles in pipe lines
US3210168A (en) * 1962-05-22 1965-10-05 Exxon Research Engineering Co Stabilized oiled coal slurry in water
US3264038A (en) * 1964-07-08 1966-08-02 Continental Oil Co Process for transporting solids in pipelines
US3268263A (en) * 1963-11-18 1966-08-23 Shell Oil Co Inhibiting settling of solid particles through a liquid
US3302977A (en) * 1964-11-19 1967-02-07 Continental Oil Co Method for simultaneously transporting liquids and solids through a common pipeline
US3432209A (en) * 1965-11-04 1969-03-11 Shell Oil Co Transport of solids with petroleum in pipelines
US3865547A (en) * 1971-07-28 1975-02-11 Shell Oil Co Preventing corrosion during the pipeline transportation of coal slurries
DE2629797A1 (en) * 1975-07-03 1977-01-27 American Minechem Corp PROCEDURE FOR CONVEYING OR TRANSPORTING COAL
US4265737A (en) * 1974-01-14 1981-05-05 Otisca Industries, Ltd. Methods and apparatus for transporting and processing solids
US4398919A (en) * 1981-11-04 1983-08-16 Akzona Incorporated Polyethoxylated compounds as coal-water slurry surfactants
US5380342A (en) * 1990-11-01 1995-01-10 Pennsylvania Electric Company Method for continuously co-firing pulverized coal and a coal-water slurry
US5513583A (en) * 1994-10-27 1996-05-07 Battista; Joseph J. Coal water slurry burner assembly

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2421968A (en) * 1941-08-30 1947-06-10 Lummus Co Method of conveying fluids
US2610901A (en) * 1948-02-13 1952-09-16 Kansas City Testing Lab Pipeline transportation of solid materials
US2610900A (en) * 1948-02-13 1952-09-16 Kansas City Testing Lab Pipeline transportation of solid materials and petroleum products
US2686085A (en) * 1950-07-15 1954-08-10 William W Odell Method of conveying or transporting small-size solids
US2835536A (en) * 1952-09-18 1958-05-20 Lorraine Houilleres Plant for conveying granular or solid products, notably coal sludges, through hydraulic means
US2894788A (en) * 1956-10-22 1959-07-14 Nat Distillers Chem Corp Handling of sodium dispersions
US3180691A (en) * 1959-10-15 1965-04-27 Ruhrgas Ag Method of transporting solid and viscous material in pipe lines
US3210168A (en) * 1962-05-22 1965-10-05 Exxon Research Engineering Co Stabilized oiled coal slurry in water
US3206256A (en) * 1963-07-15 1965-09-14 Shell Oil Co Transportation of dispersed solid particles in pipe lines
US3268263A (en) * 1963-11-18 1966-08-23 Shell Oil Co Inhibiting settling of solid particles through a liquid
US3264038A (en) * 1964-07-08 1966-08-02 Continental Oil Co Process for transporting solids in pipelines
US3302977A (en) * 1964-11-19 1967-02-07 Continental Oil Co Method for simultaneously transporting liquids and solids through a common pipeline
US3432209A (en) * 1965-11-04 1969-03-11 Shell Oil Co Transport of solids with petroleum in pipelines
US3865547A (en) * 1971-07-28 1975-02-11 Shell Oil Co Preventing corrosion during the pipeline transportation of coal slurries
US4265737A (en) * 1974-01-14 1981-05-05 Otisca Industries, Ltd. Methods and apparatus for transporting and processing solids
DE2629797A1 (en) * 1975-07-03 1977-01-27 American Minechem Corp PROCEDURE FOR CONVEYING OR TRANSPORTING COAL
US4398919A (en) * 1981-11-04 1983-08-16 Akzona Incorporated Polyethoxylated compounds as coal-water slurry surfactants
US5380342A (en) * 1990-11-01 1995-01-10 Pennsylvania Electric Company Method for continuously co-firing pulverized coal and a coal-water slurry
US5513583A (en) * 1994-10-27 1996-05-07 Battista; Joseph J. Coal water slurry burner assembly

Similar Documents

Publication Publication Date Title
US2128913A (en) Coal handling
Castro et al. Review of the flotation of molybdenite. Part I: Surface properties and floatability
Laskowski et al. Oil agglomeration and its effect on beneficiation and filtration of low-rank/oxidized coals
US2346151A (en) Process of treating coal
Jaiswal et al. An overview of reverse flotation process for coal
Song et al. Effects of nonpolar oil on hydrophobic flocculation of hematite and rhodochrosite fines
NO840050L (en) DIFFICULT SUSPENSION OF A SOLID FUEL AND A PROCEDURE FOR PRODUCING THEREOF
AU2017314935B2 (en) Sulfonated modifiers for froth flotation
Song et al. Hydrophobic flocculation of sphalerite fines in aqueous suspensions induced by ethyl and amyl xanthates
CN103934113B (en) Beneficiation method for tungsten polymetallic ore
US4062694A (en) Stable particulate suspensions
Sadowski et al. Agglomerate flotation of fine oxide particles
US3919080A (en) Pyrite depression in coal flotation by the addition of sodium sulfite
CN108187917A (en) A kind of aromatic radical phosphonic acids and its esters collecting agent and its application
NL6507491A (en)
AU648649B2 (en) Froth flotation of fine particles
US2410376A (en) Beneficiation of iron ores
US2934208A (en) Silicone reagent flotation
Labuschagne Relationships between oil agglomeration and surface properties of coal: Effect of pH and oil composition
Yang et al. Oil agglomeration of coal in inorganic salt solutions
US3458044A (en) Treatment of coal and other minerals
Ding et al. Coal reverse flotation. Part II: Cleaning of a subbituminous coal
CN105344485B (en) The method for reclaiming gold and its intergrowth from difficult-treating gold mine based on sulphur oil aggregative flotation
Ding et al. Application of a modified water glass in a cationic flotation of calcite and dolomite
Ciftci et al. Settling characteristics of coal preparation plant fine tailings using anionic polymers