US2567136A - Agglomerates of fuel and manufacture process - Google Patents

Agglomerates of fuel and manufacture process Download PDF

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Publication number
US2567136A
US2567136A US700389A US70038946A US2567136A US 2567136 A US2567136 A US 2567136A US 700389 A US700389 A US 700389A US 70038946 A US70038946 A US 70038946A US 2567136 A US2567136 A US 2567136A
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less
suitable amount
agglomerates
fuel
manufacture process
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US700389A
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Vloeberghs Antoine
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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

Definitions

  • a synthetic resin will vbe used as polymerizable product, for instance a condensation product of phenol and formaldehyde.
  • the synthetic resin and the sulphite liquor can be introduced either separately, or as a compound previously formed by the mixture of the two cements. Thereafter, the solid fuel as finely divided, mixed with its binder and submitted to an appropriate mechanical action, in order to be briquetted in the shape of agglomerates of pre-determined sizes. In order to assure a quicker hardening of the agglomerates, these will preferably go through a drying-oven in which will be maintained a temperature equal or slightl superior to 100 C.
  • a fuel agglomerate comprising coal dust, a suitable amount of waste sulphite liquor up to less than 6%, and a suitable amount of a phenolformaldehyde resin up to less than 3%.
  • a fuel agglomerate comprising finely divided anthracite, a suitable amount of waste sulphite liquor up to less than 6%, and a suitable amount 2 of a phenol-formaldehyde resin up to less than 3%.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

Patented Sept. 4, 1951 AGGLOMERATES OF FUEL AND MANUFACTURE PROCESS Antoine Vloeberghs, Antwerp, Belgium No Drawing. Application October 1, 1946, Serial N 0. 700,389. In Belgium September 22, 1939 6 Claims.
In my patent application Serial No. 700,391, now abandoned, there has been disclosed the means to manufacture fuel agglomerates by applying two distinct cements, of which one respectively is capable to give to the mass a good resistance during the whole duration of the combustion and the other is capable of giving to the mass a sufficient water-proofness, so that it may be kept in the open air which is necessary for a normal and prolonged stocking.
According to the present improvements, one substitutes for the sulfate liquor commended in the principal patent, a certain quantity of a polymerizable product, so that the latter brings about a cement capable of giving to the mass its water-proofness. Preferably, a synthetic resin will vbe used as polymerizable product, for instance a condensation product of phenol and formaldehyde.
From the tests made by the inventor, it results that the agglomerates of finely divided anthracite to which are added less than 6% of waste sulphite liquor from the manufacture of the cellulose and less than 3% of synthetic resin, resist perfectly to all operations to which coal is generally submitted and resists even a prolonged immersion in boiling water.
The synthetic resin and the sulphite liquor can be introduced either separately, or as a compound previously formed by the mixture of the two cements. Thereafter, the solid fuel as finely divided, mixed with its binder and submitted to an appropriate mechanical action, in order to be briquetted in the shape of agglomerates of pre-determined sizes. In order to assure a quicker hardening of the agglomerates, these will preferably go through a drying-oven in which will be maintained a temperature equal or slightl superior to 100 C.
What I claim is:
1. A fuel agglomerate comprising coal dust, a suitable amount of waste sulphite liquor up to less than 6%, and a suitable amount of a phenolformaldehyde resin up to less than 3%.
2. A fuel agglomerate comprising finely divided anthracite, a suitable amount of waste sulphite liquor up to less than 6%, and a suitable amount 2 of a phenol-formaldehyde resin up to less than 3%.
3. In a process for manufacturing coal briquettes, the steps of adding to coal dust a, suitable amount, up to less than 6%, of waste sulphite liquor for binding the particles of said coal dust and a suitable amount, up to less than 3% of a phenol-formaldehyde resin for waterproofing the resultant mixture, moulding said mixture and drying the same by heat.
4. In a process for manufacturing coal briquettes and the like, the steps of adding to finely divided anthracite a suitable amount, up to less than 6%, of waste sulphite liquor for binding the particles of said anthracite, and a suitable amount, up to less than 3%, of a phenolformaldehyde resin for waterproofing the resultant mixture, moulding said mixture and subjecting the same to heat.
5. In a process for manufacturing coal briquettes and the like, the steps of adding to coal dust a suitable amount, up to less than 6%, of waste sulphite liquor for binding the particles of said coal dust, and a suitable amount, up to less than 3%, of a phenol-formaldehyde resin for waterproofing the resultant mixture, moulding said mixture and subjecting said moulded mixture to a temperature of about C.
6. In a process for manufacturing coal briquettes, the steps of adding to coal dust the following previously prepared mixture: a suitable amount, up to less than 6% of waste sulphite liquor and a suitable amount, up to less than 3% of phenol-formaldehyde resin; moulding the resultant agglomerate and subjecting the same to a temperature of about 100 C. in an oven.
ANTOINE VLOEBERGHS.
REFERENCES CITED The following references are of record in the file of this patent:
FOREIGN PATENTS Number Country Date 476,344 Great Britain Dec. '7, 1937 657,930 Germany Mar. 17, 1938

Claims (1)

1. A FUEL AGGLOMERATE COMPRISING COAL DUST, A SUITABLE AMOUNT OF WASTE SULPHITE LIQUOR UP TO LESS THAN 6%, AND A SUITABLE AMOUNT OF A PHENOLFORMALDEHYDE RESIN UP TO LESS THAN 3%.
US700389A 1939-09-22 1946-10-01 Agglomerates of fuel and manufacture process Expired - Lifetime US2567136A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
BE2567136X 1939-09-22

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US2567136A true US2567136A (en) 1951-09-04

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4230459A (en) * 1978-09-20 1980-10-28 Moreau Jean R Process for agglomerating particulate wood material and products obtained thereby
US4260423A (en) * 1980-02-25 1981-04-07 Fmc Corporation Kiln tar binder and method of producing it
US4758244A (en) * 1983-02-17 1988-07-19 University Of Melbourne Upgrading solid fuels
US4802890A (en) * 1986-04-08 1989-02-07 Fosroc International Limited Agglomeration of coal fines
US5244473A (en) * 1992-01-22 1993-09-14 Sardessai Kashinath S Process for making moisture resistant briquettes
US5743924A (en) * 1995-03-03 1998-04-28 Cq, Inc. Pelletized fuel composition and method of manufacture

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB476344A (en) * 1935-06-29 1937-12-07 Mead Corp Improvements in or relating to non-cellulosic material obtained from spent digestionliquor
DE657930C (en) * 1934-10-14 1938-03-17 Johanna Petersen Geb Wichulla A binding agent consisting of a resin solution

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE657930C (en) * 1934-10-14 1938-03-17 Johanna Petersen Geb Wichulla A binding agent consisting of a resin solution
GB476344A (en) * 1935-06-29 1937-12-07 Mead Corp Improvements in or relating to non-cellulosic material obtained from spent digestionliquor

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4230459A (en) * 1978-09-20 1980-10-28 Moreau Jean R Process for agglomerating particulate wood material and products obtained thereby
US4260423A (en) * 1980-02-25 1981-04-07 Fmc Corporation Kiln tar binder and method of producing it
US4758244A (en) * 1983-02-17 1988-07-19 University Of Melbourne Upgrading solid fuels
US4802890A (en) * 1986-04-08 1989-02-07 Fosroc International Limited Agglomeration of coal fines
US5244473A (en) * 1992-01-22 1993-09-14 Sardessai Kashinath S Process for making moisture resistant briquettes
US5743924A (en) * 1995-03-03 1998-04-28 Cq, Inc. Pelletized fuel composition and method of manufacture
WO1998028384A1 (en) * 1996-12-20 1998-07-02 Duquesne Energy, Inc. Pelletized fuel composition and method of manufacture

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