EP0377995A2 - Briquetting process - Google Patents

Briquetting process Download PDF

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Publication number
EP0377995A2
EP0377995A2 EP89313406A EP89313406A EP0377995A2 EP 0377995 A2 EP0377995 A2 EP 0377995A2 EP 89313406 A EP89313406 A EP 89313406A EP 89313406 A EP89313406 A EP 89313406A EP 0377995 A2 EP0377995 A2 EP 0377995A2
Authority
EP
European Patent Office
Prior art keywords
mix
coal
process according
binder
magnesium oxide
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.)
Withdrawn
Application number
EP89313406A
Other languages
German (de)
French (fr)
Other versions
EP0377995A3 (en
Inventor
Stuart Hale
Simon Kelly
Rodney Taylor
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.)
Coal Industry Patents Ltd
Original Assignee
Coal Industry Patents Ltd
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 Coal Industry Patents Ltd filed Critical Coal Industry Patents Ltd
Publication of EP0377995A2 publication Critical patent/EP0377995A2/en
Publication of EP0377995A3 publication Critical patent/EP0377995A3/en
Withdrawn legal-status Critical Current

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Classifications

    • 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

Definitions

  • the present invention concerns a briquetting process. More especially it concerns such a process which gives improved cure rate and green strength in "cold" briquetting, that is briquetting at temperatures of up to 100°C.
  • magnesium oxide accelerates the rate of cure. Magnesium oxide has been found, in particular, to impart a significant improvement to the green shatter resistance of molasses/phosphoric acid bound briquettes.
  • the present invention provides a process for the cold briquetting of fine coal, comprising mixing fine coal with a binder utilising phosphoric acid to produce a water-containing briquetting mix, and characterised by the presence in the briquetting mix, preferably in an amount of up to 2% by weight of the mix of magnesium oxide, and briquetting the mix, whereby the green shatter strength, the hot crushing strength of the resulting briquettes during curing and/or the water resistance of the cured briquettes are improved.
  • the binder is a combination of molasses and optionally an organic hardening agent, or a sugar solution, together with phosphoric acid and we refer to our prior applications mentioned above for examples of such binders.
  • Molasses/phosphoric acid binder is particularly preferred.
  • Preferred coals are high rank non-caking coals, especially those having low smoke emissions such as anthracite.
  • the coal is of a particular size mainly below 3mm, and anthracite duff is especially suitable.
  • the invention is also applicable to coals for power stations or steam raising and to coal blends containing coking coal components and/or treated coals, e.g. by mild oxidation or pyrolysis.
  • the coal may be crushed or be the direct product of coal cutting.
  • the briquetting step of the present invention includes all methods of forming agglomerates from fine coal, and these agglomerates may be of any size or shape according to market requirements. There may be mentioned forming agglomerates by extrusion, ringroll or roll-pressing, die-pressing, rotary table pressing and pelletising, e.g. on a disc pelletiser.
  • the hardening (curing) stage in the briquetting process is preferably carried out at temperature of the order of 200 o C to 300 o C for up to an hour.
  • Hot curing may be conveniently carried out by passing the briquettes on a conveyor through an oven, in an atmosphere which may contain nitrogen, carbon dioxide, water vapour and/or oxygen.
  • Anthracite duff (88 parts, - 1.7mm particle size) was mixed with iron ore (1 part) and binder (11 parts) by weight.
  • the binder was a mixture providing molasses (10 parts) and phosphoric acid (1 part).
  • the mixture was briquetted in a pilot plant roll press, and the briquettes produced were tested for green crushing strength, green shatter resistance, hot crushing strength (at 250oC) and water resistance.
  • the properties of the control mix were compared with those of a similar mix containing 1% w/w of magnesium oxide additive.
  • the results shown in the attached table indicate a significant increase in the green shatter resistance and hot crushing strength of the briquettes and in their water resistance. Similar results were obtained whether the magnesium oxide additive was added before or after the binder.

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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)

Abstract

Fine coal is briquetted using a binder incorporating phosphoric acid e.g. molasses/phosphoric acid and up to 2% by weight of the mix of magnesium oxide. The briquettes show good initial green shatter resistance, improved hot crushing strength and/or water resistance.

Description

  • The present invention concerns a briquetting process. More especially it concerns such a process which gives improved cure rate and green strength in "cold" briquetting, that is briquetting at temperatures of up to 100°C.
  • Our U.K. Patent Number 2,187,754B discusses a variety of cold coal briquetting processes and discloses a useful process utilising a combination of molasses and inorganic hardening agent as binder. Our co-pending U.K. Published Patent application Number 2 209 763A discloses a variation of the process of GB 2,187,754B in its use of concentrated sugar solutions. The disclosures of both these applications are incorporated herein by reference.
  • A great many cold briquetting processes, in which a water-containing binder is used, while apparently producing satisfactory briquettes of adequate final strength and combustion characteristics, result in green briquettes of inadequate initial strength and water resistance. That is to say, the briquette, when emerging from the briquette forming step are easily broken. In practice on the industrial scale, further handling of the green briquettes and hot curing thereof can result in undesirably high breakages and loss of complete briquettes, requiring recycle of broken briquette pieces or the acceptance of less desirable and less valuable product.
  • It has now been discovered that the incorporation of minor quantities of magnesium oxide into a water-containing mixture of coal and binder, especially under the normal operating temperatures of industrial processing, yields worthwhile improvements in green shatter resistance, final curing strength and water resistance of the cured briquette combined with undiminished or only slightly diminished green crushing strength. Additionally, magnesium oxide accelerates the rate of cure. Magnesium oxide has been found, in particular, to impart a significant improvement to the green shatter resistance of molasses/phosphoric acid bound briquettes.
  • The present invention provides a process for the cold briquetting of fine coal, comprising mixing fine coal with a binder utilising phosphoric acid to produce a water-containing briquetting mix, and characterised by the presence in the briquetting mix, preferably in an amount of up to 2% by weight of the mix of magnesium oxide, and briquetting the mix, whereby the green shatter strength, the hot crushing strength of the resulting briquettes during curing and/or the water resistance of the cured briquettes are improved.
  • Desirably, the binder is a combination of molasses and optionally an organic hardening agent, or a sugar solution, together with phosphoric acid and we refer to our prior applications mentioned above for examples of such binders. Molasses/phosphoric acid binder is particularly preferred.
  • Preferred coals are high rank non-caking coals, especially those having low smoke emissions such as anthracite. Desirably the coal is of a particular size mainly below 3mm, and anthracite duff is especially suitable. The invention is also applicable to coals for power stations or steam raising and to coal blends containing coking coal components and/or treated coals, e.g. by mild oxidation or pyrolysis. The coal may be crushed or be the direct product of coal cutting.
  • The briquetting step of the present invention includes all methods of forming agglomerates from fine coal, and these agglomerates may be of any size or shape according to market requirements. There may be mentioned forming agglomerates by extrusion, ringroll or roll-pressing, die-pressing, rotary table pressing and pelletising, e.g. on a disc pelletiser.
  • The hardening (curing) stage in the briquetting process, to give the required strength and water resistance of the product, is preferably carried out at temperature of the order of 200oC to 300oC for up to an hour. Hot curing may be conveniently carried out by passing the briquettes on a conveyor through an oven, in an atmosphere which may contain nitrogen, carbon dioxide, water vapour and/or oxygen.
  • The present invention will now be described by way of example only.
  • Example 1
  • Anthracite duff (88 parts, - 1.7mm particle size) was mixed with iron ore (1 part) and binder (11 parts) by weight. The binder was a mixture providing molasses (10 parts) and phosphoric acid (1 part). The mixture was briquetted in a pilot plant roll press, and the briquettes produced were tested for green crushing strength, green shatter resistance, hot crushing strength (at 250oC) and water resistance. The properties of the control mix were compared with those of a similar mix containing 1% w/w of magnesium oxide additive. The results shown in the attached table indicate a significant increase in the green shatter resistance and hot crushing strength of the briquettes and in their water resistance. Similar results were obtained whether the magnesium oxide additive was added before or after the binder. TABLE
    Influence of Magnesium Oxide on the Green Strength and Cure Rate of Molasses/Phosphoric Acid Bound Briquettes
    ADDITIVE CONTROL 1% MAGNESIUM OXIDE
    10lb Green Shatter
    + 1 1/4 35 71
    + 7/8 42 78
    Green Crushing Strength (Kg) 3.7 3.5
    Hot Crushing Strength (Kg) (Curing Time - mins)
    5 2.5 4.1
    10 7.8 9.1
    15 21.1 47.3
    20 71.9 89.4
    25 92.2 129.2
    30 105.7 125.2
    24 hour Water Resistance (Kg) (Curing Time - mins)
    5 D D
    10 3.2 10.2
    15 27.0 68.6
    20 93.5 126.9
    25 109.0 141.9
    30 101.4 149.7

Claims (6)

1. A process for the cold briquetting of fine coal comprising mixing fine coal with a binder to produce a briguetting mix and briquetting the mix, characterised by the presence in the briquetting mix of magnesium oxide in an amount such that the green shatter strength, hot crushing strength and/or the water resistance of the resulting briquettes are improved.
2. A process according to claim 1 characterised in that the binder comprises molasses, a sugar solution and an inorganic hardening agent.
3. A process according to any claim 1 or 2 characterised in that the binder comprises molasses in an amount of from 5-15% by weight of the mix together with an acid and optionally, a hardening agent selected from iron oxide (or iron ore), calcium carbonate (or limestone), calcium phosphate (or phosphate rock) and aluminium oxide (or bauxile). 4. A process according to any preceding claim, characterised in that the magnesium oxide is mixed with dry coal before addition of the binder.
5. A process according to any of claims 1 to 3 characterised in that the magnesium oxide is mixed with the coal simultaneously with or after addition of the binder.
6. A process according to any preceding claim characterised in that the magnesium oxide is present in an amount of up to 2% by weight of the mix.
7. A process according to any preceding claim, characterised in that the coal is a high rank non-caking coal.
EP19890313406 1989-01-12 1989-12-21 Briquetting process Withdrawn EP0377995A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8900631 1989-01-12
GB8900631A GB2227023A (en) 1989-01-12 1989-01-12 Briquetting process

Publications (2)

Publication Number Publication Date
EP0377995A2 true EP0377995A2 (en) 1990-07-18
EP0377995A3 EP0377995A3 (en) 1990-09-05

Family

ID=10649920

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19890313406 Withdrawn EP0377995A3 (en) 1989-01-12 1989-12-21 Briquetting process

Country Status (3)

Country Link
EP (1) EP0377995A3 (en)
GB (1) GB2227023A (en)
ZA (1) ZA899782B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0566034A1 (en) * 1992-04-14 1993-10-20 SOPHIA-JACOBA GmbH Cold briquetted coal
WO2002050219A1 (en) * 2000-12-19 2002-06-27 Posco Coal briquette having superior strength and briquetting method thereof
WO2004020555A1 (en) * 2002-09-02 2004-03-11 Posco Coal briquettes for smelting reduction process, and method for manufacturing the same
US7129371B2 (en) * 2002-07-02 2006-10-31 Ferro Corporation Benzene phosphinic acid with improved flowability
US7566807B2 (en) 2006-09-14 2009-07-28 Novolyte Technologies Inc. Benzene phosphinic acid with improved flowability

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105296045A (en) * 2015-11-23 2016-02-03 广西金壮锦节能技术有限公司 High viscosity briquette waterproof composite binder

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2138442A (en) * 1983-04-23 1984-10-24 Akzo Nv Fuel briquettes
GB2187754A (en) * 1986-03-14 1987-09-16 Coal Ind Coal briquetting process
GB2209763A (en) * 1987-09-16 1989-05-24 Coal Ind Coal briquetting process

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4165221A (en) * 1978-10-24 1979-08-21 Ohio & Penna. Fuels, Inc. Formed carbon fuel briquettes, process for forming the same and process for utilizing the same in the manufacture of steel
SU1010146A1 (en) * 1981-07-06 1983-04-07 Московский Ордена Трудового Красного Знамени Горный Институт Method for making coal and ore briquets

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2138442A (en) * 1983-04-23 1984-10-24 Akzo Nv Fuel briquettes
GB2187754A (en) * 1986-03-14 1987-09-16 Coal Ind Coal briquetting process
GB2209763A (en) * 1987-09-16 1989-05-24 Coal Ind Coal briquetting process

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0566034A1 (en) * 1992-04-14 1993-10-20 SOPHIA-JACOBA GmbH Cold briquetted coal
WO2002050219A1 (en) * 2000-12-19 2002-06-27 Posco Coal briquette having superior strength and briquetting method thereof
CN1309844C (en) * 2000-12-19 2007-04-11 Posco公司 Coal briquette having superior strength and briquetting method thereof
US7129371B2 (en) * 2002-07-02 2006-10-31 Ferro Corporation Benzene phosphinic acid with improved flowability
WO2004020555A1 (en) * 2002-09-02 2004-03-11 Posco Coal briquettes for smelting reduction process, and method for manufacturing the same
CN1328358C (en) * 2002-09-02 2007-07-25 Posco公司 Coal briquettes for smelting reduction process, and method for manufacturing the same
US7566807B2 (en) 2006-09-14 2009-07-28 Novolyte Technologies Inc. Benzene phosphinic acid with improved flowability

Also Published As

Publication number Publication date
EP0377995A3 (en) 1990-09-05
ZA899782B (en) 1990-09-26
GB2227023A (en) 1990-07-18
GB8900631D0 (en) 1989-03-08

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