[go: up one dir, main page]

GB2223505A - Briquetting process - Google Patents

Briquetting process Download PDF

Info

Publication number
GB2223505A
GB2223505A GB8823444A GB8823444A GB2223505A GB 2223505 A GB2223505 A GB 2223505A GB 8823444 A GB8823444 A GB 8823444A GB 8823444 A GB8823444 A GB 8823444A GB 2223505 A GB2223505 A GB 2223505A
Authority
GB
United Kingdom
Prior art keywords
process according
coal
briquetting
mix
desiccant
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.)
Granted
Application number
GB8823444A
Other versions
GB2223505B (en
GB8823444D0 (en
Inventor
Rodney Taylor
Simon Kelly
Stuart Hale
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.)
University of Surrey
Original Assignee
University of Surrey
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 University of Surrey filed Critical University of Surrey
Priority to GB8823444A priority Critical patent/GB2223505B/en
Publication of GB8823444D0 publication Critical patent/GB8823444D0/en
Publication of GB2223505A publication Critical patent/GB2223505A/en
Application granted granted Critical
Publication of GB2223505B publication Critical patent/GB2223505B/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

Landscapes

  • 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 and up to 2% by weight of the mix of a dessicant or drying agent. The briquettes show an improved initial green strength and shatter index combined with a good final strength. Preferred desiccants are anhydrous calcium chloride and magnesium chloride.

Description

Briquetting Process The present invention concerns a briquetting process. More especially it concerns such a process which gives improved green strengths in "cold" briquetting, that is, briquetting at temperatures of up to 1000C.
Our UK published Patent Application No 2,187,754 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 application No. 8721757 discloses avariation of the process of GB 2,187,754 in its use of concentrated sugar solutions. The disclosures of both these applications are incorporated herein by reference.
We have found that a great many cold briquetting processes, in which a water-containing binder is used, while apparently producing satisfactory briquettes of adequate final strength, and even acceptable to good burning properties, result in green briquettes of inadequate initial strength. That is to say, the briquettes, when emerging from the briquette forming step, have a low crushing strength and are easily broken. In practice on the industrial scale, mechanical handling of the green briquettes results 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.
Our British Patent Application No. 8725252 describes a process for cold briquetting a mixture of fine coal with a binder wherein the briquetting mix contains up to 2% by weight of the mix of a cement.
Although initial green strength of the briquettes is improved particularly at elevated temperatures in some instances the necessary level of cement addition results in a reduced final cured strength and impaired combustion characteristics.
It has now been discovered that the incorporation of minor quantities of a desiccant or drying agent into a water-containing mixture of coal and binder yields worthwhile improvements in initial green strength.
Magnesium or calcium chlorides, in particular, have been found to increase green strength without reducing final cured strength and in some instances where a subsequent drying or curing operation is involved to also increase the rate at which the briquettes develop strength.
The present invention provides a process for the cold briquetting of fine coal, comprising mixing fine coal with a binder 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 a desiccant, and briquetting the mix whereby the initial green strength of the resulting briquettes is improved, as also may be the rate at which crushing strength develops.
Although the process is nominally "cold", it is found that on the industrial scale the mix enters and leaves the briquette formation steps at a temperature above ambient, for example of the order of 60or. For example, it may be necessary to dry the fine coal by heating, before briquetting, and this mix retains sensible heat, or, depending upon the briquette formation step, friction and/or compression may give rise to heating of the briquette during formation. It has been found that the present invention is applicable with regard to initial green strength at both ambient and elevated briquetting temperatures.
Desirably, the binder is a combination of molasses or a sugar solution and an inorganic hardening agent and we refer to our prior applications mentioned above for examples of such binders. The invention however is applicable to any water-based binder which produces briquettes with unsatisfactory green strengths.
The desiccant used is preferably solid inorganic dessicant e.g. anhydrous calcium chloride, which exhibits good results in tests and is readily available at low price, but other desiccants may be used. The desiccant may be pre-mixed with dry coal, either alone, or in combination with other hardening agents, prior to adding water-containing binders. But preferably the desiccant is added to the coal at the same time as or after the coal is mixed with binder and optionally other hardening agents. Specific desiccants and coal/binder mixes should be routinely tested to ensure that they are satisfactory and yield briquettes of the desired appearance and properties. Preferably, the desiccant is used in an amount of up to 1% by weight of the mix.Suitable desiccants include anhydrous calcium chloride, magnesium chloride, silica gel and activated alumina Preferred coals are high rank non-caking coals, especially those having low smoke emissions such as anthracite. Desirably the coal is of a particle 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 caking 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, ringrollor roll-pressing, die-pressing, rotary table pressing and pelletising, e.g. on a disc pelletiser.
The process preferably includes a hardening stage to permit the green briquettes to gain additional strength, depending upon the binder used. Hereinafter, reference will be made for convenience only to binders comprising molasses and an inorganic hardening agent.
The green briquettes harden over a period of 1 to 3 days at ambient temperature to give adequate crushing strengths, but the briquettes tend to have inadequate water resistance. However, the briquettes may be bagged in impervious sacks and allowed to further harden during storage. Preferably, however, a hot curing step is included to speed up the hardening stage and to make the briquettes water resistant, and this may be carried out at temperatures of the order of 200 to 3000C 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. It is to be noted that the hot curing step does not correspond to a carbonisation step, and thus not only are there energy savings, but the solid yield on a dry basis is very high.Additionally, there is a reduced risk of pollution.
The water resistance and/or appearance of the briquettes may be improved by an additional treatment with a spray or bath of a waterproofing agent. Several agents are known to have been proposed including, for example, aluminium acetate.
The present invention also provides briquettes formed using a process as described above.
The present invention will now be described by way of example only.
Example 1 A fine anthracite, from South Wales, was prepared by crushing and screening to minus 3mm. The anthracite was admixed with 10% of molasses, 1% iron ore and 1% phosphoric acid by weight of the final composition.
The mixture was briquetted in a pilot plant roll press, for comparison with the same mixture together with additions of 1.0% anhydrous magnesium chloride and 1.0% anhydrous calcium chloride.
Briquette testing was carried out under laboratory conditions at ambient temperatures of 200C. Crushing strengths according to standard tests were established for the green briquettes, hot briquettes and briquettes in which the final strength had developed.
The results obtained are presented below: Additive Green Strength Hot Crushing Final Strength Strength (kg) Product Crushing Shatter (%) ~~~~~~~~~~~~ Crushing 5 5 mins 10 mins Strength (kg) kg +1 1/4" +7/8" (+32mm) (+22mm) ~~~~~~ ~~~~~~~ ~~~~~~~ None 2.7 53 59 2.4 11.7 110 Magnesium chloride (anhydrous) 3.6 69 76 6.6 30.1 115 Calcium chloride (anhydrous) 8.7 83 86 7.4 15.8 105

Claims (12)

  1. CLAIMS 1. A process for the cold briquetting of fine coal comprising mixing fine coal with a binder to produce a water-containing briquetting mix and briquetting the mix, characterised by the presence in the briquetting mix of a desiccant or drying agent in an amount such that the initial green strength of the resulting briquettes is improved.
  2. 2. A process according to claim 1, wherein the mixture is briquetted at an elevated temperature.
  3. 3. A process according to claim 2, wherein the mixture is briquetted at a temperature above 50 C.
  4. 4. A process according to any preceding claim, wherein the binder comprises molasses or a sugar solution and an inorganic hardening agent.
  5. 5. A process according to any preceding claim, wherein the binder comprises molasses in an amount of from 5 15% by weight of the mix together with a hardening agent selected from iron oxide (or iron ore), calcium carbonate (or limestone) calcium phosphate (or phosphate rock) and aluminium oxide (or bauxite) optionally together with an acid.
  6. 6. A process according to any preceding claim, wherein the desiccant is anhydrous calcium chloride or magnesium chloride.
  7. 7. A process according to any preceding claim, wherein the desiccant is mixed with dry coal before addition of the binder.
  8. 8. A process according to any of claims 1 to 6, wherein the desiccant is mixed with the coal simultaneously with or after addition of the binder.
  9. 9. A process according to any preceding claim, wherein the desiccant is present in an amount of up to 2% by weight of the mix.
  10. 10. A process according to any preceding claim, wherein the coal is a high rank non-caking coal.
  11. 11. A process according to claim 10, wherein the coal is anthracite duff.
  12. 12. A process for the cold briquetting of fine coal substantially as hereinbefore described with reference to the Example.
GB8823444A 1988-10-06 1988-10-06 Briquetting process Expired - Lifetime GB2223505B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB8823444A GB2223505B (en) 1988-10-06 1988-10-06 Briquetting process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB8823444A GB2223505B (en) 1988-10-06 1988-10-06 Briquetting process

Publications (3)

Publication Number Publication Date
GB8823444D0 GB8823444D0 (en) 1988-11-16
GB2223505A true GB2223505A (en) 1990-04-11
GB2223505B GB2223505B (en) 1992-02-19

Family

ID=10644786

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8823444A Expired - Lifetime GB2223505B (en) 1988-10-06 1988-10-06 Briquetting process

Country Status (1)

Country Link
GB (1) GB2223505B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4212452A1 (en) * 1992-04-14 1993-10-21 Sophia Jacoba Gmbh Cold briquetted coal
US7288201B2 (en) * 1997-07-29 2007-10-30 Entegris, Inc. Methods for removing moisture from hydrogen halides
CN103374426A (en) * 2012-04-17 2013-10-30 张建民 Coal briquette and method for processing same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB241175A (en) * 1924-10-11 1925-12-17 Frankensteiner Magnesitwerke A Process for briquetting fuels
GB321646A (en) * 1928-06-06 1929-11-06 Bindphast Products Ltd A new or improved hardening cement or binder
GB877558A (en) * 1959-09-29 1961-09-13 Southern Wharves Ltd Improved binder for the production of coal briquettes

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB241175A (en) * 1924-10-11 1925-12-17 Frankensteiner Magnesitwerke A Process for briquetting fuels
GB321646A (en) * 1928-06-06 1929-11-06 Bindphast Products Ltd A new or improved hardening cement or binder
GB877558A (en) * 1959-09-29 1961-09-13 Southern Wharves Ltd Improved binder for the production of coal briquettes

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4212452A1 (en) * 1992-04-14 1993-10-21 Sophia Jacoba Gmbh Cold briquetted coal
US7288201B2 (en) * 1997-07-29 2007-10-30 Entegris, Inc. Methods for removing moisture from hydrogen halides
CN103374426A (en) * 2012-04-17 2013-10-30 张建民 Coal briquette and method for processing same
CN103374426B (en) * 2012-04-17 2015-05-06 张建民 Coal briquette and method for processing same

Also Published As

Publication number Publication date
GB2223505B (en) 1992-02-19
GB8823444D0 (en) 1988-11-16

Similar Documents

Publication Publication Date Title
EP0237179B1 (en) Coal briquetting process
US4219519A (en) Method for agglomerating carbonaceous fines
US5009671A (en) Process for producing a solid, finely divided fuel based on coal
CA2091832A1 (en) Binding composition for the preparation of a novel agglomerate based on finely divided materials, process using the said composition and thus obtained agglomerate
RU2224007C1 (en) Elevated-strength coal briquette and a method of fabrication thereof
US4877761A (en) Refractory composition for refractory linings of metallurgical vessels
GB2211512A (en) Briquetting process
RU2669940C1 (en) Method of briquetting carbon reducing agents
CA1158442A (en) Self-reducing iron oxide agglomerates
US4528029A (en) Self-reducing iron oxide agglomerates
EP0308095A1 (en) Coal briquetting process
CS204971B2 (en) Process for manufacturing carbonaceous pellets
GB2223505A (en) Briquetting process
US4728358A (en) Iron bearing briquet and method of making
EP0377995A2 (en) Briquetting process
KR100905581B1 (en) Coal Briquettes For Iron and Steel Making Process, Method Of Manufacturing Thereof
GB2227024A (en) Coal briquetting process
US4824438A (en) Process for producing smokeless, cured fuel briquettes
CA1174854A (en) Production of abrasion-resistant pressed articles mainly consisting of metal
EP0408327B1 (en) Fuel briquettes
EP0309266A2 (en) Process for producing carbon-containing agglomerates of siliceous material and silicon carbide therefrom
CN1011419B (en) Chafing dish fuel
RU2044076C1 (en) Method for production of briquettes from zinc-containing materials
SU1043106A1 (en) Batch for pelletizing phosphate raw material
WO1992007048A1 (en) Briquettes

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee

Effective date: 19931006