EP1013747A2 - Fabrication d'agglomérats - Google Patents
Fabrication d'agglomérats Download PDFInfo
- Publication number
- EP1013747A2 EP1013747A2 EP99309100A EP99309100A EP1013747A2 EP 1013747 A2 EP1013747 A2 EP 1013747A2 EP 99309100 A EP99309100 A EP 99309100A EP 99309100 A EP99309100 A EP 99309100A EP 1013747 A2 EP1013747 A2 EP 1013747A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- weight
- agglomerates
- montmorillonite
- clay
- binder
- 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- Withdrawn
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 238000000034 method Methods 0.000 claims abstract description 28
- 239000011230 binding agent Substances 0.000 claims abstract description 21
- 239000004927 clay Substances 0.000 claims abstract description 19
- 239000002245 particle Substances 0.000 claims abstract description 16
- 229920002689 polyvinyl acetate Polymers 0.000 claims abstract description 13
- 239000011118 polyvinyl acetate Substances 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 239000000839 emulsion Substances 0.000 claims abstract description 8
- 239000000654 additive Substances 0.000 claims abstract description 6
- 239000010815 organic waste Substances 0.000 claims abstract description 6
- 230000000996 additive effect Effects 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 3
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 13
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 11
- 239000003245 coal Substances 0.000 claims description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 5
- 229910052791 calcium Inorganic materials 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- 239000003973 paint Substances 0.000 claims description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical group C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 3
- 239000011734 sodium Substances 0.000 claims description 3
- 229910052708 sodium Inorganic materials 0.000 claims description 3
- 229920001353 Dextrin Polymers 0.000 claims description 2
- 239000004375 Dextrin Substances 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 239000003610 charcoal Substances 0.000 claims description 2
- 239000000571 coke Substances 0.000 claims description 2
- 235000019425 dextrin Nutrition 0.000 claims description 2
- 230000002538 fungal effect Effects 0.000 claims description 2
- 239000003112 inhibitor Substances 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 229920005615 natural polymer Polymers 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims description 2
- 239000002699 waste material Substances 0.000 description 9
- 239000004484 Briquette Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 239000010791 domestic waste Substances 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 2
- 239000003830 anthracite Substances 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
Definitions
- the present invention is concerned with methods for the production of fuel agglomerates (such as briquettes or pellets) and, in particular, the production of agglomerates in the nature of briquettes or pellets for gasification.
- fuel agglomerates such as briquettes or pellets
- Briquettes or pellets are conventionally formed by bonding together particles such as waste materials, using binders such as bitumen or pitch. With such binders, the bonding process is carried out at elevated temperatures, resulting in the emission of substantial quantities of smoke and other polluting by-products from the briquetting or pelletising plant.
- a method of producing agglomerates comprises blending carbonaceous particles, and optionally organic waste material, with an additive comprising particulate clay, and with a binder comprising polyvinyl acetate, shaping the resulting blend to form agglomerates, and permitting the binder to cure in the agglomerates.
- the binder is such that it is activated in the presence of moisture (moisture being present because the binder is present as an emulsion) and, when cured, generally renders the agglomerate substantially waterproof or at least water resistant.
- the binder used in the method according to the present invention is generally readily available and can be adapted to suit the characteristics of many types of carbonaceous particles required to be agglomerated.
- the polyvinyl acetate is one which mixes readily and is combustible whilst being substantially free of noxious pollutants; it is safe to handle and sets hard when mixed with finely divided particulate materials such as finely divided sludges.
- the binder used in the method according to the invention namely polyvinyl acetate, has a special affinity for fine particles of coal (which are preferred), as well as other carbonaceous fuels.
- the binder continues to bind such particles even in the presence of other materials which are organic in nature.
- the clay is a montmorillonite, such as sodium montmorillonite, or potassium montmorillonite or magnesium montmorillonite.
- Calcium montmorillonite is the preferred such clay; such a clay may have at least some of the cations replaced by other cations, such as sodium ions.
- a particularly preferred such clay is sodium exchanged calcium montmorillonite.
- the clay is present in an amount of 0.1 to 5% by weight, based on the weight of the agglomerates. It is preferred that the particulate clay has a particle size of less than 2 ⁇ , further preferably less than 1 ⁇ .
- the polyvinyl acetate may be derived from a waste material.
- a suitable waste material for recycling includes base materials used in the manufacture of emulsion paint.
- recycled material from the manufacture of emulsion paint in the manufacture of agglomerates said agglomerates comprising carbonaceous particles, and additive comprising a clay, and said recycled material as binder therefor.
- the blend preferably contains substantially equal amounts of carbonaceous particles and organic waste material (typically from 25 to 45% by weight of each), with 0.1 to 5% by weight (such as about 2%) of particulate clay, 0.5 to 8.0% by weight (such as about 2%) of polyvinyl acetate (the latter being measured on a dry solids basis), all in the presence of 2 to 25% (such as about 10 to 12%) by weight moisture.
- the ingredients when thoroughly mixed into a doughy consistency, are typically extruded or pelletised to form agglomerates of the required shape or size.
- the agglomerate may be rubbery in nature at this stage but hardens on curing as excess moisture is allowed to evaporate.
- the speed of this curing process is directly influenced by ambient temperatures. Typically hardening takes place over 24 hours at about 15°C, or over 3 minutes when at the higher temperature of about 100°C. Evaporation of moisture can be accelerated by the use of radio wave frequencies, or the like.
- the agglomerates When the agglomerates are formed by extrusion, there is generally a temperature increase in the extruder nozzle which assists in the evaporation of moisture.
- the hardness of the resulting agglomerates progressively increases with time, provided that the ambient temperature is over 0°C.
- the curing process should ideally take place inside a building in a controlled temperature atmosphere.
- the agglomerates are preferably allowed to dry and harden and may subsequently be dried by means of gentle heating. When optimum hardness has been achieved, the agglomerate is waterproof, and can be stored outside so as to be exposed to the ambient climatic conditions.
- the binder may contain one or more further polymer materials, including natural polymers such as dextrin or the like.
- Suitable additives which enhance thermal shock resistance include calcium carbonate.
- the carbonaceous particles used in the method according to the invention may be charcoal, coke or one of various grades of coal, of which anthracite is preferred because of its clean combustion characteristics.
- the carbonaceous particles may be in moist form when mixed with the binder, without deleterious effect on the resulting briquettes. This is advantageous as the use of such moist material avoids the need for previous drying.
- the ingredients were transported by conveyor 2 to tunnel 3, and thence to a plough type rotary mixer 4 for a period of 2 minutes.
- the resultant blend was agglomerated to produce briquettes on twin roll press 6.
- the briquettes were then air-dried at 80°C for 10 minutes in curing unit 7, and then allowed to cool to ambient temperature.
- the briquettes were then transported on conveyor 8 to store 9.
- the resultant briquettes have a crushing strength of 63kgf (compared with 32kgf without the presence of clay in the briquette).
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)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
- Carbon And Carbon Compounds (AREA)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9825064.0A GB9825064D0 (en) | 1998-11-16 | 1998-11-16 | Agglomerate production |
GB9825064 | 1998-11-16 | ||
GBGB9922690.4A GB9922690D0 (en) | 1998-11-16 | 1999-09-27 | Agglomerate production |
GB9922690 | 1999-09-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1013747A2 true EP1013747A2 (fr) | 2000-06-28 |
EP1013747A3 EP1013747A3 (fr) | 2002-06-05 |
Family
ID=26314679
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99309100A Withdrawn EP1013747A3 (fr) | 1998-11-16 | 1999-11-16 | Fabrication d'agglomérats |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP1013747A3 (fr) |
GB (1) | GB2343678B (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018033712A1 (fr) * | 2016-08-15 | 2018-02-22 | Binding Solutions Limited | Briquettes |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100355868C (zh) * | 2006-10-11 | 2007-12-19 | 北京科兰之星环保科技有限公司 | 化肥造气的洁净型煤及其制备方法和应用 |
US11136517B2 (en) * | 2017-03-28 | 2021-10-05 | Pelleton Global Renewables Ltd. | Method for producing agglomerates from a biomass stream |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1031723A (en) * | 1962-04-06 | 1966-06-02 | Yorkshire Dyeware And Chemical | Process for the preparation of agglomerates of solid fuel |
GB2006179A (en) * | 1977-10-17 | 1979-05-02 | Revertex South Africa | The treatment of particulate material to form aggregates |
WO1987000855A1 (fr) * | 1985-08-08 | 1987-02-12 | Alternative Fossil Fuels, Inc. | Briquettes de charbon contenant de l'argile inorganique et leur procede de production |
US4773919A (en) * | 1984-11-15 | 1988-09-27 | Metallgesellschaft Ag | Fixed bed gasification process |
FR2683544A1 (fr) * | 1991-11-08 | 1993-05-14 | Viabilite Ste Ind | Materiau combustible divise agglomere par un liant, procede de preparation du materiau. |
US5221290A (en) * | 1991-02-04 | 1993-06-22 | American Colloid Company | Charcoal briquettes bound with an organic binder and a water-swellable clay and method |
WO1994017161A1 (fr) * | 1993-01-19 | 1994-08-04 | Schulz Helmut W | Procede et appareil pour l'elimination de dechets solides |
-
1999
- 1999-11-16 EP EP99309100A patent/EP1013747A3/fr not_active Withdrawn
- 1999-11-16 GB GB9927016A patent/GB2343678B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1031723A (en) * | 1962-04-06 | 1966-06-02 | Yorkshire Dyeware And Chemical | Process for the preparation of agglomerates of solid fuel |
GB2006179A (en) * | 1977-10-17 | 1979-05-02 | Revertex South Africa | The treatment of particulate material to form aggregates |
US4773919A (en) * | 1984-11-15 | 1988-09-27 | Metallgesellschaft Ag | Fixed bed gasification process |
WO1987000855A1 (fr) * | 1985-08-08 | 1987-02-12 | Alternative Fossil Fuels, Inc. | Briquettes de charbon contenant de l'argile inorganique et leur procede de production |
US5221290A (en) * | 1991-02-04 | 1993-06-22 | American Colloid Company | Charcoal briquettes bound with an organic binder and a water-swellable clay and method |
FR2683544A1 (fr) * | 1991-11-08 | 1993-05-14 | Viabilite Ste Ind | Materiau combustible divise agglomere par un liant, procede de preparation du materiau. |
WO1994017161A1 (fr) * | 1993-01-19 | 1994-08-04 | Schulz Helmut W | Procede et appareil pour l'elimination de dechets solides |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018033712A1 (fr) * | 2016-08-15 | 2018-02-22 | Binding Solutions Limited | Briquettes |
Also Published As
Publication number | Publication date |
---|---|
GB2343678B (en) | 2002-12-11 |
EP1013747A3 (fr) | 2002-06-05 |
GB2343678A (en) | 2000-05-17 |
GB9927016D0 (en) | 2000-01-12 |
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