WO1987003296A1 - The production of hard compact carbonaceous material through acid/alkali treatment - Google Patents
The production of hard compact carbonaceous material through acid/alkali treatment Download PDFInfo
- Publication number
- WO1987003296A1 WO1987003296A1 PCT/AU1986/000154 AU8600154W WO8703296A1 WO 1987003296 A1 WO1987003296 A1 WO 1987003296A1 AU 8600154 W AU8600154 W AU 8600154W WO 8703296 A1 WO8703296 A1 WO 8703296A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- carbonaceous material
- coal
- dried
- processes
- lignite
- Prior art date
Links
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
-
- 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
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/02—Treating solid fuels to improve their combustion by chemical means
Definitions
- the invention described herein involves the treatment of carbonaceous material with water or aqueous acid or aqueous alkali or a combination of these so as to produce a carbonaceous material of altered composition and in general exhibiting improved hardness and abrasion resistance.
- the treatment may be adjusted so as to produce a carbonaceous material contaning elements, principally metals, in intimate contact with the carboneous material as may be advantages in subsequent process.
- the inorganic and mineral contents may be altered or reduced to obviate problems associated with their presence in subsequent processes.
- the products of this process described herein, may be produced as powdered or granular forms or they may be formed into shapes for future beneficial use.
- Carbonaceous materials suffer in commercial applicaion through a lack of resistance to abrasion and through levels of inorganic or mineral constituents which are inappropriate in the final application of the carbonaceous material.
- carbonaceous material including wood based material, coal, lignite, peat and like carbonaceous material
- a fine state either with or without previous drying procedures, added to water and aqueous alkali to form a paste, exhibiting gel like properties under appropriate conditions, and extruded to form pellets or applied as a slurry to a tray or pan or similar drying area and allowed to dry or is subjected to forced drying.
- the dried or partially dried carbonaceous material which has been so treated is then leached using water at a tempreature between 0 deg C and 1000 deg C or with dilute aqueous acid between such temperatures.
- the leached material is then dried to form a hard compact product.
- a proportion of the carbonaceous material is removed by this process together with a proportion of the mineral and inorganic material.
- Such alteration to the inorganic and mineral content may be beneficial in processes such as combustion, gasification, carbonization, ion exchange processes and n 1iquefaction processesi
- liqnite or brown coal treated by this process using potassium hydroxide as the alkali and leached using water alone, gave a hard * compact carbonaceous product from the insoluble fraction » loaded with potassium in intimate contact with the carbonaceous components of the product, rendering it suitable for processes such as gasification, where the potassium acts as a catalyst or in adsorption processes or ion exchange processes in which the potassium ions may be replaced by other ions.
- the hardness or abrasion resistance of this product is significantly better than briquettes or solar densified coal produced from the same coal feed.
- Alkali within the meaning of the above process is specifically to include carbonates.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Carbonaceous material, including wood based material, coal, lignite, peat and like carbonaceous material, is ground to a fine state, either with or without previous drying procedures, added to water and aqueous alkali to form a paste, exhibiting gel like properties and extruded to form pellets or applied as a slurry to a tray or pan or similar drying area and allowed to dry or is subjected to forced drying. The dried or partially dried carbonaceous material which has been so treated is then leached using water at a temperature between 0oC and 1000oC or with dilute aqueous acid or alkali between such temperatures. The leached material is then dried to form a hard compact product. The carbonaceous products so formed by this process have an altered mineral and inorganic content and good resistance to abrasion on drying. Such alteration to the inorganic and mineral content may be beneficial in processes such as combustion, gasification, carbonization, ion exchange processes and in liquefaction processes. The treatment may be adjusted so as to produce a carbonaceous material containing elements, principally metals, in intimate contact with the carbonaceous material as may be advantageous in subsequent processes. Alternatively the inorganic and mineral contents may be altered or reduced to obviate problems associated with their presence in subsequent processes.
Description
Title: The Production of Hard Compact Carbonaceous Material Through Acid/Alkali Treatment.
Suaβary of the Invention
In essence , the invention described herein involves the treatment of carbonaceous material with water or aqueous acid or aqueous alkali or a combination of these so as to produce a carbonaceous material of altered composition and in general exhibiting improved hardness and abrasion resistance. The treatment may be adjusted so as to produce a carbonaceous material contaning elements, principally metals, in intimate contact with the carboneous material as may be advantages in subsequent process.
Alternately the inorganic and mineral contents may be altered or reduced to obviate problems associated with their presence in subsequent processes. The products of this process described herein, may be produced as powdered or granular forms or they may be formed into shapes for future beneficial use.
Carbonaceous materials suffer in commercial applicaion through a lack of resistance to abrasion and through levels of inorganic or mineral constituents which are inappropriate in the final application of the carbonaceous material.
In the invention described herein carbonaceous material, including wood based material, coal, lignite, peat and like carbonaceous material, is ground to a fine state, either with or without previous drying procedures, added to water and aqueous alkali to form a paste, exhibiting gel like properties under appropriate conditions, and extruded to form pellets or applied as a slurry to a tray or pan or similar drying area and allowed to dry or is subjected to forced drying. The dried or partially dried carbonaceous material which has been so treated is then leached using water at a tempreature between 0 deg C and 1000 deg C or with dilute aqueous acid between such temperatures. The leached material is then dried to form a hard compact product.
A proportion of the carbonaceous material is removed by this process together with a proportion of the mineral and inorganic material. The carbonaceous products so formed by this process, or by similar process in which the material is subjected to acid and alkali treatment in different order or in which the products are dried or partially dried between the processing steps, have an altered mineral and inorganic content and good resistance to abrasion on drying. Such alteration to the inorganic and mineral content may be beneficial in processes such as combustion,
gasification, carbonization, ion exchange processes and n 1iquefaction processesi
For example, liqnite or brown coal, treated by this process using potassium hydroxide as the alkali and leached using water alone, gave a hard* compact carbonaceous product from the insoluble fraction » loaded with potassium in intimate contact with the carbonaceous components of the product, rendering it suitable for processes such as gasification, where the potassium acts as a catalyst or in adsorption processes or ion exchange processes in which the potassium ions may be replaced by other ions. The hardness or abrasion resistance of this product is significantly better than briquettes or solar densified coal produced from the same coal feed. Alkali within the meaning of the above process is specifically to include carbonates.
Claims
Claim 1. A process wherein carbonaceous material , including coal, brown coal, lignite, peat, wood or like carbonaceous material, is ground, with or without predrying, either in the presence of aqueous alkali or added to aqueous alkali, mixed and/or additionally ground and then either formed into shapes or spread as a slurry and partially or completely dried.
Claim 2. A Process wherein carbonaceous material, including coal, brown coal, lignite, peat, wood or like carbonaceous material, is ground, with or without predrying, added to aqueous acid, mixed and/or additionally ground and then either formed into shapes or spread as a slurry and partially or completely dried.
Claim 3. A Process wherein coal, brown coal, lignite, peat, wood or like carbonaceous material is treated as described in claim 1 then subjected with or without complete drying to treatment with water at a temperature in the range 0 deg C to 1000 deg C, filtered and partially or completely dried.
Claim 4. A Process wherein coal, brown coal, lignite, peat, wood or like carbonaceous material is treated as described in claim 2 then subjected to treatment with water at a temperature in the range of 0 deg C to 1000 deg C, filtered if required and partially or completely dreid.
Claim 5. A Process wherein coal, brown coal, lignite, peat, wood or like carbonaceous material is subjected to treatment as described in Clain 1 then subjected, with or without complete drying, to treatment with aqueous acid at a temperature in the range 0 deg C to 1000 deg C, filtered if required and then treated with water at a temperature in the range 0 deg C to 1000 deg C, filtered and dried.
Claim 6. A Process wherein coal, brown coal, lignite, peat, wood or like carbonaceous material is first treated as in claim 2, then subjected with or without complete drying, to aqueous alkali at a temperature in the range 0 deg C to 1000 deg C, filtered if required and then treated with water at a temperature in the range 0 deg C to 1000 deg C, filtered and dried.
Claim 7. Any process embodying all or part of any of the previous claims where in the filtrate is retained as a product.
Claim 8. Any process embodying all or part of any of the previous claims.
Claim 9. Any process embodying all or part of any previous claims in any combination.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU50888/85A AU5088885A (en) | 1985-11-29 | 1985-11-29 | The production of hard compact carbonaceous material through water/acid/alkali treatment |
AU50888/85 | 1985-11-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1987003296A1 true WO1987003296A1 (en) | 1987-06-04 |
Family
ID=3737473
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU1986/000154 WO1987003296A1 (en) | 1985-11-29 | 1986-05-29 | The production of hard compact carbonaceous material through acid/alkali treatment |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0246242A1 (en) |
AU (1) | AU5088885A (en) |
WO (1) | WO1987003296A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110684580A (en) * | 2019-11-14 | 2020-01-14 | 安徽省宗正农业科技开发有限公司 | Preparation method of composite high-energy biomass fuel rod |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU1211470A (en) * | 1969-03-12 | 1971-09-09 | Fisons Limited | Composition |
AU5688973A (en) * | 1972-06-15 | 1974-12-19 | Commonwealth Scientific And Industrial Research Organisation | Demineralisation of brown coal |
AU6996774A (en) * | 1973-07-31 | 1975-03-06 | International Oils Exploration N. L | Demineralization of coal |
AU6849174A (en) * | 1973-05-01 | 1975-11-06 | Australian Portland Cement Ltd. | Upgrading of coal |
AU1220476A (en) * | 1975-03-31 | 1977-09-22 | Leeds & Northrup Co. | Treating solid fuels |
AU2261577A (en) * | 1976-02-27 | 1978-08-31 | Papirindustriens Forskningsinstitutt | Mechanical pulp |
AU2495177A (en) * | 1976-09-14 | 1978-11-09 | G. G. Monsod Jr | Paper pulp from water hyacinth |
AU5057279A (en) * | 1978-09-22 | 1980-03-27 | Mo Och Domsjo Aktiebolag | Alkaline digestion of lignocellulosic material |
AU6126580A (en) * | 1979-07-19 | 1981-02-13 | Eric S. Prior | Accelerated pulping process |
AU6262480A (en) * | 1979-09-25 | 1981-04-09 | Shell Internationale Research Maatschappij B.V. | Up-grading low-grade solid fuel |
AU2675484A (en) * | 1983-04-14 | 1984-11-22 | Shinnenryoyu Kaihatsugijutsu Kenkyukumiai | Pretreatment of cellulose biomass |
-
1985
- 1985-11-29 AU AU50888/85A patent/AU5088885A/en not_active Abandoned
-
1986
- 1986-05-29 EP EP19860903151 patent/EP0246242A1/en not_active Withdrawn
- 1986-05-29 WO PCT/AU1986/000154 patent/WO1987003296A1/en unknown
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU1211470A (en) * | 1969-03-12 | 1971-09-09 | Fisons Limited | Composition |
AU5688973A (en) * | 1972-06-15 | 1974-12-19 | Commonwealth Scientific And Industrial Research Organisation | Demineralisation of brown coal |
AU6849174A (en) * | 1973-05-01 | 1975-11-06 | Australian Portland Cement Ltd. | Upgrading of coal |
AU6996774A (en) * | 1973-07-31 | 1975-03-06 | International Oils Exploration N. L | Demineralization of coal |
AU1220476A (en) * | 1975-03-31 | 1977-09-22 | Leeds & Northrup Co. | Treating solid fuels |
AU2261577A (en) * | 1976-02-27 | 1978-08-31 | Papirindustriens Forskningsinstitutt | Mechanical pulp |
AU2495177A (en) * | 1976-09-14 | 1978-11-09 | G. G. Monsod Jr | Paper pulp from water hyacinth |
AU5057279A (en) * | 1978-09-22 | 1980-03-27 | Mo Och Domsjo Aktiebolag | Alkaline digestion of lignocellulosic material |
AU6126580A (en) * | 1979-07-19 | 1981-02-13 | Eric S. Prior | Accelerated pulping process |
AU6262480A (en) * | 1979-09-25 | 1981-04-09 | Shell Internationale Research Maatschappij B.V. | Up-grading low-grade solid fuel |
AU2675484A (en) * | 1983-04-14 | 1984-11-22 | Shinnenryoyu Kaihatsugijutsu Kenkyukumiai | Pretreatment of cellulose biomass |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110684580A (en) * | 2019-11-14 | 2020-01-14 | 安徽省宗正农业科技开发有限公司 | Preparation method of composite high-energy biomass fuel rod |
Also Published As
Publication number | Publication date |
---|---|
EP0246242A1 (en) | 1987-11-25 |
AU5088885A (en) | 1987-06-04 |
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