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 PDF

Info

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
Application number
PCT/AU1986/000154
Other languages
French (fr)
Inventor
Colin Graham Mcallan
John Arthur Harris
Original Assignee
Gippsland Institute Of Advanced Education
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 Gippsland Institute Of Advanced Education filed Critical Gippsland Institute Of Advanced Education
Publication of WO1987003296A1 publication Critical patent/WO1987003296A1/en

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
    • 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
    • C10L9/00Treating solid fuels to improve their combustion
    • C10L9/02Treating 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.

Landscapes

  • 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

CLAIMSThe claims defining the invention are as follows:
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.
PCT/AU1986/000154 1985-11-29 1986-05-29 The production of hard compact carbonaceous material through acid/alkali treatment WO1987003296A1 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (11)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US4496365A (en) Method of producing briquettes from organic waste products
EP0002275A1 (en) Granular activated carbon manufacture from brown coal treated with dilute inorganic acid
HUT35708A (en) Process for the production of pigment compositions
RU97108692A (en) METHOD FOR PRODUCING ANIMAL FOOD ADDITIVE ON THE BASIS OF FERMENTATION BOILON
GB2138442A (en) Fuel briquettes
US2985643A (en) Process for conversion of lignocellulose materials
WO1987003296A1 (en) The production of hard compact carbonaceous material through acid/alkali treatment
CN1022845C (en) Method for manufacturing coal brick
EP0308095A1 (en) Coal briquetting process
EP0124038A3 (en) Process for producing cement material from industrial processing and urban slurries
DE3335484C2 (en)
JPH089954A (en) Carbide of beer cake
JPH03174241A (en) Binder and binder compound for coagulation of segmented substance, as well as obtained coagulated product and its manufacture
EP0192807A2 (en) Process for manufacturing active briquettes rich in carbon
EP0377995A2 (en) Briquetting process
US4067894A (en) Process for the production of granular metal-capturing agents for treating waste effluents containing heavy metals
RU2786721C1 (en) Method for obtaining a complex sorbent
EP0848743B1 (en) Processing of resilient materials
SU575078A1 (en) Method of granulating fodder mixture
RU2105043C1 (en) Method of fabricating briquets
SU711135A1 (en) Charge for production of vanadium-containing agglomerate and pellets
US686248A (en) Process of making decolorizing charcoal and filtering compounds.
SU1583380A1 (en) Method of producing claydite
MXPA98000598A (en) Materials manufacturing process resilien
JPS5799329A (en) Manufacture of granular composition

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): HU JP US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE FR GB IT LU NL SE