GB926213A - Improvements in and relating to the production of physically strong carbonaceous material from coal - Google Patents
Improvements in and relating to the production of physically strong carbonaceous material from coalInfo
- Publication number
- GB926213A GB926213A GB21162/60A GB2116260A GB926213A GB 926213 A GB926213 A GB 926213A GB 21162/60 A GB21162/60 A GB 21162/60A GB 2116260 A GB2116260 A GB 2116260A GB 926213 A GB926213 A GB 926213A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coal
- minutes
- temperature
- coking
- oxygen
- 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.)
- Expired
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
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/02—Treating solid fuels to improve their combustion by chemical means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
- C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
- C10B49/08—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
- C10B49/10—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form according to the "fluidised bed" technique
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/08—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form in the form of briquettes, lumps and the like
Abstract
In a process for producing physically strong briquettes or the like from any rank of coal, finely divided coal particles are heated to a temperature below that at which the distillate vapours evolved condense as tar and above that at which moisture is evolved in an atmosphere which in the case of high oxygen-containing coals need not contain added oxygen, in the case of non-coking coals contains from 1 to 8% by volume of oxygen, and in the case of coking coals contains from 8 to 20% by volume of oxygen, for a time sufficient to produce catalysed coal particles conditioned so that in a subsequent healing stage the hydrocarbonaceous matter is reduced and wherein the catalysed coal particles are rapidly heated in a fluidised bed to a higher temperature at which they are maintained for a time sufficient to evolve vapours and produce a char having a volatile matter content substantially less than that of the parent coal, the char being then calcined until the content of volatile matter is reduced to not more than 3% by weight. The initial treatment may be carried out with the coal particles in a fluidized bed or a dispersed phase. When the coal is a non-coking coal the coal particles may be heated to between 250 DEG and 500 DEG F., for a period of at least 5 minutes and up to 180 minutes. In the case of a coking coal the temperature may be maintained at between 500 DEG and 800 DEG F. for a period of at least 5 minutes and up to 180 minutes. Alternatively higher temperatures and shorter periods of treatment may be employed for both coking and noncoking coals. Heat for the treatment may be supplied by indirect heat exchange, partial combustion or by heating the fluidising or carrier gas. The catalysed coal particles are heated to a temperature between 800 DEG -1200 DEG F. for coking coals and 500 DEG -1200 DEG F. for non-coking coals. for a period of between 10 and 60 minutes and the char is heated, preferably in a fluidized bed with a fluidized medium free from carbon di-oxide, steam and oxygen, to a temperature between 1400 DEG -1800 DEG F. for a period of at least 7 minutes but not exceeding 60 minutes. The calcined char may be mixed with a bituminous binder after first being cooled to a temperature of from 30 DEG to 60 DEG F. above the softening point of the binder and briquetted, the briquettes being cured in an atmosphere containing at least 2,5% and up to 21% by volume of oxygen for a period of 90 to 180 minutes and at a temperature between 450 DEG -500 DEG F. The curing of the briqettes may be enhanced by incorporating in the briquettes or effecting the curing in the presence of reagents such as boran trifluoride, aluminium chloride, hydrogen peroxide and phosphoric acid. The carbonaceous binder for the briquettes may be produced from the tar evolved during carbonization of the catalysed coal particles. The separated tar is dehydrated to contain not more than 0,5% by weight of water and blown with air or steam until 5% of the lighter fractions have been removed. Catalysts may be incorporated in the tar during the blowing and may be organic persades, e.g. benzoyl persade, or inorganic substances such as sulphuric acid, boron trifluoride or aluminium chloride. The amount of catalyst used may be between 0,1% and 2% by weight. A suitable mixture for briquetting may comprise 75%-90% calcined char and 25-10% binder.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US821137A US3140241A (en) | 1959-06-18 | 1959-06-18 | Processes for producing carbonaceous materials |
Publications (1)
Publication Number | Publication Date |
---|---|
GB926213A true GB926213A (en) | 1963-05-15 |
Family
ID=25232618
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB21162/60A Expired GB926213A (en) | 1959-06-18 | 1960-06-16 | Improvements in and relating to the production of physically strong carbonaceous material from coal |
Country Status (9)
Country | Link |
---|---|
US (1) | US3140241A (en) |
AT (1) | AT244901B (en) |
BE (1) | BE591859A (en) |
CS (1) | CS155126B2 (en) |
FR (1) | FR1259299A (en) |
GB (1) | GB926213A (en) |
LU (1) | LU38797A1 (en) |
NL (2) | NL252579A (en) |
SE (1) | SE308502B (en) |
Families Citing this family (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3968052A (en) * | 1971-02-11 | 1976-07-06 | Cogas Development Company | Synthesis gas manufacture |
BE788835A (en) * | 1971-09-15 | 1973-03-14 | Fmc Corp | PRODUCTION OF TAR FROM THE COKEFACTION OF AGGLOMERS |
BE790753A (en) * | 1971-11-01 | 1973-04-30 | Fmc Corp | MIXED BRIQUETTES CONTAINING COAL AND IRON AND PROCESS FOR THEIR MANUFACTURE |
US3996108A (en) * | 1973-04-09 | 1976-12-07 | Fmc Corporation | Briquetting of reactive coal calcinate with high-temperature coke oven pitch |
US4108731A (en) * | 1973-11-29 | 1978-08-22 | Centro Sperimentale Metallurgico S.P.A. | Coke production |
IT1021566B (en) * | 1974-07-03 | 1978-02-20 | Sperimentale Metal Lurgico Spa | PERFECTION TO THE PROCESS FOR THE PRODUCTION OF FORMAT COKE |
NL7510613A (en) * | 1974-09-14 | 1976-03-16 | Werner Wenzel En Priv Doz Hein | PROCEDURE TO PREPARE KOOKS WITH IMPROVED STRENGTH. |
US4139416A (en) * | 1975-01-21 | 1979-02-13 | Centro Sperimentale Metallurgico S.P.A. | Carbonaceous material with high characteristics of surface area and activity and process for producing the same |
IT1046993B (en) * | 1975-02-19 | 1980-09-10 | Centro Speriment Metallurg | PROCESS PERFECTED FOR THE PRODUCTION OF COKE FORMATO |
US3992266A (en) * | 1975-07-24 | 1976-11-16 | Inland Steel Company | Recovery of coal fines from preheater |
US4148692A (en) * | 1977-08-26 | 1979-04-10 | Bethlehem Steel Corporation | Process for producing low reactivity calcined coke agglomerates |
US4260456A (en) * | 1979-05-29 | 1981-04-07 | Tosco Corporation | Single retort manufacturing technique for producing valuable char and gases from coke |
US4287023A (en) * | 1979-08-23 | 1981-09-01 | Phillips Petroleum Co. | Waste heat recovery |
US4288293A (en) * | 1980-04-14 | 1981-09-08 | Fmc Corporation | Form coke production with recovery of medium BTU gas |
US4303415A (en) * | 1980-09-29 | 1981-12-01 | Lubille Energy Development Co., Ltd. | Gasification of coal |
US4362532A (en) * | 1981-08-11 | 1982-12-07 | Conoco Inc. | Production of blast furnace coke via novel briquetting system |
US4461627A (en) * | 1981-12-18 | 1984-07-24 | Hitachi, Ltd. | Upgrading method of low-rank coal |
US4557733A (en) * | 1984-11-05 | 1985-12-10 | Peabody Development Company | Formcoke process |
US4602917A (en) * | 1985-04-22 | 1986-07-29 | Fmc Corporation | Formcoke having modified bituminous binder |
US4698067A (en) * | 1985-06-24 | 1987-10-06 | Fmc Corporation | Formcoke having modified bituminous binder |
US5236468A (en) * | 1992-03-19 | 1993-08-17 | J. S. Mccormick Company | Method of producing formed carbonaceous bodies |
AT505227B1 (en) * | 2007-05-09 | 2012-07-15 | Siemens Vai Metals Tech Gmbh | PROCESS FOR THE MANUFACTURE OF FORMINGS |
CN113621393B (en) * | 2021-07-21 | 2022-11-01 | 武汉钢铁有限公司 | Classification matching method of coking coal with 18-22% of volatile matter |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2734851A (en) * | 1956-02-14 | smith | ||
US1943291A (en) * | 1931-02-04 | 1934-01-16 | Arthur V Abbott | Process for the low temperature distillation of coal |
US2164933A (en) * | 1934-11-07 | 1939-07-04 | Maurel Invest Corp | Process of baking fuel briquettes |
US2582712A (en) * | 1947-05-17 | 1952-01-15 | Standard Oil Dev Co | Fluidized carbonization of solids |
US2805189A (en) * | 1950-05-25 | 1957-09-03 | Standard Oil Co | Method of heating and fluidizing for a carbonization process |
US2815316A (en) * | 1952-01-18 | 1957-12-03 | American Cyanamid Co | Process of treating coal |
BE551782A (en) * | 1956-12-31 | |||
US2869992A (en) * | 1957-01-02 | 1959-01-20 | Exxon Research Engineering Co | Preliminary heating of fluid coke briquettes |
US3018227A (en) * | 1957-01-22 | 1962-01-23 | Consolidation Coal Co | Preparation of formcoke |
US3070515A (en) * | 1957-05-06 | 1962-12-25 | Consolidation Coal Co | Fluidized low temperature carbonization of caking bituminous coal |
US3051629A (en) * | 1958-07-07 | 1962-08-28 | Consolidation Coal Co | Preparing metallurgical fuel briquets from non-caking coal by preshrinking char |
-
0
- NL NL130819D patent/NL130819C/xx active
- NL NL252579D patent/NL252579A/xx unknown
-
1959
- 1959-06-18 US US821137A patent/US3140241A/en not_active Expired - Lifetime
-
1960
- 1960-06-10 FR FR829685A patent/FR1259299A/en not_active Expired
- 1960-06-11 LU LU38797D patent/LU38797A1/xx unknown
- 1960-06-14 AT AT188762A patent/AT244901B/en active
- 1960-06-14 BE BE591859A patent/BE591859A/en unknown
- 1960-06-16 GB GB21162/60A patent/GB926213A/en not_active Expired
- 1960-06-16 CS CS388660A patent/CS155126B2/cs unknown
-
1963
- 1963-09-06 SE SE9785/63A patent/SE308502B/xx unknown
Also Published As
Publication number | Publication date |
---|---|
NL130819C (en) | 1900-01-01 |
CS155126B2 (en) | 1974-05-30 |
FR1259299A (en) | 1961-04-21 |
LU38797A1 (en) | 1960-08-11 |
NL252579A (en) | 1900-01-01 |
DE1421258B1 (en) | 1972-09-21 |
BE591859A (en) | 1960-10-03 |
SE308502B (en) | 1969-02-17 |
US3140241A (en) | 1964-07-07 |
AT244901B (en) | 1966-02-10 |
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