EP0032412A2 - Verfahren zur Herstellung von metallurgischem Koks aus einer Kohlenmischung - Google Patents
Verfahren zur Herstellung von metallurgischem Koks aus einer Kohlenmischung Download PDFInfo
- Publication number
- EP0032412A2 EP0032412A2 EP81200035A EP81200035A EP0032412A2 EP 0032412 A2 EP0032412 A2 EP 0032412A2 EP 81200035 A EP81200035 A EP 81200035A EP 81200035 A EP81200035 A EP 81200035A EP 0032412 A2 EP0032412 A2 EP 0032412A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- coking
- fine
- coal
- little
- drying
- 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
Links
- 239000003245 coal Substances 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 29
- 239000000571 coke Substances 0.000 title claims abstract description 18
- 239000000203 mixture Substances 0.000 title claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 238000004939 coking Methods 0.000 claims abstract description 63
- 239000011230 binding agent Substances 0.000 claims abstract description 13
- 239000002904 solvent Substances 0.000 claims abstract description 13
- 239000003610 charcoal Substances 0.000 claims description 21
- 238000001035 drying Methods 0.000 claims description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 13
- 229910052799 carbon Inorganic materials 0.000 claims description 13
- 230000001590 oxidative effect Effects 0.000 claims description 9
- 238000003763 carbonization Methods 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 8
- 238000000576 coating method Methods 0.000 claims description 8
- 238000002485 combustion reaction Methods 0.000 claims description 7
- 230000003647 oxidation Effects 0.000 claims description 7
- 238000007254 oxidation reaction Methods 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 230000001681 protective effect Effects 0.000 claims description 4
- 230000015556 catabolic process Effects 0.000 claims description 3
- 238000006731 degradation reaction Methods 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 4
- 239000003570 air Substances 0.000 description 3
- 239000003517 fume Substances 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000004520 agglutination Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
- C10B57/10—Drying
Definitions
- the present invention relates to an improved process for the manufacture of metallurgical coke, usable in particular as a constituent of the charge of blast furnaces
- metallurgical coke is generally produced by charging raw materials, mainly coking coal, in carbonization cells, and by heating these materials which, by distillation and agglutination, give a product having well-known properties. coke used in steel plants.
- the process for the production of metallurgical coke from a mixture of fine carbon with little or no coking and fine coking coal which is the subject of the present invention, is essentially characterized in that the moisture content is reduced of said fine charcoal with little or no coking at a value of less than 3%, in that to the said fine charcoal with little or no coking, dried, a binder and / or a solvent in suitable proportion, by mixing said fine charcoal little or not coking dried and coated with a binder and / or a solvent with said charcoal fine coking and in that one puts said mixture as is in the carbonization oven.
- the moisture content of the fine carbon which is little or not coking is reduced by heating to a temperature suitable for the various operating conditions, in particular the nature of the coal. It is also important that drying, in particular by heating, does not cause any oxidation of the fine charcoal.
- the heating of fine coal which is not very coking or not coking is carried out under a non-oxidizing atmosphere, composed for example of neutral smoke or dry steam.
- the drying gas of the fine charcoal contains only CO 2 and N 2 , as well as sufficiently diluted O 2 , all at a temperature sufficiently low to avoid any oxidation of the fine charcoal.
- the fine or little coking charcoal is at the desired temperature, it is particularly advantageous to introduce it, as quickly as possible, into a coating chamber, where the appropriate binder and / or solvent is added to it.
- the binder and / or the solvent are advantageously added in liquid form, preferably by spraying using a device which is the subject of another proposal from the same applicant.
- this transfer of fine carbon that is not very coking or not coking from the drying enclosure to the coating enclosure is carried out under a protective atmosphere, preferably under a non-oxidizing atmosphere.
- the process which is the subject of the present invention does not have these drawbacks.
- it makes it possible to avoid, or at least to greatly reduce handling of dried coal.
- the dried and possibly preheated fine coal undergoes only one manipulation, namely the transfer from the drying chamber to the coating chamber.
- the fine carbon that is not very coking or not is mixed in adequate proportions with coking fine carbon and the mixture is placed in the carbonization cells.
- the process of the invention makes it possible to carry out, in a particularly easy and economical manner, the drying and possibly the preheating of the fine coal which is not very coking or not, as well as the addition of binder. and / or solvent and the introduction of the mixture into the carbonization cells.
- binder and / or solvent ensures the coating of the carbon grains with a layer which protects them against oxidation by ambient air.
- the attached figure illustrates a device making it possible to implement the method which is the subject of the present invention.
- dans.lequel is carried out the drying of fine coal little or not coking.
- the coal, ground to size, is stored in 2 and poured by 3 into the enclosure 4 where, after splitting any lumps of coal, its actual drying takes place under the action of the fumes 5 coming from a flame 6 generated by a burner 7 supplied at 8 by air and at 9 by an appropriate fuel.
- the coal is led, along with the combustion products, through conduits in which the heat exchanges between the fumes and the fine charcoal continue.
- the coal thus dried and preheated leaves the enclosure 11 through the orifice 12 to penetrate, via an airlock, in the enclosure 13 in which, under a non-oxidizing atmosphere, obtained for example by taking a smoke at the outlet 19, the fine coal - binder / solvent (solid or liquid) mixture is carried out, the latter being brought into the enclosure 13 by 14.
- the coal little or non-coking, dried and coated is mixed with coking fine charcoal in a device not shown and the mixture is placed in carbonization cells.
- the gases leave the enclosure 11 through the opening 15, enter a chamber 16 where they are dusted at 17.
- the recovered dust is discharged at 18, while the dusted gases escape into the atmosphere. sphere at 19. Part of these is however deflected at 20 and recycled at 21 in a mixing chamber 22, disposed between the flame 6 proper and the enclosure 4, in order to lower the temperature of the flame 6 and to prevent the oxidation of carbon, and / or possibly the degradation of its coking properties.
- a heat exchanger is provided at 23 in the path of the pipe 20, to adjust the temperature of the gases to be injected at 21.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE6/47061A BE881162A (fr) | 1980-01-15 | 1980-01-15 | Procede ameliore de fabrication de coke metallurgique a partir d'un melange de charbons. |
| BE47061 | 1980-01-15 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP0032412A2 true EP0032412A2 (de) | 1981-07-22 |
| EP0032412A3 EP0032412A3 (en) | 1981-09-30 |
| EP0032412B1 EP0032412B1 (de) | 1984-04-18 |
Family
ID=3874845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP19810200035 Expired EP0032412B1 (de) | 1980-01-15 | 1981-01-13 | Verfahren zur Herstellung von metallurgischem Koks aus einer Kohlenmischung |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0032412B1 (de) |
| DE (1) | DE3163120D1 (de) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2305122C1 (ru) * | 2006-08-30 | 2007-08-27 | Борис Анатольевич Мусохранов | Шихта для получения металлургического кокса (варианты) |
| US7785447B2 (en) * | 2001-09-17 | 2010-08-31 | Combustion Resources, Llc | Clean production of coke |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2105518A5 (en) * | 1970-09-10 | 1972-04-28 | Lermusiaux Albert | Metallurgical coke - from non-cokeable precursors by reacting with binder before high temperature coking |
| FR2273857A1 (fr) * | 1974-06-07 | 1976-01-02 | Centre Rech Metallurgique | Procede de fabrication de coke metallurgique |
| BE875411A (fr) * | 1979-04-06 | 1979-07-31 | Centre Rech Metallurgique | Perfectionnements aux procedes de fabrication de agglomeres de houilles |
| BE873059A (fr) * | 1978-12-22 | 1979-06-22 | Centre Rech Metallurgique | Procede de fabrication de coke metallurgique |
-
1981
- 1981-01-13 DE DE8181200035T patent/DE3163120D1/de not_active Expired
- 1981-01-13 EP EP19810200035 patent/EP0032412B1/de not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7785447B2 (en) * | 2001-09-17 | 2010-08-31 | Combustion Resources, Llc | Clean production of coke |
| RU2305122C1 (ru) * | 2006-08-30 | 2007-08-27 | Борис Анатольевич Мусохранов | Шихта для получения металлургического кокса (варианты) |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0032412A3 (en) | 1981-09-30 |
| EP0032412B1 (de) | 1984-04-18 |
| DE3163120D1 (en) | 1984-05-24 |
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| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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| AK | Designated contracting states |
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| PUAL | Search report despatched |
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| AK | Designated contracting states |
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| 17P | Request for examination filed |
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| ITF | It: translation for a ep patent filed | ||
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| AK | Designated contracting states |
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| REF | Corresponds to: |
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| RAP2 | Party data changed (patent owner data changed or rights of a patent transferred) |
Owner name: CENTRE DE RECHERCHES METALLURGIQUES CENTRUM VOOR R |
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| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
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| STAA | Information on the status of an ep patent application or granted ep patent |
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| 26N | No opposition filed | ||
| GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
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