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WO1995023834A1 - Coke for metallurgical uses - Google Patents

Coke for metallurgical uses Download PDF

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Publication number
WO1995023834A1
WO1995023834A1 PCT/GB1995/000465 GB9500465W WO9523834A1 WO 1995023834 A1 WO1995023834 A1 WO 1995023834A1 GB 9500465 W GB9500465 W GB 9500465W WO 9523834 A1 WO9523834 A1 WO 9523834A1
Authority
WO
WIPO (PCT)
Prior art keywords
coke
coal
metal
coke oven
steel
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.)
Ceased
Application number
PCT/GB1995/000465
Other languages
French (fr)
Inventor
Peter Robertson Pelling
Rodney Martin Sambrook
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dytech Corp Ltd
Original Assignee
Dytech Corp Ltd
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 Dytech Corp Ltd filed Critical Dytech Corp Ltd
Priority to AU18530/95A priority Critical patent/AU1853095A/en
Publication of WO1995023834A1 publication Critical patent/WO1995023834A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
    • C10B57/06Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives

Definitions

  • the invention relates to the production of coke useful in the manufacture of metallurgical products such as steel or the like.
  • the invention concerns the inclusion of a waste material together with the coal from which coke is manufactured, which waste material is otherwise costly and inconvenient to treat.
  • the recycling or disposal of metal-containing solid wastes from catalytic processes is difficult and costly.
  • the wastes contain a complex mixture of materials, the contained metals typically being nickel, vanadium, cobalt, molybdenum, tungsten, tin; and the like.
  • the catalytically active material will typically be presented on a carrier, such as alumina, carbon, silica, zeolite; or the like.
  • the waste material will also contain significant residues from the catalytic process such as carbonaceous material and sulphur. It has now been realised that if these waste materials are used with the coal in the manufacture of coke, the waste material is effectively treated and the coke can then be used in circumstances in which the presence of the catalytically active metals is useful.
  • a method of providing a metal-containing coke for use in the production of steel or the like comprising feeding coal and spent metal catalyst to a coke oven and converting the coal to coke thereby to form a coke containing the catalytically active metal.
  • the spent catalyst material may be added to the oven alongside the coal or the two may be preblended in appropriate proportions.
  • the spent catalyst will be present in a low concentration to minimise the risk of any damage to the coke oven or carry over of unacceptable level of materials into the metallurgical product to be formed.
  • concentration is preferably up to 2% by weight, preferably less.
  • spent catalyst is used directly or it may be pretreated to adapt it better for the coking process.
  • the grades of coal used are selected according to the requirements of the finished coke product.
  • the coal may be partly replaced by another source of carbonaceous material, e.g. tar, pitch; or the like.
  • the catalyst support and the contained metal or metal salts or oxides will remain and be included in the formed coke.
  • the carbonaceous material can be converted into coke or become part of the coke oven gas (which at some installations can be used to heat the coke ovens).
  • the sulphur will join other sulphur released from the coal and will be treated in the usual way and some sulphur may remain in the coke.
  • the coke oven may be of any appropriate type, having a basic or an acidic lining and in which the coal is heated up to about 1200°C or even higher, e.g. up to 1800°C. Other additives may be present, in known manner.
  • a coke product of the invention can be used in the manufacture of steel.
  • it can be a reactive coke to be added to the blast furnace charge so contributing valuable alloying elements.
  • a coke may also be used in electrometallurgical furnaces; foundry cupolas; carbide furnaces; and the like. The non-metallic fractions will be included in the steelworks slag.
  • the coke is capable of uses beyond those specifically mentioned.
  • the coke is useful in the metallurgy of iron, zinc, tin, and other metals.
  • the invention may be well understood it will now be described by way of illustration with reference to the following examples.
  • Black pellets of spent catalyst comprising a mixture of carbon, hydrocarbons, sulphur, alumina, nickel, molybdenum and cobalt were added to a coal tar mix in a proportion of less than 2% by weight.
  • the resultant blend was converted to coke in a coke oven.
  • the formed coke was added to a blast furnace charge.
  • Granules of spent catalyst comprising a mixture of carbon, hydrocarbons, aluminosilicate, nickel and vanadium, were treated in the manner of Example I.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Catalysts (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

Spent catalyst is added to coal and the mixture converted to coke in a coke oven.

Description

COKE FOR METALLURGICAL USES
The invention relates to the production of coke useful in the manufacture of metallurgical products such as steel or the like. The invention concerns the inclusion of a waste material together with the coal from which coke is manufactured, which waste material is otherwise costly and inconvenient to treat.
The recycling or disposal of metal-containing solid wastes from catalytic processes is difficult and costly. The wastes contain a complex mixture of materials, the contained metals typically being nickel, vanadium, cobalt, molybdenum, tungsten, tin; and the like. The catalytically active material will typically be presented on a carrier, such as alumina, carbon, silica, zeolite; or the like. The waste material will also contain significant residues from the catalytic process such as carbonaceous material and sulphur. It has now been realised that if these waste materials are used with the coal in the manufacture of coke, the waste material is effectively treated and the coke can then be used in circumstances in which the presence of the catalytically active metals is useful.
According to the invention in one aspect there is provided a method of providing a metal-containing coke for use in the production of steel or the like; the method comprising feeding coal and spent metal catalyst to a coke oven and converting the coal to coke thereby to form a coke containing the catalytically active metal.
The spent catalyst material may be added to the oven alongside the coal or the two may be preblended in appropriate proportions. Typically the spent catalyst will be present in a low concentration to minimise the risk of any damage to the coke oven or carry over of unacceptable level of materials into the metallurgical product to be formed. The concentration is preferably up to 2% by weight, preferably less.
Usually the spent catalyst is used directly or it may be pretreated to adapt it better for the coking process.
The grades of coal used are selected according to the requirements of the finished coke product. The coal may be partly replaced by another source of carbonaceous material, e.g. tar, pitch; or the like.
When the spent catalyst is heated in a coke oven alongside the coal, the catalyst support and the contained metal or metal salts or oxides will remain and be included in the formed coke. The carbonaceous material can be converted into coke or become part of the coke oven gas (which at some installations can be used to heat the coke ovens). The sulphur will join other sulphur released from the coal and will be treated in the usual way and some sulphur may remain in the coke.
The coke oven may be of any appropriate type, having a basic or an acidic lining and in which the coal is heated up to about 1200°C or even higher, e.g. up to 1800°C. Other additives may be present, in known manner.
A coke product of the invention can be used in the manufacture of steel. For example, it can be a reactive coke to be added to the blast furnace charge so contributing valuable alloying elements. A coke may also be used in electrometallurgical furnaces; foundry cupolas; carbide furnaces; and the like. The non-metallic fractions will be included in the steelworks slag.
The invention is capable of uses beyond those specifically mentioned. For example, the coke is useful in the metallurgy of iron, zinc, tin, and other metals. In order that the invention may be well understood it will now be described by way of illustration with reference to the following examples.
Example I
Black pellets of spent catalyst comprising a mixture of carbon, hydrocarbons, sulphur, alumina, nickel, molybdenum and cobalt were added to a coal tar mix in a proportion of less than 2% by weight. The resultant blend was converted to coke in a coke oven. The formed coke was added to a blast furnace charge.
Example II
Granules of spent catalyst comprising a mixture of carbon, hydrocarbons, aluminosilicate, nickel and vanadium, were treated in the manner of Example I.

Claims

1. A method of providing a metal-containing coke for use in the production of steel or the like; the method comprising feeding coal and spent metal catalyst to a coke oven and converting the coal to coke thereby to form a coke containing the catalytically active metal.
2. A method according to Claim 1 , including heating the coal up to 1200°C.
3. A method according to Claim 1 , wherein the coke oven has a basic lining.
4. A method according to Claim 1 , wherein the coke oven has an acidic lining.
5. A method according to any preceding Claim, wherein the coal is at least partly replaced by another carbonaceous material.
6. A method according to any preceding Claim, wherein the proportion of spent catalyst is below 2% by weight of the mixture to be converted.
7. A method according to any preceding Claim, including the subsequent step of using the coke as an additive in a metallurgical process.
8. A method according to Claim 7, wherein the coke is added to a blast furnace and used in the manufacture of steel.
PCT/GB1995/000465 1994-03-03 1995-03-03 Coke for metallurgical uses Ceased WO1995023834A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU18530/95A AU1853095A (en) 1994-03-03 1995-03-03 Coke for metallurgical uses

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9404108A GB2287037B (en) 1994-03-03 1994-03-03 Coke ovens
GB9404108.4 1994-03-03

Publications (1)

Publication Number Publication Date
WO1995023834A1 true WO1995023834A1 (en) 1995-09-08

Family

ID=10751233

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1995/000465 Ceased WO1995023834A1 (en) 1994-03-03 1995-03-03 Coke for metallurgical uses

Country Status (3)

Country Link
AU (1) AU1853095A (en)
GB (1) GB2287037B (en)
WO (1) WO1995023834A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191404214A (en) * 1914-02-18 1915-05-18 Thomas Moore Hickman A New or Improved Fuel and Method of Making the Same.
DE2850152A1 (en) * 1978-03-07 1979-09-13 Arbed Redn. of fuel consumption, esp. coke, in blast furnace - by adding catalyst, pref. iron oxide, which increases activity
US4176041A (en) * 1977-02-24 1979-11-27 Kobe Steel, Ltd. Method for reforming low grade coals
DE3009834A1 (en) * 1980-03-14 1981-09-24 Coc-Luxembourg S.A., Luxembourg Addn. of surface-active solids to hydrocarbon coking feeds - increases yield and reduces fissuring tendency of coke
JPH06279876A (en) * 1993-03-26 1994-10-04 Nisshin Steel Co Ltd Treatment of ni-containing waste catalyst for recovering raw material for steel making

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB545473A (en) * 1940-08-02 1942-05-28 Pittsburgh Coal Carbonization Improvements in or relating to low temperature carbonization processes and the products obtained thereby

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191404214A (en) * 1914-02-18 1915-05-18 Thomas Moore Hickman A New or Improved Fuel and Method of Making the Same.
US4176041A (en) * 1977-02-24 1979-11-27 Kobe Steel, Ltd. Method for reforming low grade coals
DE2850152A1 (en) * 1978-03-07 1979-09-13 Arbed Redn. of fuel consumption, esp. coke, in blast furnace - by adding catalyst, pref. iron oxide, which increases activity
DE3009834A1 (en) * 1980-03-14 1981-09-24 Coc-Luxembourg S.A., Luxembourg Addn. of surface-active solids to hydrocarbon coking feeds - increases yield and reduces fissuring tendency of coke
JPH06279876A (en) * 1993-03-26 1994-10-04 Nisshin Steel Co Ltd Treatment of ni-containing waste catalyst for recovering raw material for steel making

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 9444, Derwent World Patents Index; AN 94-355057 *

Also Published As

Publication number Publication date
GB2287037B (en) 1997-11-12
AU1853095A (en) 1995-09-18
GB9404108D0 (en) 1994-04-20
GB2287037A (en) 1995-09-06

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