GB1282150A - Agglomeration of reduced iron ore - Google Patents

Agglomeration of reduced iron ore

Info

Publication number
GB1282150A
GB1282150A GB58807/69A GB5880769A GB1282150A GB 1282150 A GB1282150 A GB 1282150A GB 58807/69 A GB58807/69 A GB 58807/69A GB 5880769 A GB5880769 A GB 5880769A GB 1282150 A GB1282150 A GB 1282150A
Authority
GB
United Kingdom
Prior art keywords
bed
particles
hydrocarbon
ore
reduced iron
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
Application number
GB58807/69A
Inventor
William Joseph Metrailer
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.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering Co
Esso Research and Engineering Co
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 Exxon Research and Engineering Co, Esso Research and Engineering Co filed Critical Exxon Research and Engineering Co
Publication of GB1282150A publication Critical patent/GB1282150A/en
Expired 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
    • C10B55/00Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • C10B55/02Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
    • C10B55/04Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials
    • C10B55/08Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form
    • C10B55/10Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form according to the "fluidised bed" technique
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

1282150 Agglomerating reduced iron ore particles ESSO RESEARCH & ENG CO 2 Dec 1969 [11 Dec 1968] 58807/69 Heading C1A [Also in Division C7] Reduced iron ore particles are agglomerated by feeding into a fluidized bed thereof, particles of reduced iron ore of sizes ranging from 1 to 10,000 microns and averaging 50-400 microns, a substantial proportion of which are less than 325 Tayler Mesh size, introducing a heavy liquid hydrocarbon having a Bouradson carbon residue above 10% by weight, maintaining the particles at temperatures ranging from 850‹-1100‹ F. for a time sufficient to partially crack said hydrocarbon and deposit coke on the very fine particles thereby cementing them together to form particles larger than 325 mesh size. The bed may be fluidized with a non-oxidizing gas (e.g. N 2 or steam) at a superficial gas velocity of 0À3-1À5 ft./sec. or alternatively with a reducing gas. The hydrocarbon is preferably sprayed on to the top of the bed in droplets of size ranging from 1/10 size of the largest particle to be agglomerated to 10 times the size of the average particle in the bed. Residence times in the bed may be from 10-60 minutes. Preferably 0À1-1À0 part by weight hydrocarbon are used per hour per part of metal particles in the bed. The prior reduction of the ore is described (see Division C7) yielding typically reduced ore containing 90% Fe and 5% FeO. The ore may be fed to the fluidized bed in a hydrocarbon suspension formed by scrubbing the off gases from a reduction process.
GB58807/69A 1968-12-11 1969-12-02 Agglomeration of reduced iron ore Expired GB1282150A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US78291268A 1968-12-11 1968-12-11

Publications (1)

Publication Number Publication Date
GB1282150A true GB1282150A (en) 1972-07-19

Family

ID=25127568

Family Applications (1)

Application Number Title Priority Date Filing Date
GB58807/69A Expired GB1282150A (en) 1968-12-11 1969-12-02 Agglomeration of reduced iron ore

Country Status (3)

Country Link
US (1) US3607217A (en)
GB (1) GB1282150A (en)
NL (1) NL6918394A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4084958A (en) * 1974-05-20 1978-04-18 Stora Kopparbergs Bergslags Aktiebolag Method of reducing finely grained material containing iron oxides in a fluid bed
US4087274A (en) * 1975-07-04 1978-05-02 Boliden Aktiebolag Method of producing a partially reduced product from finely-divided metal sulphides
US5078899A (en) * 1990-05-01 1992-01-07 Idaho Research Foundation, Inc. Treating mine water
EP3708684B1 (en) 2019-03-15 2022-03-02 Primetals Technologies Austria GmbH Method for direct reduction in a fluidised bed

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US912641A (en) * 1905-06-12 1909-02-16 Ralph W H Atcherson Method of effecting the precipitation of flue-dust in blast-furnaces and of preventing the formation of the same.
US2014044A (en) * 1934-05-18 1935-09-10 Arthur B Haswell Method of cleaning gas
DE1221654B (en) * 1961-01-31 1966-07-28 Rheinstahl Ind Planung G M B H Process for the reduction of iron ores in rotary furnaces with gaseous or liquid reducing agents
US3356488A (en) * 1964-02-24 1967-12-05 John H Walsh Process for utilizing hydrocarbon injection into hot reducing gases in steelmaking
US3428446A (en) * 1965-10-26 1969-02-18 Exxon Research Engineering Co Fluidized bed production of iron
US3420656A (en) * 1966-09-02 1969-01-07 Lummus Co Process for forming hard oxide pellets and product thereof
US3414402A (en) * 1967-06-16 1968-12-03 Hydrocarbon Research Inc Beneficiation of low grade iron ores

Also Published As

Publication number Publication date
US3607217A (en) 1971-09-21
NL6918394A (en) 1970-06-15

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees