GB1135753A

GB1135753A – Method for carrying out gas-solids reactions
– Google Patents

GB1135753A – Method for carrying out gas-solids reactions
– Google Patents
Method for carrying out gas-solids reactions

Info

Publication number
GB1135753A

GB1135753A
GB5130165A
GB5130165A
GB1135753A
GB 1135753 A
GB1135753 A
GB 1135753A
GB 5130165 A
GB5130165 A
GB 5130165A
GB 5130165 A
GB5130165 A
GB 5130165A
GB 1135753 A
GB1135753 A
GB 1135753A
Authority
GB
United Kingdom
Prior art keywords
bed
beds
ore
occur
composition
Prior art date
1964-12-07
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
GB5130165A
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.)

Pullman Inc

Original Assignee
Pullman Inc
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.)
1964-12-07
Filing date
1965-12-02
Publication date
1968-12-04

1965-12-02
Application filed by Pullman Inc
filed
Critical
Pullman Inc

1968-12-04
Publication of GB1135753A
publication
Critical
patent/GB1135753A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS

B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes

B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles

B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to “fluidised-bed” technique

B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to “fluidised-bed” technique with two or more fluidised beds, e.g. reactor and regeneration installations

C—CHEMISTRY; METALLURGY

C21—METALLURGY OF IRON

C21B—MANUFACTURE OF IRON OR STEEL

C21B13/00—Making spongy iron or liquid steel, by direct processes

C21B13/0033—In fluidised bed furnaces or apparatus containing a dispersion of the material

C—CHEMISTRY; METALLURGY

C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS

C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS

C22B1/00—Preliminary treatment of ores or scrap

C22B1/02—Roasting processes

C22B1/10—Roasting processes in fluidised form

Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE

Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

Y02P10/00—Technologies related to metal processing

Y02P10/10—Reduction of greenhouse gas [GHG] emissions

Y02P10/134—Reduction of greenhouse gas [GHG] emissions by avoiding CO2, e.g. using hydrogen

Abstract

1,135,753. Fluidized bed reductions. PULLMAN Inc. 2 Dec., 1965 [7 Dec., 1964], No. 51301/65. Heading C1A. [Also in Divisions B1 and C7] Metal oxides, e.g. ores, are reduced in a reaction zone containing at least two fluidized beds separated by vertical baffles, the spaces above the beds being intercommunicating. The ore is preferably an iron ore, e.g. haematite, siderite, or limonite, which is reduced to magnetite. In Fig. 1, reactor 140 contains fluidized beds 142 and 144, preferably maintained at 800-1400‹ F., separated by arc-shaped baffle 138. Ore is fed from line 130 into bed 142, passes through orifice 146 into bed 144, is removed via line 150, and may be passed to another bed for further reduction. Beds 142 and 144 are fed with gases from partial oxidation furnaces 160 and 170 respectively, and with recycle gases from line 66. The gases may be of equal reducing strength, having a composition such that over-reduction beyond Fe 3 O 4 cannot occur. Alternatively, as described in Specification 1,135,755, the first gas may have a composition such that reduction beyond Fe 3 O 4 does occur, and the second gas may be oxidizing with respect to FeO and has a composition such that oxidation beyond Fe 3 O 4 cannot occur. The positioning of the baffle, which may be such as to give 65-80% conversion to Fe 3 O 4 in bed 142, reduces the total solids residence time necessary to achieve, e.g. 90% conversion, to below 90 mins. The ore is preheated (as described in Specification 1,135,754) first in cyclones 18 and 12, and then in fluidized bed heating zone 110 or in transfer line heat-exchanger 210 (Fig. 2, not shown), effluents from zone 110 and reactor 140 being recycled to cyclone 12. Alternatively, only the effluent from 140 may be used, or the effluents from beds 142 and 144 may be recycled separately.

GB5130165A
1964-12-07
1965-12-02
Method for carrying out gas-solids reactions

Expired

GB1135753A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US41654164

US3276858A
(en)

1964-12-07
1964-12-07
Method for carrying out gas-solids reactions

Publications (1)

Publication Number
Publication Date

GB1135753A
true

GB1135753A
(en)

1968-12-04

Family
ID=23650370
Family Applications (3)

Application Number
Title
Priority Date
Filing Date

GB5130165A
Expired

GB1135753A
(en)

1964-12-07
1965-12-02
Method for carrying out gas-solids reactions

GB2425468A
Expired

GB1135754A
(en)

1964-12-07
1965-12-02
A method of reducing non-magnetic iron ores

GB2425568A
Expired

GB1135755A
(en)

1964-12-07
1965-12-02
A method for reducing a non-magnetic oxidic iron ore

Family Applications After (2)

Application Number
Title
Priority Date
Filing Date

GB2425468A
Expired

GB1135754A
(en)

1964-12-07
1965-12-02
A method of reducing non-magnetic iron ores

GB2425568A
Expired

GB1135755A
(en)

1964-12-07
1965-12-02
A method for reducing a non-magnetic oxidic iron ore

Country Status (3)

Country
Link

US
(2)

US3276858A
(en)

FR
(1)

FR1461798A
(en)

GB
(3)

GB1135753A
(en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3276858A
(en)

*

1964-12-07
1966-10-04
Pullman Inc
Method for carrying out gas-solids reactions

US3607224A
(en)

*

1968-03-20
1971-09-21
Combustion Eng
Direct reduction of iron ore

US3661553A
(en)

*

1968-11-01
1972-05-09
Allis Chalmers Mfg Co
Process for reducing oxygen content of oxidic mineral ore

ZA71371B
(en)

*

1970-01-21
1972-06-28
Dunn Inc W
Recovery of thio2 from ores thereof

FR2450279A1
(en)

*

1979-03-01
1980-09-26
Fives Cail Babcock
Chemically attacking finely divided ore – using hot gas in circulation with fine ore particles, with heat and gas recovery to avoid energy waste gas loss and pollution

DE3540541A1
(en)

*

1985-11-15
1987-05-21
Metallgesellschaft Ag

METHOD FOR REDUCING HIGHER METAL OXIDS TO LOW METAL OXIDS

US5228901A
(en)

*

1991-02-25
1993-07-20
Idaho Research Foundation, Inc.
Partial reduction of particulate iron ores and cyclone reactor

FR2683830B1
(en)

*

1991-11-19
1994-04-08
Irsid

INSTALLATION FOR REDUCING THE IRON ORE IN A FLUIDIZED BED CIRCULATING.

FR2695141B1
(en)

*

1992-08-25
1994-10-07
Lorraine Laminage

Iron ore reduction plant using a circulating fluidized bed.

AT410802B
(en)

*

2001-11-09
2003-08-25
Voest Alpine Ind Anlagen

METHOD AND DEVICE FOR TREATING A FINE PARTICLE-SHAPED, IN PARTICULAR METAL-CONTAINING, INSERT MATERIAL

US7744848B2
(en)

*

2005-11-15
2010-06-29
Pittsburgh Mineral & Environment Technology, Inc.
High purity magnetite formation process and apparatus, and product thereof

CN105597917A
(en)

*

2016-01-19
2016-05-25
中国铝业股份有限公司
Method for increasing magnetism of weakly-magnetic iron ore

Family Cites Families (8)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

CA674804A
(en)

*

1963-11-26
Esso Research And Engineering Company
Production of magnetic oxides

US2477454A
(en)

*

1944-09-15
1949-07-26
Dorr Co
Process of reducing ferric oxide to ferrosoferric oxide

US2528552A
(en)

*

1946-09-10
1950-11-07
Pickands Mather & Co
Process for magnetically roasting hematitic ore and ore materials

DE873770C
(en)

*

1950-10-08
1953-04-16
Auto Union G M B H

Additional control for two-stroke internal combustion engines with at least two cylinders

FR1143415A
(en)

*

1955-03-18
1957-10-01
Dorr Oliver Inc

Apparatus for the fluidized bed treatment of finely divided solids

GB873770A
(en)

*

1957-03-30
1961-07-26
Azote Office Nat Ind
Improvements in or relating to the production of iron

US3020149A
(en)

*

1959-04-08
1962-02-06
Little Inc A
Beneficiation of ores

US3276858A
(en)

*

1964-12-07
1966-10-04
Pullman Inc
Method for carrying out gas-solids reactions

1964

1964-12-07
US
US41654164
patent/US3276858A/en
not_active
Expired – Lifetime

1965

1965-12-02
GB
GB5130165A
patent/GB1135753A/en
not_active
Expired

1965-12-02
GB
GB2425468A
patent/GB1135754A/en
not_active
Expired

1965-12-02
GB
GB2425568A
patent/GB1135755A/en
not_active
Expired

1965-12-06
FR
FR41085A
patent/FR1461798A/en
not_active
Expired

1966

1966-02-18
US
US52859466
patent/US3421884A/en
not_active
Expired – Lifetime

Also Published As

Publication number
Publication date

US3421884A
(en)

1969-01-14

GB1135755A
(en)

1968-12-04

US3276858A
(en)

1966-10-04

GB1135754A
(en)

1968-12-04

FR1461798A
(en)

1966-12-09

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