GB799551A - Reduction of a metal oxide with carbon monoxide and hydrogen - Google Patents
Reduction of a metal oxide with carbon monoxide and hydrogenInfo
- Publication number
- GB799551A GB799551A GB3608/56A GB360856A GB799551A GB 799551 A GB799551 A GB 799551A GB 3608/56 A GB3608/56 A GB 3608/56A GB 360856 A GB360856 A GB 360856A GB 799551 A GB799551 A GB 799551A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydrogen
- bed
- iron
- mixture
- oxide
- 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
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0073—Selection or treatment of the reducing gases
-
- 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
- Y02P10/122—Reduction of greenhouse gas [GHG] emissions by capturing or storing CO2
-
- 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
-
- 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
- Y02P10/143—Reduction of greenhouse gas [GHG] emissions of methane [CH4]
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
799,551. Extracting metals; iron manufacture. TEXACO DEVELOPMENT CORPORATION. Feb. 6, 1956, No. 3608/56. Classes 72 and 82(1) In a process for reducing metal oxide to metal in which a down-flowing bed of oxide is met by an up-flow of carbon monoxide and hydrogen whilst part of the resulting gas mixture is withdrawn at an intermediate point (21) in the bed and air is admitted to the bed above that intermediate point (at 18) for combustion of the remaining monoxide and hydrogen, nitrogen is also introduced to the bed above said intermediate point (at 24), and preferably below the air admission point, to ensure the temperature of the upper portion of the bed being below the.sintering temperature of the oxide. The process is said to be applicable to the production of Ni, Cr, V, Ti, and especially iron, a "sponge" metal being produced. The withdrawn gas mixture may be treated (at 22 and/or 14) to remove CO 2 and water vapour and the residual CO and hydrogen reintroduced into the lower part of the bed. As described for producing iron, oxide ore is admitted into furnace 12 at 16, preheated CO-hydrogen mixture at 11, air at 18, and nitrogen at 24. An air fractionator 5 supplies the nitrogen and also oxygen which is led along line 6 to a gas generator 7. There the oxygen pre-heated to 300‹F. is mixed with natural gas (or similar fuel) led in at 8 and which has been pre-heated to 1000‹F., the resulting CO- hydrogen mixture being treated if necessary at 13 for removal of sulphur and at 14 for removal of steam and CO 2 and led along line 11. CO 2 from the line 21 and separator 14, may also be led via 9 and 15 to the generator 7. Iron sulphide from separator 13 may be added to the ore at 16. The CO-H mixture should contain more than one and preferably two or three volumes of CO per volume of H 2 , and it is pre-heated to enter the furnace at 1750‹F. The gas mixture withdrawn at 21 is at about 1500‹F., whilst in the upper zone of the furnace the temperature of the ore is maintained at between 1400 and 2000‹F. Iron sponge is discharged at 17.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3608/56A GB799551A (en) | 1956-02-06 | 1956-02-06 | Reduction of a metal oxide with carbon monoxide and hydrogen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3608/56A GB799551A (en) | 1956-02-06 | 1956-02-06 | Reduction of a metal oxide with carbon monoxide and hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
GB799551A true GB799551A (en) | 1958-08-13 |
Family
ID=9761547
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3608/56A Expired GB799551A (en) | 1956-02-06 | 1956-02-06 | Reduction of a metal oxide with carbon monoxide and hydrogen |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB799551A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4556421A (en) * | 1982-10-08 | 1985-12-03 | M.A.N. Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft | Method of operating a synthesis gas-ore reduction process |
US4556417A (en) * | 1983-05-17 | 1985-12-03 | Hylsa, S.A. | Process for the direct reduction of iron ores |
US4617051A (en) * | 1982-06-25 | 1986-10-14 | M.A.N. Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft | Method of operating a reactor for synthesis gas production |
WO1996000303A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
WO1996000302A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
WO1996000304A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
WO1996017089A1 (en) * | 1994-12-01 | 1996-06-06 | Voest-Alpine Industrieanlagenbau Gmbh | Sponge iron production process and plant |
WO2016202461A1 (en) * | 2015-06-17 | 2016-12-22 | Bw-Energiesysteme Gmbh | Method of storing chemical and electrical energy via thermodynamically reversible cycle processes |
-
1956
- 1956-02-06 GB GB3608/56A patent/GB799551A/en not_active Expired
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4617051A (en) * | 1982-06-25 | 1986-10-14 | M.A.N. Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft | Method of operating a reactor for synthesis gas production |
US4556421A (en) * | 1982-10-08 | 1985-12-03 | M.A.N. Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft | Method of operating a synthesis gas-ore reduction process |
US4556417A (en) * | 1983-05-17 | 1985-12-03 | Hylsa, S.A. | Process for the direct reduction of iron ores |
US5858058A (en) * | 1994-06-23 | 1999-01-12 | Voest-Alpine Industrieanlagenbau Gmbh | Process and plant for avoiding metal dusting in the direct reduction of iron-oxide-containing materials |
WO1996000302A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
WO1996000304A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
AU691293B2 (en) * | 1994-06-23 | 1998-05-14 | Brifer International Ltd. | Direct reduction process for iron oxide-containing materials |
US5855643A (en) * | 1994-06-23 | 1999-01-05 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
WO1996000303A1 (en) * | 1994-06-23 | 1996-01-04 | Voest-Alpine Industrieanlagenbau Gmbh | Direct reduction process for iron oxide-containing materials |
US5871560A (en) * | 1994-06-23 | 1999-02-16 | Voest-Alpine Industrieanlagenbau Gmbh | Process and plant for the direct reduction of iron-oxide-containing materials |
WO1996017089A1 (en) * | 1994-12-01 | 1996-06-06 | Voest-Alpine Industrieanlagenbau Gmbh | Sponge iron production process and plant |
US5997609A (en) * | 1994-12-01 | 1999-12-07 | Voest-Alpine Industrieanlagenbau Gmbh | Sponge iron production process and plant |
WO2016202461A1 (en) * | 2015-06-17 | 2016-12-22 | Bw-Energiesysteme Gmbh | Method of storing chemical and electrical energy via thermodynamically reversible cycle processes |
CN107787381A (en) * | 2015-06-17 | 2018-03-09 | Bw能源系统有限公司 | Can be with the method for electric energy by thermodynamics Reversible Cycle process storage of chemical |
CN107787381B (en) * | 2015-06-17 | 2020-02-07 | Bw能源系统有限公司 | Method for storing chemical and electrical energy by means of a thermodynamically reversible cyclic process |
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