• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method of converting a charge of non-ferrous metal matte in a Pierce-Smith or similar converter. The fluid charge is blown with a total flow of oxidizing gas effective to maintain autogenous converting temperatures through a plurality of spaced-apart tuyeres limited in number and individual cross-sectional area effective to maintain the gas underexpanded at a pressure within the range from about 50 to about 150 psig so that it penetrates the bath in the form of discrete steady jets to positions remote from the tuyere tips thereby reducing degradation of the refractories and build up of accretions. The gas is injected through from three to six tuyeres.
    公开号:SU1487819A3
    申请号:SU802901508
    申请日:1980-03-26
    公开日:1989-06-15
    发明作者:J Keith Brimacombe；Enrique O Hoefele
    申请人:Liquid Air Canada；
    IPC主号:
    专利说明:

    UNION OF SOVIET
    SOCIALIST
    REPUBLIC „ZU I1) 1487819 AZ (51) 4 С 22 В 15 / 06_
    STATE NOMINATION
    BY INVENTIONS AND DISCOVERIES
    AT GNST USSR
    DESCRIPTION OF THE INVENTION
    TO THE PATENT
    ALL-UNION (21) 2901508 / 23-02 (22) 03/26/80 (31) 024243 (32) 03/27/79 (33) of (46) 06/15/89. Bull. No. 22 (71) Kaneidian Liquide Air Ltd (CA) (72) J. Kate Brimacombe (CA) and Enrique O. Hoefel (CI) (53) 669.333.3 (088.8) (56) French application No. 2219235, cp. C 22 V 15/06, 1974.
    (54) METHOD FOR CONVERTING COPPER STEINS (57) The invention relates to the conversion of copper mattes in a converter by supplying blast containing 21-40% oxygen through tuyeres. The aim of the invention is to reduce the wear of the refractory lining of the Converter. The supply of blasting is carried out during the purge period at a pressure of 3.5-10.5 kg / cm 2 at a speed of more than 0.9 M. When the converter is turned from loading to the purge and back, the blast is supplied at a pressure of 0.7-1.4 kg / cm ^. Purge through 3-6 lances. The lance cross section in the light is 6.5-19.5 cm 2 , the lances are located at a distance of 91.5 cm from the ends and 20.3-38 cm from each other. The invention is intended for converting copper mattes to blister copper.
    The purpose of the invention is to reduce the wear of the refractory lining of the Converter.
    The conditions in the converter during the purge process change as follows. The temperature range in which the converters operate according to the invention is approximately 11001300 ° C. The purge time is 6-20 hours, depending on the quality of the matte. The load varies between 100-200 tons of matte, depending on the quality of matte, flux - in the range of 20-60 tons (also depending on the quality of matte). With this loading of raw materials, the oxygen consumption necessary for oxidation is in the range of 112-224 m g / min. The output is
    70-120 tons of copper and 30-80 tons of slag per cycle. The frequency of penetration by a known process is every 15-60 s. According to the invention, punching is usually not necessary until the end of the purge process, however standard punches are used at the end of the cycle, especially for copper, when gas consumption is reduced, and consequently ·. and temperature.
    Due to the injection of high pressure gas according to the proposed method, its total flow rate can increase up to about 840 m 3 / min, in this case, the reduction in cycle time is proportional to the increase in flow rate.
    311,. ,, 1487819>
    cm
    When the furnace is rotated from the loading position to the purge position until the desired degree of immersion is achieved, the pressure in the tuyeres is maintained
    1487819 2
    0.7-1.4 kg / cm (mainly 1.05 kg / cm 2 ).
    The duration of the cycle is affected by the quality of the raw materials. So various grades of raw materials contain from 20 to 60% Cu (for copper).
    High-quality matte get- '. They are used when concentrates are enriched with copper due to the high chal-C) cocyte (Cu ^ 3) content and / or when flame melting methods are used to melt the solid concentrate.
    In this case, a matte containing 55% Cu is usually obtained. Since at 15 higher contents of Cu the Fe content in matte is lower, then .. less slag is formed and the converter volume is filled to a greater degree with a valuable metal, for example Cu ^ Z 20 (formed at the first stage of the copper conversion cycle). In this case, fresh matte (or the original matte) is introduced in a smaller number of time intervals (twice for a matte with 55% 25 Cu) and the cycle time is shorter, since less Re3 is oxidized at the first stage of conversion.
    Example 1. Used a converter with a length of 1068 cm and a diameter
    396.5 there, equipped with 3-6 tuyeres with an inner diameter of 1.27 cm. Copper matte (55% Cu) was used as raw material; Flux contained 85% 5O g . The oxidizing gas is air.
    The first stage of the treatment cycle:
    1. The converter is hot immediately after the completion of the previous cycle,
    2. Through, the neck with the help of ladles, driven by cranes, load 80-100 tons of matte. To load the converter you need 4-5 full buckets. Matte temperature 11001150 ° С о
    In the loading position of the converter (tuyeres are not immersed in the bath), air is blown through the tuyeres at low pressure, not more than 1.05 kg / cm 2 ,
    4. The converter rotates until it reaches the purge position; the tuyeres are immersed 45.7 cm in molten matte.
    5. The purge pressure is increased to
    8.5 kg / cm 2 immediately after the converter reaches the purge position.
    6o Airflow rate is maintained at approximately equal.
    700 m ^ s / min for about 45 min. At this moment, the temperature in the converter is approximately „, 1200 ° С depending on the temperature of the feedstock.
    7. The purge pressure is reduced to 1.05 kg / cm 2 , the converter is turned to the loading position and the air flow is turned off.
    8. Through the neck of the converter load 15-20 tons of siliceous flux.
    9. Re-start the purge, as in paragraphs. 3-5.
    10. After purging for 2030 min, the air flow is turned off, as in paragraph 7.
    11. At this time, the temperature in the converter is approximately 1220-1240 ° C on the copper content of the matte is 72-75%. About 35 tons of slag is formed.
    12. Drain approximately 30 tons of slag (2 buckets).
    13. If the temperature in the converter is π. 11 higher than 123 ° C, approximately 10 tons of cold material (solid recirculation material) are loaded into the converter.
    14. In the converter add 40-60 tons of fresh matte (55% Cu) (2-3 buckets),
    15. At this point, another 10-20 tons are usually added.
    16. Begin purging on PP. 3-5.
    17. Repeat n, 6,
    18. Operations in paragraphs 8 and 9 can be carried out or not depending on. ·> Whether the operation is performed according to clause 15.
    19 ° After 60-80 minutes of purging (from p. 16), the air is turned off according to p. 7.
    20. The temperature in the converter is approximately 1220-1240 ° C. The matte quality is 78-80% (most or all of Fe8 is oxidized and approximately 30 tons of slag is formed). This slag is poured into buckets.
    21. The end of the first stage: together with the product in the reactor remains 80 110 tons of Cu 1 5,
    Second stage: the starting material is mainly Cu ^ 3, Fe8 and / or flux may be present.
    22. If the temperature at the end-stage is too high (above 1240 ° C) and / or. If relatively pure copper working materials remain (80% Cu or more), approximately 10 tons of cold working material are added to the reactor.
    s 1487819
    23 ° Start purging by following. p. 3-5 of the first stage.
    24. The air flow rate is maintained at about 700 m 3 / min 5 at a pressure of 8.4 kg / cm 1 . Usually there are no stops in the second stage. The temperature rises slowly from 1180 ° C to 1220 ° C. The purge time varies depending on the amount of Cu ^ 3 contained in the system at the beginning of the second stage, and is 3-4 hours ('the total purge time in the cycle is
    5-8 hours, total cycle time, including loading, shutdowns to cranes, etc. prolongs the cycle by 1-2 hours
    25. When the content of C in the bath is 97-98% (an experienced operator can accurately indicate this point),. the pressure is reduced to not more than 1.05 kg / cm 1 .
    o After about 5 minutes, the converter is turned to the loading position and the gas is turned off. You can add 25 a bit of flux to bind iron oxide, which can be in the system.
    27. The final product is blister copper in an amount of 60-90 tons (98.5-99.5% Cu). *
    Low-quality mattes are formed when concentrates are enriched in chalcopyrite and melted in a baking oven. In such cases, a matte containing 30% Cu is typically obtained. ^ 5 This means that the matte contains a greater amount of Re3 and a greater amount of slag and a smaller amount are formed. Cu (in the form of Cu ^ 3) in the reactor.
    To solve this problem, fresh matte is added to the converter several times during the first stage of purging (approximately 5 times for matte with 30% Cu) and the quantities of flux loaded and the resulting slag change accordingly. However, the converter is based on the same principles: temperatures do not exceed 1. 1250 ° C; a thorough assessment of the matte quality during the purge process.
    Example 2. In the converter, a matte containing 30% Cu is treated in the same manner as in Example 1, using the same flux and air as the oxidizing gas.
    The cycle is as follows.
    Pp 1-4 are the same as in example 1 Ф <
    For items 5 and 6, the temperature in the converter exceeds 1250 r C, since the purge time is longer. This can be avoided by lowering the purge pressure to about 5.6 kg / cm 1 in 6 lances and reducing the total flow rate to no more than 560 m 3 / min. Conversely, the purge pressure can be 8.4 kg / cm g , but the number of tuyeres is 4 and the total consumption is also reduced to no more than 560 m 5 / min.
    In addition, to avoid high temperatures, you can use a purge pressure of 8.4 kg / cm 1 , a total air flow of 700 m 3 / min and 6 tuyeres, as well as additives of large quantities of cold recirculating materials, but this way requires more frequent shutdowns during purging and a large number of cold materials.
    Other than this, the process is carried out analogously to example 1, but the purge time is longer (i.e., approximately 60 minutes).
    7. The same as in example 1.
    8. Requires 30 tons of flux.
    9. The same as in example 1.
    10. The purge time 30-45 minutes
    11. That’s the same as and in Example I, except that the content
    C in matte is 45%,
    12. Formed 60 tons of slag.
    13. Enter 10-20 tons of cold material.
    14. 60 tons of fresh matte (30% C).
    15.30 tons of flux,
    16. The same as in example 1.
    17. Same as in clause 7 for a low-quality matte.
    18. The same as in example 1.
    19. 60 min; matte with a content of 55-60% C.
    20. Repeat paragraphs. 12-19 with the following changes:
    12. Up to about 40 tons of slag.
    13. Up to about 10 tons of cold material.
    14. Up to about 40 tons of matte.
    15. Up to 20. t of flux.
    and 17. Same as in example 1.
    19. 60 min; matte contains approximately 70% C.
    20. Repeat paragraphs. 12-17 with the following. changes:
    '- 12. 30 tons of slag.
    13. Ut. cold slag optional). ''
    ... 14. 20 tons of fresh matte.
    15. 10 tons of flux (otherwise, paragraphs 16-21 are the same as in example 1 until the end of the first stage).
    The second stage is similar to that described in example 1.
    The following variables affect. process flow.
    When using oxygen-enriched air, the heat balance is improved and the cycle time is reduced, This is significant when
    a) 50% matte is used, therefore, at a lower Fe8 content in fresh matte, a large amount of heat (cold mattes) is not generated in the first stage;
    b) low-quality mattes are used and it is required to melt large quantities of cold materials (recirculation material) or even concentrates;
    c) in the second stage, especially if the consumption for a lance is large, some melt cooling in the lance zone occurs due to increased pressures.
    An increased gas flow rate (840 m / min) increases the concentration of 0 ^, i.e. heat generation is improved, but this can also cause excessive removal of material from the waste gas bath, which shortens the cycle time. This is convenient in cases where
    a) the tuyeres are located near one end of the reactor, and the neck is at the other; .
    b) there is a need to generate more heat when using oxygen-enriched gas;
    c) finely ground materials (for example, concentrates) are not loaded into the reactor.
    权利要求:
    Claims (1)
    [1]
    Formulas of Conversion Method for converting matte, including loading matte and flux into a horizontal cylindrical converter, containing an elongated closed chamber formed by a cylindrical metal body and round ends and having a refractory lining, a neck, an exhaust pipe that exhausts gases, metal lances external devices for supplying oxidizing gas under pressure into the tuyeres entering the chamber through the housing and passing through the refractory lining, devices supporting the conve rubbed in a horizontal position when turning it from the loading position to the purge position, in which the ends of the tuyeres are immersed in a bath, blowing molten matte with jets of oxidizing gas containing 21-40% oxygen, under the melt surface passing 25 through the melt bath, while maintaining the process autogeneity at temperature up to 1300 ° C, a converter rotation between a loading position for loading and purging of flux, slag removal, and re-loading the extraction of copper from hydrochloric poluchen10 converter, e of r l aspirants and by the fact that, for the purpose abbreviated wear of the refractory lining of the converter, while blowing, the oxidizing gas is supplied at a pressure of 3.5-10.5 kg / cm g and a speed of more than 0.9 M, when the converter is turned from the loading position to the purge position, and the oxidizing gas is fed back 40 are blown at a pressure of 0.7-1, 4 kg / cm2; purging is carried out through 4-6 tuyeres with a cross-sectional area of 6.5-19.5 cm 12 each, located at a distance of 20.3-38 cm from each other and at a distance of 91.5 cm from the ends of the elongated closed chamber, and the oxidizing gas is fed into the melt to a depth of 38-45.7 cm at an angle down to the horizontal hoists.
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE241351C|
    US1768649A|1929-04-22|1930-07-01|Edward I Williams|Method of and converter for bessemerizing|
    CA869474A|1967-11-20|1971-04-27|Vogt John|Process for gaseous reduction of oxygen containing copper and apparatus therefor|
    US3819362A|1969-05-06|1974-06-25|Copper Range Co|Copper converting process with prolonged blowing period|
    CA931358A|1971-02-01|1973-08-07|J. Themelis Nickolas|Process for continuous smelting and converting of copper concentrates|
    US3990890A|1972-05-17|1976-11-09|Creusot-Loire|Process for refining molten copper matte with an enriched oxygen blow|
    US3802685A|1972-08-29|1974-04-09|Steel Corp|Q-bop vessel construction|
    BE795117A|1973-02-07|1973-05-29|Centre Rech Metallurgique|METHOD AND DEVICE FOR THE CONVERTING OF COPPERY MATERIALS|US4652917A|1981-10-28|1987-03-24|Honeywell Inc.|Remote attitude sensor using single camera and spiral patterns|
    JPH0350807B2|1983-09-30|1991-08-02|Nippon Mining Co|
    JPH0350806B2|1983-09-30|1991-08-02|Nippon Mining Co|
    JPS60114528A|1983-11-25|1985-06-21|Sumitomo Metal Mining Co Ltd|Operating method of copper converter or cylindrical copper refining furnace|
    US5374298A|1990-11-20|1994-12-20|Mitsubishi Materials Corporation|Copper smelting process|
    MY110307A|1990-11-20|1998-04-30|Mitsubishi Materials Corp|Apparatus for continuous copper smelting|
    AU647207B2†|1990-11-20|1994-03-17|Mitsubishi Materials Corporation|Process for continuous copper smelting|
    CA2041297C|1991-04-26|2001-07-10|Samuel Walton Marcuson|Converter and method for top blowing nonferrous metal|
    US5435833A|1993-09-30|1995-07-25|L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude|Process to convert non-ferrous metal such as copper or nickel by oxygen enrichment|
    ES2245525B1|2002-01-11|2007-03-16|Atlantic Copper, S.A.|Controlling copper matte converters, for producing blister copper, by controlling start of blowing and flow of air introduced to mimimize gas and solid emission|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/024,243|US4238228A|1979-03-27|1979-03-27|Non-ferrous metal treatment|
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