• 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 process for heating a molten material by injecting oxygen and a fuel into a molten bath of the material at a bath temperature above the spontaneous combustion temperature of the fuel, at least a portion of the fuel forming a shroud around the oxygen, and combusting the fuel to provide heat to the molten material. Where the molten material is impure copper the amount of oxygen and fuel injected may also be controlled to alternately oxidize and reduce the copper impurities and remove them from the bath. Solid material may be melted in the bath during any stage of heating or refining. In a preferred embodiment, a portion of the fuel forms a shroud around the oxygen during injection, and the oxygen forms a shroud around the remaining fuel.
    公开号:SU1591816A3
    申请号:SU864028469
    申请日:1986-10-24
    公开日:1990-09-07
    发明作者:Yan Frensis Masterson；Devid Bechtel Dzhordzh；Frederik Allan Rudloff
    申请人:Union Carbide Corp；
    IPC主号:
    专利说明:

    The invention relates to the technology of refining blister copper.
    The purpose of the invention is to increase the productivity of the process and increase the degree of heat utilization.
    Example 1. 225 short tons (204 metric tons) of molten blister copper are introduced into the anode furnace. The initial levels of sulfur and oxygen are 0.022 and 0.1933%, respectively. venno.
    Oxygen and natural gas are blown into the bath with a volume flow rate of 2/1. Costs are 400 ft 3 / min (11.3 m 3 / / min) for oxygen and 200 ft 3 / min ·
    (5.7 m 3 / min) natural gas. Double-screen tuyeres are used, and
    2
    (57) The invention relates to the refinement of blister copper. The purpose of the invention is to increase the productivity of the process. The method is carried out in such a way that the molten material'- copper, containing impurities, is processed so that the amount of acid, rock and fuel can be adjusted in order to alternately oxidize and restore copper impurities and remove them from the bath. The solid material can be melted in the bath during the heating or refining phase. In a preferred embodiment of the invention, part of the fuel forms a screen around oxygen during its introduction and oxygen forms a screen around the rest of the fuel.
    45% of natural “gas is injected through the outermost channel, and the rest is · ο through the central channel. Oxygen is introduced through the internal annular canal. The injection lasts 37 minutes. During this time, 9.6 short tons (8.7 metric tons) of scrap are added in parts and melted in a bath, the temperature rises from 2042 ° P (1116 * 0 to 2055-2100 *
    (1124-1150 ° C). During this initial: hydrochloric blowdown heat recovery was 95%, After purging sulfur and oxygen is 0.003% and 0.270%, respectively.
    Then 167 ft 3 / min
    (4.7 m 3 / min) oxygen and 250 ft 3 / min
    zi '1591816 AZ
    3
     1591816
    four
    (7.1 m 3 / min) natural gas for 2/3 volumetric flow ratios. The second purge is continued for 52 minutes. During this time, 5.4 tons of rotary tons (4.9 metric tons) of copper scrap are added and melted at a bath temperature of 2057-2148 ° Р (1125-1176 ° С). The achievable heat recovery for this period is 93%, while the efficiency of deoxidation is 60%. The oxygen content drops to 0.093%.
    At this moment, 72 short tons (66 metric tons) of copper are released from the furnace and cast into the anodes. The levels of sulfur and oxygen in the cast anodes are 0.003 and 0.11%, respectively.
    The rest of the molten mixture is blown a third time with a volume ratio of 2 θ for oxygen and natural gas consumption of 2/1. Volumetric flow rates are 400 ft 3 / min (11.3 m 3 / min) for oxygen and 200 ft 3 / min
    (5.7 m 3 / min) for natural gas. Three-25 purging continues for 71 minutes, during which 17 short tons (15.5 metric tons) of scrap are dissolved at a bath temperature of 2064-2145 ° (1129-11 / 4 ° С). Heat utilization in this period is 96%, the oxygen content increases to 0.13%. ·
    Fourth purge 300 ft3 / min (8.5 m 3 / min) of oxygen and 200 ft3 / min (5.7 m 3 / min) of natural gas osuschest- vlyayut 33 for 66 min (the volume ratio of oxygen and natural gas
    -3/2). In total, 13 short tons (11.8 metric tons) of scrap 40
    are swimming during this purge. The oxygen content is reduced to 0.068, attainable utilization was 94%.
    The fifth and final purge of 167 ft 3 / / min (4.7 m 3 / min) oxygen and 250 ft 3 / min (7.1 m 3 / min) natural gas is carried out for 48 min (volume flow of oxygen in relation to natural gas is 2/3)
    During this purge, 12 short tons (10.9 metric 3 θ tons) of scrap are added. The final oxygen content of 0.032%, achievable heat recovery of 94%.
    Example 2. 161 short tons (147 metric tons) of molten copper blister, containing 0.265% oxygen and 0.0096% sulfur, are loaded into an anode furnace. Oxygen and natural
    the gas is introduced into the molten bath at a volume ratio of 2/1, oxygen with a flow rate of 400 ft 3 / min (11.3 m 3 / min) and natural gas - 200 ft 3 / min (5.7 m 3 / min). Double-screen tuyeres are used, with 35% of all natural gas being injected through the outermost annular channel, tuyeres, and the remaining 65% through the central channel.
    Within 96 minutes of purging at the indicated ratio, 16 short tons (14.6 metric tons) of scrap are added and melted in a bath. Bath temperature rises from 1980 ° (1082 ° C) to 2090 ° (1143 ° C). The calculated amount of heat utilization for this period is 97%. The oxygen content in the bath is reduced to 0.233%, and the sulfur content is reduced to 0.0004%.
    Oxygen and natural gas are then injected into the bath at a volume flow rate of 2/3, with oxygen consumption 1-67 ft 3 / min (4.7 m 3 / min), natural gas consumption 250 ft 3 / min (7.1 m 3 / min) After 40 minutes of blowing at this ratio the oxygen content is reduced to 0.071% and bath temperature increased from 2060 * (1127 ° C) to 2106 F F (1152 C). During this period, the calculated amount of heat utilization is 98% and the deoxidation efficiency is 68%. In addition, no soot in the exhaust gases is not detected and the opacity of the gases is on average 15%.
    Example 3. 239 short tons (217 metric tons) of molten blister copper containing .0.342% oxygen and 0.276% sulfur are loaded into an anode furnace. Air is introduced into the molten bath at a rate of 500 Ft 3 / min (14.2-m 3 / min.) Using double-shielded tuyeres. After 70 minutes of purging with air at the indicated flow rate, the sulfur content is reduced to 0.0050% and the oxygen content is from 0.342% to 0.354%.
    Oxygen and natural gas are then injected into the bath at a volume flow rate of 2/3, with 167 ft 3 / min (4.7 m 3 / min) of oxygen being consumed and 250 ft 3 / min (7.1 m 3 / min) of natural gas . The double-screen tuyeres are again used, with 41% of natural gas being fed through the outermost annular channel. For 81 minutes purging at the indicated proportions
    5 159181
    .8 short tons (7.3 metric tons) of scrap are added and melted. The oxygen content of the bath decreases from 0.354 to 0.080%, and the temperature of the bath increases from 2127 ° G (1164 ° C) $ to 2142 ° G (1172 ° C). During this time, the calculated heat recovery is 15%.
    Example 4. 197 short tons (179 metric tons) of molten blister copper containing 0.289% oxygen and 0.0010% sulfur is loaded into the anode furnace. Oxygen and natural gas are introduced into the bath at a volume ratio of 2/1, with 400 ft 3 / min (11.3 m 3 / min) of oxygen and 200 ft 3 / min (5.7 m 3 / min) of natural gas being consumed. A double-screen tuyere is used, with 45% of natural gas being injected through 20
    the outermost annular channel.
    Within 42 minutes of purging at the specified ratio, 12 tons of scrap are added and melted in a bath. Bath temperature rises from 2073 ° P 25
    (1134 ° С) up to 2142 ° Р (1172 ° С), and the calculated heat utilization is 93%.
    Oxygen and natural gas are introduced into the bath at a flow ratio of 1/1, with oxygen consumption being 300 ft 3 / min (8.5 m 3 / min), and natural gas - .400 ft 3 / min (8.5 m 3 / min) After 43 minutes of purging at this ratio, 6 short tons (5.5 metric tons) of melt are melted and the bath temperature rises from 2062 ° P (1128 ° C) to 2128 ° P (1164®С).
    Dawn heat utilization during this time is 88%, the oxygen content of the bath is reduced to 0.185%,
    Oxygen and natural gas are introduced into the bath at a flow ratio of 2/3, and they consume 167 ft 3 / min (4.7 m 3 / min) oxygen and 250 ft 3 / min (7.1 m 3 / min) natural gas. 39 minutes after purging at these ratios, the bath temperature increases from 2070 ° K (1132 ° C) to 2106 ° P (1 152 ° C) and the oxygen content of the bath decreases from 0.185 to 0.064%. Heat recovery for this period is 92%, deoxidation efficiency is 64%, and opacity of exhaust gases is on average 15%.
    Examples .5 and 6 illustrate the practical implementation of the proposed method using single-screen tuyeres, while the liquid fuel6 6
    it is introduced into the outer annular channel, and oxygen is supplied through the central channel.
    Example 5. 189 short tons (172 metric tons) of molten blister copper containing 0.360% oxygen and 0.0207% sulfur are loaded into an anode furnace. Oxygen and natural gas are fed to the bath at a ratio of volumetric flow rates of 4/3, and consume 400 ft 3 / min (11.3 m 3 / min) of oxygen and 300 ft 3 / min (8.5 n 3 / min) of natural gas.
    Within 74 minutes of purging at this ratio of 5.3 short tons (4.8 metric tons) scrap is loaded and melted in a bath. The bath temperature increases from 2079 ^ 1 1 (1137 ° С) to 2138 ° Г (1170 ° С). The calculated heat utilization during this time is 60%. The oxygen content of copper is reduced to 0.316%, and the sulfur content is reduced to 0.0075%.
    Oxygen and natural gas are then injected into the bath at a volume flow rate of 2/3, with 200 foot 3 / min (5.7 m 3 / min) of oxygen and 300 foot 3 / min (8.5 m 3 / min) of natural gas being consumed . After 61 minutes after purging at this ratio, the temperature of the bath increases from 2094 ° G (1146 ° C) to 2137 ° P (1170 ° C). Heat recovery is 71%. During this time, the oxygen content of the bath is further reduced to 0.031%. The efficiency of deoxidation is 62%.
    Example 6. 222 short tons (202 metric tons) of molten blister copper containing 0.319% oxygen and 0.01646% sulfur are loaded into an anode furnace. Oxygen and natural gas are injected into the molten bath with
    d 3 using single-screen tuyeres. Consume 400 ft 3 / min (11.3 m 3 / min) of oxygen and 300 ft 3 / min (8.5 m 3 / min) of natural gas. During the 98 min purge with sootno50 shenii 6 short tons (5.5 "metric tons) of scrap were added and melted. The bath temperature increases from 2067 ° F (1131 ° C) to 2135 ° F (1168 C th), and the oxygen content reduced to 0.274%. Calculated heat recovery over the echo period is 73%.
    Oxygen and natural gas then
    injected into the molten bath at a ratio of volumetric flow rates of 2/3 during 7
    1591816
    eight
    of 53 minutes, the oxygen flow rate is 200 ft3 / min (5.7 m 3 / mission) and natural gas - 300 ft 3 / min (8.5 m 3 / min). During this period the bath temperature increased from 2120 e F (1160 ° C) to 2150 ° F (1177 ° C), and heat recovery is 71%, the oxygen content of the bath is further reduced to 0.064%, the deoxidation efficiency was 70%.
    权利要求:
    Claims (1)
    [1]
    Claim
    The method of refining blister copper containing oxygen and oxidized impurities using oxygen and fuel, including creating a metal bath, melting it, heating to a temperature above the spontaneous ignition temperature of the fuel, introducing oxygen and fuel below the bath surface through a lance, controlling the oxygen consumption within more than 150% of the amount required for complete combustion of the fuel, adding solid copper to the melt and melting it, maintaining the bath temperature not lower than 1090 ° С, which is different from that that, in order to improve the performance of the process and the degree of heat utilization, a part of the fuel is fed into the copper melt by a ring stream, surrounding oxygen introduced into the copper melt, and this part of the fuel amounts to 10-50 wt.% of the total fuel introduced through the lance, or all fuel is supplied to the copper melt by an annular stream surrounding oxygen introduced into the copper melt, or fuel and oxygen are supplied to the copper melt by alternating annular streams, or oxygen introduced into the copper melt is supplied by an annular stream surrounding the fuel.
    类似技术:
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    同族专利:
    公开号 | 公开日
    EP0225998B1|1990-03-28|
    US4657586A|1987-04-14|
    KR870004155A|1987-05-07|
    KR910009873B1|1991-12-03|
    CA1290943C|1991-10-22|
    MX165182B|1992-10-30|
    CN1010032B|1990-10-17|
    FI864330A|1987-04-26|
    FI83096B|1991-02-15|
    CN86107592A|1987-09-09|
    EP0225998A1|1987-06-24|
    JPS62174337A|1987-07-31|
    ZA868120B|1987-09-30|
    ZM9786A1|1988-08-29|
    JPH032215B2|1991-01-14|
    FI864330A0|1986-10-24|
    BR8605228A|1987-07-28|
    PH23754A|1989-11-03|
    AU581542B2|1989-02-23|
    AU6437386A|1987-04-30|
    DE3669891D1|1990-05-03|
    ES2013592B3|1990-05-16|
    FI83096C|1991-05-27|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/791,514|US4657586A|1985-10-25|1985-10-25|Submerged combustion in molten materials|
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