会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • METHOD FOR CONTROLLING COOLING
    • JPH06108166A
    • 1994-04-19
    • JP25690992
    • 1992-09-25
    • NIPPON KOKAN KK
    • TAMURA KAZUTAKAHONDA AKIYOSHITAGUCHI NOBORU
    • C21D9/573C21D11/00
    • PURPOSE:To restrain the strip temp. from exceeding the allowance range in a cooling zone and to improve the quality of a product by securing the stable cooling capacity operation while effectively utilizing a CC zone having a small cooling capacity in spite of various kind conditions of a material to be cooled. CONSTITUTION:In the cooling control method for cooling the material 2 to be cooled in the rapid cooling (GJC) zone using cooling gas blow 11 and the slow cooling (CC) zone using a cooling tube 12, when the cooling capacity of the material to be cooled passing through the slow cooling zone is lower than the max. furnace hearth load in the preset slow cooling zone, the strip temp. on the outlet side of the rapid cooling zone is controlled basing on the relation being almost proportional to the CC zone furnace hearth load. When the cooling capacity of the material to be cooled passing through the slow cooling zone according to the variation, etc., of various kind conditions of the material to be cooled exceeds the max. furnace hearth load, the strip temp. on the outlet side of the rapid cooling zone is obtd. basing on the preset max. furnace hearth load to control the strip temp. on the outlet side of the rapid cooling zone.
    • 6. 发明专利
    • METHOD FOR CONTROLLING STRIP TEMPERATURE IN CONTINUOUS ANNEALING LINE
    • JPH0625756A
    • 1994-02-01
    • JP20623692
    • 1992-07-10
    • NIPPON KOKAN KK
    • TAMURA KAZUTAKAHONDA AKIYOSHIMATSUSHITA YASUSHITAGUCHI NOBORU
    • C21D9/56C21D11/00
    • PURPOSE:To keep the strip temperature jump within the permissible range without reducing the productive efficiency by rapidly changing the line speed within the permissible value when the strip size changing part passes the direct fire furnace of the continuous annealing line. CONSTITUTION:A strip 2 where the head end of the succeeding coil is welded to the tail end of the preceding coil is carried into a direct fire furnace 1 and heated and then, passed into a soaking furnace or the like to apply the necessary thermal cycle. The strip size changing part such as the strip thickness and the strip width is detected, the jumping quantity of the strip temperature on the furnace outlet side is calculated by a strip temperature control device 7. When this quantity exceeds the lower or upper permissible value of the strip temperature, the jumping quantity of the strip temperature is re-calculated by making an assumption that the line speed is arbitrarily changed while the strip is passing through the direct fire furnace 1. If the strip temperature when the jump of the strip temperature is observed is within the strip temperature permissible value, the strip temperature controlling device 7 gives an order to a line drive control device 9 so that the rapid change may be made to the corrective line speed which can control the strip temperature jump when the size changing part comes in the vicinity on the outlet side of the direct fire furnace 1.
    • 7. 发明专利
    • AUTOMATIC CONTROLLER FOR HOT-DIPPING DEPOSITION
    • JPH0617218A
    • 1994-01-25
    • JP5852793
    • 1993-03-18
    • NIPPON KOKAN KK
    • KUNISHIMA YUJIIRIE KATSUHIROHONDA AKIYOSHI
    • B05B12/00C23C2/16
    • PURPOSE:To automatically control the plating amts. of a molten metal on the front and rear surfaces of a steel strip by controlling the shifts of gas ejection nozzles for controlling the molten metal deposition and the pressure of gas by the deviation between the set value of the plating deposition and the actually measured value of the deposition at the time of plating the steel strip with the molten metal. CONSTITUTION:The amts. of the molten metal sticking to the front and rear surfaces of the steel strip 3 stuck with the molten metal on the surfaces by passing the inside of a bath cell 1 for hot dipping are adjusted by the injection of the gas from a pair of the nozzles 2 and thereafter, the deposited amts. of the plating metal are actually measured with a plating deposition meter 4. The measurement signals 41 obtd. in such a manner are inputted to a feed forward controller and a feedback controller 7. The measurement signals 41 of the molten metal deposition and the signal 81 from a plating deposition setter 8 are compared and a set signal 71 of a nozzle injection pressure is outputted in accordance with the deviation therebetween. The gas injection pressure from the nozzles 2 is regulated by a pressure regulator 9. The shift quantity of the nozzles is controlled with an angle controller 12 by the deviation between the ratio of the set plating deposition on the front and rear of the steel strip 3 and the ratio of the actual plating deposition and the actual value of the deposition on the front and rear of the steel strip.
    • 8. 发明专利
    • METHOD FOR CONTROLLING ALLOYING DEGREE OF GALVANIZED STEEL SHEET
    • JPH08269669A
    • 1996-10-15
    • JP7797995
    • 1995-04-03
    • NIPPON KOKAN KK
    • YAMAUCHI KENJIHONDA AKIYOSHITAGUCHI NOBORU
    • C23C2/28F27D11/06F27D19/00H03M20060101
    • PURPOSE: To control the alloying degree in continuous galvanizing in an adequate range by controlling alloying electric power to the value determined by functions, of steel kind, sheet thickness, sheet width, line speed, deposit and alloying degree. CONSTITUTION: A continuously transported steel strip is subjected to galvanizing and after the steel strip is adjusted to the prescribed deposit of plating, the plating is alloyed in an induction heating and alloying furnace. At this time, the alloying electric power is controlled to the value obtd. by the conditions of the equation which is the relation among the steel kind, sheet thickness, sheet width, line speed, deposit and alloying degree. In the equation, a0 to a5 are the constants given by each of the steel kinds. Further, the alloying degree after alloying is measured online and is substd. into the equation which count back a model error. Calculation with high accuracy is executed by taking this model error as a correction factor into consideration at the time of setting the electric power. As a result, the electric power setting of the alloying furnace is automated and the optimum alloying state is obtd. from the coil top part and, therefore, the length parts of the alloying defect are drastically decreased and the yield is improved.
    • 10. 发明专利
    • METHOD FOR CONTROLLING SHEET TEMPERATURE IN CONTINUOUS ANNEALING FURNACE
    • JPH0192322A
    • 1989-04-11
    • JP24733487
    • 1987-09-30
    • NIPPON KOKAN KK
    • KAWAKAMI MASAAKIHONDA AKIYOSHI
    • C21D9/56C21D11/00
    • PURPOSE:To efficiently and stably control sheet temp. at the time of changing line speed by making the prescribed speed changing rate after accelerating speed and reducing speed of the metal sheet reaches the limit speed at the max. speed changing rate and on the other hand, controlling the temp. at outlet of a heating furnace to the fixed value. CONSTITUTION:At the time of changing the running speed of the metal sheet as a material to be annealed in a direct firing type continuous annealing furnace, the upper and lower limit speeds, which the temp. of the metal sheet at the outlet of the furnace comes to out of the prescribed temp. range, in the case of making the max. speed changing rate and the max. burner combustion load at the time of the accelerating speed, and in the case of making the negative and the max. absolute value of the speed changing rate and the min burner combustion load at the time of the reducing speed, are found respectively. Further, the limit speed changing rates under conditions, which the burner combustion loads are the max. and the min in the case of being more than the above upper limit speed at the time of accelerating speed and in the case of being less than the above lower limit speed at the time of reducing speed, are found, respectively. Next, the running speed of the metal sheet is accelerated or reduced at the above speed changing rate till the running speed reaches the above limit speed, respectively. In the case of being more than or less than the above limit speed changing rate, respectively. On the other hand, the temp. control of the outlet of the heating furnace is executed by the fixed value control independently to the running speed of the metal sheet. By this method, lowering of the line efficiency at the time of changing the speed is prevented.