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
    • 2. 发明专利
    • Method for controlling pelletization of sintering raw material
    • 控制烧结原料粉末的方法
    • JPS62116727A
    • 1987-05-28
    • JP25568485
    • 1985-11-14
    • Kobe Steel Ltd
    • MURATA HIROYUKIMIZUKAMI SHUNICHITOKUKASA KUNIHIKOITO RYOJISHIBUTA KATSUHIKO
    • C22B1/16
    • PURPOSE: To quickly find out exact pelletization conditions by solving the material balance equation into which a pelletization speed function is incorporated for each of grain sizes, estimating the change of the grain size distribution of pelletized particles with time and adjusting the conditions for pelletizing raw materials and the conditions for operating pelletization.
      CONSTITUTION: The pelletization speed function to express the propability at which the particles meeting each other in a pelletizing machine combine each other is incorporated into the material balance equation to express the grain size distribution according to the progression of the pelletization. The equation is solved for each of the grain sizes to estimate the change of the grain size distribution with time according to the growth of the pelletized particles. The grain size distribution after the execution of the prescribed pelletization stage is determined from the estimated value. The conditions for the pelletizing raw materials and the conditions for operating the pelletization are adequate if the grain size distribution obtd. in such a manner coincides with the standard value. The conditions forthe pelletizing raw materials and the conditions for operating the pelletization are returned to a setting stage and the new conditions are set when the grain size distribution does not coincide with the standard value. The similar operations are thereafter carried out and the operations are repeated until the calculated value coinciding with the target grain size distribution is obtd.
      COPYRIGHT: (C)1987,JPO&Japio
    • 目的:为了快速找出准确的造粒条件,通过求解每种晶粒尺寸引入造粒速度函数的材料平衡方程,估算造粒颗粒的粒度分布随时间的变化,并调整造粒原料的条件 以及运行造粒的条件。 构成:在造粒机中彼此相遇的颗粒彼此结合的表达粒子速度函数被结合到材料平衡方程中以根据造粒的进展来表示粒度分布。 针对每个晶粒尺寸求解该方程,以根据粒化颗粒的生长来估计晶粒尺寸分布随时间的变化。 根据估计值确定执行规定的造粒阶段之后的粒度分布。 如果颗粒尺寸分布受到限制,原料造粒条件和操作造粒条件就足够了。 以这种方式与标准值一致。 原料造粒条件和造粒条件恢复到凝固阶段,当粒度分布与标准值不一致时,设定新条件。 此后进行类似的操作,并重复操作,直到计算出的值与目标粒度分布一致为止。
    • 3. 发明专利
    • CYCLONE FOR DUST REMOVAL FROM HIGH TEMPERATURE EXHAUST GAS
    • JPS6427656A
    • 1989-01-30
    • JP18427987
    • 1987-07-23
    • KOBE STEEL LTD
    • MIZUKAMI SHUNICHIHIROSE JUN
    • B04C5/22B04C5/18
    • PURPOSE:To enable secure removal of accumulated material stocking to the internal wall surface of a cyclone for dust removal from high temperature exhaust gas by providing an impact particle supply device in the lower half of the cyclone and introducing impact particles into the cyclone. CONSTITUTION:In a cyclone 3 for removal of dust from exhaust gas released from a melting-reducing furnace, for instance, a supply port 20a for charging impact particles 29 is provided in the almost intermediate stage position of a conical part 3b. When the impact particles 29 are charged into the cyclone 3 through the supply port 20a, the impact particles 29 hit the inner wall surface of the cyclone 3, while gyrating, to knock of accumulated material sticking to the wall surface and to drop it into the hopper 8, so that a connection with the hopper 8 is not clogged with the adhering accumulated material. As dust contained in the gas generated in the melting and reducing furnace sticks to the lower part of the conical section 3b concentratedly, the supply port 20a for the impact particles 29 is arranged at a point lower front the middle stage of the conical section 3b to assure secure removal of the accumulated material.
    • 4. 发明专利
    • METHOD FOR MOLDING FIBER REINFORCED COMPOSITE MATERIAL
    • JPS63306013A
    • 1988-12-14
    • JP14191587
    • 1987-06-06
    • KOBE STEEL LTD
    • MATSUSHITA TOMIHARUHATTORI SHIGEOOSUNA HIROSHIMIZUKAMI SHUNICHI
    • B29C45/00B29C45/18B29C45/74
    • PURPOSE:To make it possible to prepare mixture with stable quality without fear such as dust explosion and the like due to fine dust-size particle by a method wherein granular mixture is produced by granulating slurry-like mixture into granules after being subjected to liquid extraction. CONSTITUTION:Slurry-like mixture, which is produced by mixing wiskers and matrix metal powder with organic solvent, is liquid extracted. After that, by adding with binder and kneading said mixture is granulated into granules having the diameter of about 0.5-1 mm so as to obtain granular mixture 2 by drying in order to feed to an injection molder 20 under vacuum atmosphere. The matrix metal is heated up to a temperature, at which both the solid phase and liquid phase of the metal are present each other, or higher in the gap between an injection cylinder barrel 11 and a screw rotor 12 of the molder. At the same time, the matrix metal is injection-molded from the injection nozzle of the molder into a mold so as to obtain a molded item with required shape. Further, in order to dry the granular mixture 2, the mixture is dried by being heated up to a temperature near the melting point of the matrix metal. Furthermore, after being injected in the mold, the matrix metal is compressed with the mold in order to obtain the molded item.
    • 6. 发明专利
    • METHOD FOR REFORMING GAS GENERATED IN MELT REDUCTION FURNACE AND REMOVING DUST THEREFROM
    • JPS62205208A
    • 1987-09-09
    • JP4688286
    • 1986-03-04
    • KOBE STEEL LTD
    • MIZUKAMI SHUNICHIAOKI MAMORUKOBAYASHI ISAOITO SHUZOHIKOSAKA AKIHIDEKIKUCHI SHOICHI
    • C21B13/00C21B13/14
    • PURPOSE:To increase the reduction potential of a secondary combustion gas and making effective reutilization of the gas for preliminary reduction of iron ore by subjecting the gaseous CO generated at the time of supplying the iron ore subjected to the preliminary reduction in a preliminary reduction furnace to a melt reduction furnace and producing a molten iron to secondary combustion then supplying the same together with a reducing agent into a cyclone. CONSTITUTION:The powdery iron ore 3 and the CO-contg. gas formed by decreasing the temp. of the high-temp. reducing gas from a cyclone separator 13 to about 850 deg.C by utilizing the heat of a boiler are supplied to the preliminary reduction furnace 1 to preliminarily reduce the powdery iron ore. Such molten iron is then added into the melt reduction furnace 2. Pulverized coal 6 and oxygen 8 are supplied into the furnace 2 to thoroughly reduce the preliminarily reduced iron ore by heating and melting to form the molten iron. The CO in the reaction gas generated in this stage is burned by the oxygen 8 to increase the temp. of the molten iron and thereafter the CO is put together with hydrocarbon such as CH4 into the cyclone separator 13 to form CO+H2 and to restore the reduction potential; thereafter, the gas is utilized as the reducing gas to the furnace 1 via the boiler 18. The Fe-contg. dust emitted from the cyclone 13 is supplied to the furnace 2.