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    • 2. 发明专利
    • METHOD AND APPARATUS FOR PRODUCING SEMI-CARBONIZED COKE
    • JPS60177094A
    • 1985-09-11
    • JP3173984
    • 1984-02-22
    • SUMITOMO METAL IND
    • TAKATANI KOUJI
    • C10B57/02
    • PURPOSE:To obtain semi-carbonized coke, in high thermal efficiency, without causing the cracking of the coke, by partially carbonizing green briquette utilizing the sensible heat of the gas exhausted from a reducing furnace after the reduction of iron ore, and carbonizing the briquette again with a hot reducing gas. CONSTITUTION:The fuel blasted through the tuyere 4 is converted to a hot gas composed mainly of CO and H2 in the coke layer (b), transferred upward through the gaps in the layer (b) to melt the partially reduced iron, etc., and recovered from the gas-outlet port 3 as a hot reducing gas. At the same time, the produced molten iron, etc. is made to contact countercurrently with the ascending gas in the gaps, and the iron oxide in the molten slag is reduced with coke to molten iron. The produced molten iron and slag are discharged through respective discharging port. The gas 12 composed mainly of CO and H2 and taken out through the outlet port 3 is blasted into the iron ore reducing furnace 14 and the recarbonization furnace 17 for the semi-carbonized coke to reduce the iron ore 15 in the reducing furnace 14. The gas 18 exhausted from the reducing furnace is used for the partial carbonization of the green briquette.
    • 4. 发明专利
    • Method for measuring flow rate of powder body
    • 测量粉体体积流量的方法
    • JPS59108917A
    • 1984-06-23
    • JP21979182
    • 1982-12-14
    • Sumitomo Metal Ind Ltd
    • TAKATANI KOUJIMIYAZAKI TOMIO
    • G01F1/74G01F1/86
    • G01F1/74
    • PURPOSE:To measure the flow rate of a powder body stably and highly accurately, by detecting the pressure loss of the mixture of the powder body and a carrier gas when the mixture passes a bent pipe part, detecting the flow rate of the carrier gas, and computing the flow rate of the powder body. CONSTITUTION:A powder body, which is supplied to a straight pipe part 3a of a transporting pipe 3, is carried by a carrier gas, which is supplied through a carrier gas supplying pipe 4, and sent to a required place through a bent pipe part 3b. An operating part 9 reads a pressure loss DELTAPSG of a solid and gas mixture fluid at the bent pipe part 3b from a differential pressure gage 5, and also reads the pressure, temperature, and flow rate of the gas from a pressure gage 6, a thermometer 7, and a flowmeter 8. The operating part 9 computes the pressure loss DELTAPG of the gas at the bent pipe part 3b and the mass flow rate WG of the gas. Since DELTAPSG/PG is the function of only a ratio (m) between the mass flow rate WS of the solid and the mass flow rate WG of the gas, the mass flow rate (m) (a) is computed by a specified conversion expression, and the mass flow rate WS of the powder body is computed.
    • 目的:为了通过检测混合物通过弯管部分时的粉末体和载气的混合物的压力损失,通过检测载气的流量,可以稳定,高精度地测定粉体的流量, 并计算粉体的流量。 构成:供给到输送管3的直管部3a的粉体由通过载气供给管4供给的载气承载,并通过弯管部送出到所需要的位置 3B。 操作部9从差压计5读出弯曲管部3b处的固体和混合气体的压力损失DELTAPSG,并且还从压力计6读取气体的压力,温度和流量 温度计7和流量计8.操作部9计算弯管部3b处的气体和气体的质量流量WG的压力损失DELTAPG。 由于DELTAPSG / PG只是固体质量流量WS与气体的质量流量WG之间的比值(m)的函数,所以通过规定的转化表达式计算出质量流量(m)(a) ,并计算粉体的质量流量WS。
    • 5. 发明专利
    • GAS DISPERSER FOR COAL LIQUEFACTION TOWER
    • JPS5996188A
    • 1984-06-02
    • JP20528082
    • 1982-11-22
    • SUMITOMO METAL IND
    • TAKATANI KOUJIHAYAKAWA KEIICHI
    • C10G1/08B01J8/00B01J8/44
    • PURPOSE:To improve the efficiency of gas dispersion and increase the efficiency of coal liquefaction, by using rings having a diamond-shaped crosssection with a specified vertical angle as hydrogen gas dispersers for a coal liquefaction tower. CONSTITUTION:Rings 3, 3 having a diamond-shaped crosssection with a vertical angle larger than 60 deg. are attached as gas dispersers to form a concentric circle, with a cone 4 being positioned in the center, at a desired height of a reaction tower 2 for hydrogenation and liquefaction of raw material slurry consisting of coal particles, solvent, catalyst particles, etc. at high temperature and under high pressure. The raw material slurry and hydrogen gas are blown into the reactor 2 through a one-orifice nozzle 1 to disperse the hydrogen gas evenly by means of the ring 3 and perform hydrogenation and liquefaction of the raw material slurry. The ring disperser 3 of the above specified shape has a higher gas dispersion efficiency than rings having circular and oval crosssections or a diamond-shape crosssection with a vertical angle smaller than 60 deg..
    • 7. 发明专利
    • Method and apparatus for prevention of entrapment of gas in decanter
    • 用于防止气体在气瓶中的侵入的方法和装置
    • JPS59202290A
    • 1984-11-16
    • JP7554883
    • 1983-04-28
    • Sumikin Coke Co LtdSumitomo Metal Ind Ltd
    • NAKANO HISAOTAKATANI KOUJI
    • C10C1/00C10B27/00
    • PURPOSE: To prevent entrapment of gas bubbles under a liquid level, by changing the flow of a mixture of coal tar and liquid gas from a suction main of a coke oven to a horizontal direction near the level of sealing liquid at the bottom of an inlet pipe and by decreasing the rate of settlement.
      CONSTITUTION: A mixture of coal tar and liquid gas is introduced from a downcomer 2 of a suction main 1 of a coke oven through an inlet pipe 3 into the top of a large-diameter sealed pipe 4 welded to the ceiling of a tar decanter 5 and a vertical flow of the mixture is deflected to a horizontal direction by means of a buffer 10 affixed to a support 6 arranged radially on the underside of a brim 8 mounted on a flange 6 of a short pipe 7 affixed to the upper side of the periphery of an opening made in the ceiling of the decanter 5. The mixture is allowed to fall on the sealing liquid level and settle down at a rate of 3cm/sec or lower.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了防止在液面下夹带气泡,通过将煤焦油和液体气体的混合物从焦炉的吸入主体的流动改变到接近入口底部的密封液体水平的水平方向的流动 管道和降低沉降率。 构成:将煤焦油和液体气体的混合物从焦炉的吸入主体1的降液管2通过入口管3引入焊接到焦油倾析器5的顶部的大直径密封管4的顶部 并且混合物的垂直流动通过固定在径向上布置在安装在固定在上游侧的短管7的凸缘6上的边缘8的下侧的支撑件6上的缓冲器10偏转。 在滗水器5的天花板上形成的开口的周边。允许混合物落在密封液体水平上并以3cm / sec或更低的速率沉降。
    • 8. 发明专利
    • Powdered material supplying method
    • 粉末材料供应方法
    • JPS5974822A
    • 1984-04-27
    • JP18195582
    • 1982-10-15
    • Sumitomo Metal Ind Ltd
    • TAKATANI KOUJIMIYAZAKI TOMIO
    • G01F1/74B65G53/40B65G53/66
    • B65G53/40
    • PURPOSE:To make it possible to stably supply a prescribed amount of powdered material by controlling the number of revolutions of a rotary type exhaust valve and the real volume flow rate of gas for aeration so as to set the raried amount of weight of the powdered material in a tank to a prescribed value. CONSTITUTION:Powdered material is supplied from a throwing-in tube 22 into a storage tank 20, and further supplied to a transporting tube 27 by a rotary discharge valve 26 provided on the intermittent feed part 25 of the tank 20. In this case, a weight detector 28 is provided on the load supporting part of the tank 20, a signal from which is fed to a differentiator 29, and converted to a differential value representing the flow rate of the powdered with material. Moreover, a pressure detector 31a is provided near the ceiling plate 21 of the tank 20, and aeration piping 33 on a funnel part 24, and further outputs from the pressure detector 31a and the volume flowmeter 33b are fed to a regulating meter 34. And, the number of revolutions of the rotary discharge valve 26 and the opening of the flow rate adjusting valve 33a are controlled by means of a control part 30, allowing a prescribed amount of the powdered material to be supplied through the transporting tube 27.
    • 目的:通过控制旋转式排气阀的转数和用于曝气的气体的实际体积流量,可以稳定地供给规定量的粉末材料,以便设定粉末材料的稀有重量 在一个坦克到一个规定的价值。 构成:将粉状材料从投入管22供给到储罐20中,并且通过设置在罐20的间歇进料部25上的旋转排出阀26进一步供给到输送管27.在这种情况下, 重量检测器28设置在罐20的负载支撑部分上,信号被馈送到微分器29,并被转换成表示粉末状材料的流量的差值。 此外,压力检测器31a设置在罐20的顶板21附近,并且漏斗部24上的曝气管33,以及来自压力检测器31a和容积流量计33b的进一步输出被馈送到调节计34。 旋转排出阀26的转速和流量调节阀33a的开度通过控制部30进行控制,允许通过输送管27供给规定量的粉末状材料。
    • 9. 发明专利
    • Distributing method of particulate material pneumatically conveyed
    • 颗粒物质的分布方法
    • JPS58216829A
    • 1983-12-16
    • JP10102182
    • 1982-06-11
    • Sumitomo Metal Ind Ltd
    • FUKUDA TADASHISHIYOUJI YASUOTAKATANI KOUJI
    • B65G53/56B65G53/52F16L41/03
    • F16L41/03B65G53/521
    • PURPOSE: To contrive to enhance accuracy in distributing a particulate material and to reduce the abrasion of a distributor or the like, by a method wherein a particulate material being pneumatically conveyed is mixed by agitating in an expanding pipe having a specified shape, the concentration of the material is made to be uniform in a straight pipe having a specified length, and then it is directed into the distributing pipes.
      CONSTITUTION: The expanding pipe 2-1, the straight pipe 2-2 and the distributing pipes 2-3 are connected to a main pipe 1 for pneumatically conveying a particulate material, through flanges 2-4W2-6, to constitute the distributor 2. The expanding pipe 2-1 has a bend angle θ of 8W180° and an expansion ratio on an inside diameter basis of not lower than 1.3. The length of the straight pipe 2-2 is set to be 3W50 times of the open end diameter on the outlet side of the expanding pipe 2-1. The particulate material pneumatically conveyed through the main pipe 1 is expandingly dispersed in the pip 2-1, is mixed by agitating therein, the concentration thereof is made to be uniform by forming a uniform suspended particle layer in the straight pipe 2-2, and is uniformly distributed into the plurality of distributing pipes 2-3.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了提高分散颗粒材料的分布精度和减少分布器等的磨损,通过在具有规定形状的膨胀管中搅拌将气动输送的颗粒材料混合, 该材料在具有指定长度的直管中制成均匀的,然后被引导到分配管中。 构成:膨胀管2-1,直管2-2和分配管2-3连接到主管1,用于通过法兰2-4-2-6气动输送颗粒材料,以构成分配器 膨胀管2-1的弯角θ为8-180度。 内径的膨胀率为1.3以上。 直管2-2的长度设定为膨胀管2-1的出口侧的开口端直径的3-50倍。 通过主管1气动输送的颗粒材料在管道2-1中膨胀分散,通过在其中搅拌混合,通过在直管2-2中形成均匀的悬浮颗粒层使其浓度均匀,以及 均匀分布在多个分配管道2-3中。
    • 10. 发明专利
    • PRODUCTION OF PIG IRON
    • JPS5891106A
    • 1983-05-31
    • JP18982881
    • 1981-11-25
    • SUMITOMO METAL IND
    • TAKATANI KOUJIHIRAOKA FUMIAKIYAMAOKA HIDEYUKI
    • C21B11/02C21B13/14
    • PURPOSE:To provide a producing method for pig iron which makes the production up to production of hydrogen of high purity possible by the simple process of not using liquid raw materials by combining a reducing furnace for iron ore, a melting and gasifying furnace for melting the reduced iron and producing gases and a hydrogen generating furnace for producing H2 by oxidizing reduced iron with steam. CONSTITUTION:O2, steam and puluertzed coal are blown through a tuyere 1 into a combustion chamber (a), and the combustion gases consisting essentially of CO, H2 formed by said blowing are run into a melting part (b) where reduced iron is melted and discharged 4 therefrom. The molten reduced iron is subjected to carburizing and SiO2 reduction reaction in the part (b) and is discharged 6 through a well 5 together with slag. On the other hand, the above-described gas to be discharged 4 from a melting and gasifying furnace A is supplied 7 to a moving bed type reducing furnace B, and the reduced iron is dispensed from a dispensing device 10. Part thereof is supplied to a moving bed type hydrogen producing furnace (c) and the balance to the furnace A, respectively. In the furnace (c), the reduced iron is oxidized by the steam entering 11 the furnace to recover the formed H2 and to circulate the same to the furnace B for recirculation.