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    • 2. 发明专利
    • Manufacture of briquette containing carbonaceous material
    • 含有炭黑的材料的制造
    • JPS59123728A
    • 1984-07-17
    • JP23465882
    • 1982-12-27
    • Kobe Steel Ltd
    • NOZAKI TERUHIKOKOIZUMI HIDEONISHIDA REIJIROUKANEKO DENTAROU
    • C22B1/14
    • PURPOSE: To manufacture a starting material for iron manufacture having strength and reducibility and causing hardly rolling in a furnace by mixing fine iron ore and a carbonaceous material with a binder under specified conditions, press-molding the mixture into briquettes, and solidifying the briquettes by heating.
      CONSTITUTION: Cement free from sulfur or a heat curing agent is added to a mixture of fine iron ore contg. 60W70% grains of ≤about 44μm grain size with a carbonaceous material almost free from ash and sulfur. They are kneaded, and the kneaded material is press-molded into briquettes with a briquetting machine. The briquettes are solidified by heating at ≤about 500°C. The resulting briquettes hold proper strength in an iron manufacturing furnace and has high reducibility at low and high temps. Since the briquettes are not spherical, they hardly roll in the furnace.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了制造具有强度和还原性的铁制原料,在特定条件下,通过将细铁矿石和碳质材料与粘合剂混合,在炉内难以轧制,将混合物压制成块状,并将该团块固化 加热。 构成:将不含硫或热固化剂的水泥加入到细铁矿石混合物中。 60-70%的颗粒大小约为44μm,碳质材料几乎不含灰分和硫。 将它们捏合,并用压块机将捏合的材料压制成块。 通过在<=约500℃加热而将团块固化。 所得到的团块在铁制造炉中保持适当的强度,并且在低温和高温下具有高的还原性。 由于团块不是球形,它们几乎不在炉中滚动。
    • 5. 发明专利
    • MANUFACTURE OF REDUCED IRON
    • JPS5834114A
    • 1983-02-28
    • JP13178381
    • 1981-08-21
    • KOBE STEEL LTD
    • ARIKAWA MASAYASUMORI KENJINARITA KIICHIKANEKO DENTAROUKAMIMURA NOBUOMIYAZAKI KAZUHIRO
    • C21B13/00
    • PURPOSE:To expand width of utilized hydrocarbon, to manufacture reduced gas at a low cost and easily, and to realize high temperature reduction, by placing in series a spare reducing furnace of a fluid layer system, a gas reforming furnace and a reducing furnace, and making iron ore grains and hydrocarbon flow through in order. CONSTITUTION:Iron ore grains are heated by a heater 1, and after that, are fed to a spare reducing furnace 2, and are brought into contact with hydrocarbon preheated to such an extent as it is not decomposed, by a preheater 5, and circulating gas containing oxidizing gas such as CO2, H2O, etc., which has passed through a heater 21 from a line 12. Subsequently, a part of the hydrocarbon is decomposed and becomes reduced gas, and a part by-produces C and sticks onto the surface of iron ore grains, and the iron ore grains are prereduced. The C stuck grains are fed to a gas reforming furnace 3 together with decomposed gas which has passed through a purifying device 18, and a part of reduced iron of a reducing furnace 4, and the decomposed gas is reformed to reduced gas mainly consisting of CO, H2, etc. This reduced gas is made to pass through a heater 22, also iron ore and the reduced iron which has been partially oxidized are fed to the furnace 4 from the furnace 3 and are made to contact with each other, and reduced iron is generated, and its waste gas is fed to the furnace 2.
    • 6. 发明专利
    • Direct reduction type steel processing
    • 直接还原型钢加工
    • JPS5776114A
    • 1982-05-13
    • JP2795481
    • 1981-02-26
    • Kobe Steel Ltd
    • AOKI MAMORUTOMITA MASAHIROSAKO HIRONOBUKANEKO DENTAROUISHII YOSHITOMOSHIMAZAKI KATSUNORISOGA KAZUYA
    • C21B13/00
    • Y02P10/143Y02P10/212
    • PURPOSE: To reform exhaust gas into reduction gas easily without segregation of carbon by preheating exhaust gas beforehand in case of generating reduction gas for the solid phase reduction of the iron ore in the reduction furnace by reforming reaction of natural gas and exhaust gas from the reduction furnace.
      CONSTITUTION: In manufacturing the sponge iron by direct solid phase reduction of the iron ore in the reduction shaft furnace 1, after exhaust gas from the reduction furnace is cooled, removed from the dust and dehumidified by the scrubber 2, a part b' is made into the fuel for the reformer 3 and the remainder is fed to the high temperature heat exchanger 4, heated at 750W850°C. The preheated exhaust gas C is put in a high speed mixer 6 and mixed with natural gas d, and mixed gas e is fed to the reformer 3. In this case 1pts.wt. of exhaust gas is mixed with 0.2W0.25pts. wt. of natural gas, reformed in the reformer 3 at 850W950°C and fed to the reduction furnace as reduction gas f. Because reforming reaction proceeds without segregation of solid carbon, the reformer 3 can be of a small type.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过在还原炉中通过天然气和废气的重整反应产生还原炉中的铁矿石的固相还原产生还原气体的情况下,预先将废气容易地预先排放成还原气体而不会分解碳 炉。 构成:在还原炉1中通过铁矿石的直接固相还原制造海绵铁时,在来自还原炉的废气被冷却后,从灰尘中除去并通过洗涤器2除湿,制成b'部分 进入用于重整器3的燃料中,其余部分被供给到在750-850℃加热的高温热交换器4。 将预热废气C放入高速混合器6中并与天然气d混合,将混合气体e供给到重整器3中。在这种情况下为1pts.wt。 的废气与0.2-0.25pts混合。 重量 的天然气,在重整器3中在850-950℃下重整,并作为还原气体f送入还原炉。 由于重整反应不进行固体碳的分离,重整器3可以是小型的。