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    • 1. 发明专利
    • Method for producing coke for blast furnace
    • 用于生产烤炉的焦炭的方法
    • JP2011026514A
    • 2011-02-10
    • JP2009175648
    • 2009-07-28
    • Nippon Steel Corp新日本製鐵株式会社
    • NOMURA SEIJIKUBOTA MASAHIROAIHARA YOICHIIKEDA KOICHI
    • C10B57/04C10B57/06C10B57/08
    • PROBLEM TO BE SOLVED: To provide a method for producing coke for a blast furnace, the method achieving both of increase in the particle diameter of coke and increase in the coke strength.
      SOLUTION: The method for producing coke for a blast furnace comprises pulverizing a plurality of brands of raw material coals for each brand and blending the pulverized coals to obtain target coke strength DI
      150
      15 , and charging a coke oven with the blended coal to produce coke for a blast furnace. The method includes the following steps. (A)(A1) A low contraction coal material j (where j represents 1 to n and n is a natural number of 2 or more) included in the blended coal is classified by a length size into a size division i (where i represents 1 to m and m is a natural number of 2 or more); and a weight percentage Ib
      ij of each size division i with respect to the whole low contraction coal material j is measured. (A2) An influence degree Ai(-/wt.%) of the size division i on the low contraction coal material j on a coke surface breakage powder ratio D
      150
      -6 and an influence degree Ci (mm/wt.%) on a coke grain size MS are predetermined.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 待解决的问题:为了提供一种用于生产高炉焦炭的方法,该方法既实现了焦炭粒径的增加,又提高了焦炭强度。 ,并用混合煤装入焦炉,生产高炉焦炭。 该方法包括以下步骤。 (A)(A1)混合煤中包含的低收缩煤料j(其中j表示1〜n,n为2以上的自然数)分类为尺寸分割i(其中i表示 1〜m,m为2以上的自然数)。 并且测量每个尺寸部分i相对于整个低收缩煤料j的重量百分比Ib ij 。 (A2)尺寸i i对焦炭表面破碎粉末比D的低收缩煤料j的影响程度Ai( - /重量%)D 150 -6
    • 3. 发明专利
    • Method of manufacturing coke for blast furnace
    • 用于制作烤炉的焦炭方法
    • JP2010138254A
    • 2010-06-24
    • JP2008314860
    • 2008-12-10
    • Nippon Steel Corp新日本製鐵株式会社
    • KUBOTA MASAHIRONOMURA SEIJIAIHARA YOICHIIKEDA KOICHI
    • C10B57/04C10B57/00
    • PROBLEM TO BE SOLVED: To provide a method of manufacturing coke which has extremely high strength without increasing pulverized coal having the particle size of ≤0.3 mm and reducing the bulk density of blended coal.
      SOLUTION: In the method of manufacturing coke for blast furnace by pulverizing a plurality of brands of coking coals by brands, and charging the blended coal blended to be the target coke strength DI
      150
      15 into a coke furnace, an inert tissue having a length size of ≥0.6 mm is divided into a size division i (=1 to m[natural number]) in length size, the degree of influence Ai(-/volume%) to coke surface breakage powder ratio DI
      150
      -6 of the inert tissue and/or the degree of influence Bi(-/volume%) to coke volume breakage powder ratio DI
      150
      6-15 of the inert tissue are predetermined by size divisions i, and the coking coals constituting the blended coal are effectively pulverized, then are blended so as to obtain the target coke strength in consideration of the difference between the degrees of influence Ai and Bi.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 待解决的问题:提供一种制造焦炭的方法,该焦炭具有非常高的强度,而不增加粒径≤0.3mm的粉煤并降低混合煤的堆积密度。 解决方案:在通过品牌粉碎多个品牌的焦煤的高炉焦炭的制造方法中,将混合煤混合成为目标焦炭强度DI 150 15 进入焦炉,长度尺寸≥0.6mm的惰性组织被分成长度尺寸的尺寸i(= 1至m [自然数]),影响程度Ai( - / 体积%)与惰性组织的焦炭表面破碎粉末比例和/或影响程度Bi( - /体积%)对焦炭体积破碎粉末的比例(SP)= 150 -6 惰性组织的比例DI 150 6-15 由尺寸分隔i预定,构成混合煤的焦煤被有效地粉碎,然后混合,得到 目标焦炭强度考虑到影响度Ai和Bi之间的差异。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • LIQUEFACTION OF COAL
    • JPH10298557A
    • 1998-11-10
    • JP10924197
    • 1997-04-25
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • AIHARA YOICHIIMADA KUNIHIROMOCHIZUKI MICHIHARUIGUCHI KENJINOGAMI YOSHINOBU
    • C10G1/06
    • PROBLEM TO BE SOLVED: To produce a liquefied coal wherein a solvent for liquefaction of coal to be recycled is surely judged in terms of stabilization of the solvent by determining the time when each of the concentrations of specific substances contained in the solvent result in a certain convergence and hence a recovery of stabilized liquefied oil is increased and a running time required for the stabilization is lessened. SOLUTION: This method comprises the following steps: preparing a coal slurry 4 by blending coal 1 and a solvent and catalyst for liquefying coal; producing a liquefied oil by heating and pressurizing the coal slurry 4 in the presence of hydrogen 5 so as to be subjected to pyrolysis and hydrocracking reaction; fractionating the liquefied oil into a product oil, circulating solvent 14 and liquefied residuals 13 by distillation under normal and reduced pressures; hydrogenating the circulating solvent 14 by heating and pressurizing the solvent 14 in the presence of hydrogen 15 and a catalyst for solvent hydrogenation; and recyclably employing the resultant solvent in the first slurry-preparing process. In the above liquefied process, when the variation of the respective concentrations of paraffin, pyrene, biphenyl, dibenzofuran and/or anthracene falls within the range of 2% per day, the solvent in question is judged as a stabilized solvent.
    • 5. 发明专利
    • METHOD OF LIQUEFYING COAL
    • JPH08302356A
    • 1996-11-19
    • JP11198195
    • 1995-05-10
    • NIPPON STEEL CORP
    • AIHARA YOICHIKAWABATA MUTSUMAROIKEDA KOICHI
    • C10G1/06C10G1/08
    • PURPOSE: To provide a method of liquefying coal whereby the amount of heteroatom compounds produced can be reduced by determining the relationship between the N and S contents of a middle oil and those of a solvent and using an aromatic compound having a specified ring structure as the solvent which reduces the N and S contents of the middle oil to at least the target values. CONSTITUTION: A liquefied coal heavy oil having a boiling point of 350-538 deg.C is hydrogenated to prepare a bi- to tetra-cyclic aromatic compound having specified N and S contents determined from the relationship between the N and S contents of a middle oil and a solvent under the same operating conditions, and this compound is used as the solvent. A coal powder prepared so as to have a grain size of about 100 mesh or below and a water content of about 1.5wt.% is mixed with a synthetic iron sulfide catalyst and the prepared solvent to prepare a slurry. A reducing gas such as H2 is blown into the slurry, and the mixture is subjected to a liquefaction reaction under applied pressure and heat. The formed liquefied coal oil is distilled to obtain a light oil having a boiling range from ordinary temperature to 220 deg.C, a heavy oil of a boiling range from 350 to 538 deg.C, distillation residues, and a middle oil having N and S contents of at least the target values (N: 1.0% or below, and S: about 0.05% or below).
    • 6. 发明专利
    • LIQUEFACTION OF COAL
    • JPH09296179A
    • 1997-11-18
    • JP10831996
    • 1996-04-30
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • AIHARA YOICHIIMADA KUNIHIROITONAGA MASUMIIGUCHI KENJINOGAMI YOSHINOBU
    • B01J23/847B01J23/88C10G1/06
    • PROBLEM TO BE SOLVED: To stably liquefy coal at a high efficiency by mixing the coal with a solvent and a catalyst, carrying out the hydrogenolysis of the resultant slurry, providing a liquefied oil, distilling the prepared liquefied oil, controlling the feed rates of a medium oil and a heavy oil obtained by the distillation, hydrogenating the oils, affording a solvent with a constant aromatic hydrocarbon fraction and circulating the solvent for use. SOLUTION: Coal 1 is mixed with a catalyst 2 for liquefying the coal 1 and a solvent 3 for liquefying the coal 1 to provide a slurry 4, which is then heated and pressurized in the presence of hydrogen 5 to carry out the pyrolysis and hydrogenolysis reactions. Thereby, a liquefied oil is obtained, distilled under atmospheric and reduced pressures and separated into a product oil and a liquefaction residue. The feed rates of a part or all of the resultant medium oil 11 and a heavy oil 12 are controlled with a feed pump 14, etc., so as to keep the aromatic hydrocarbon fraction (fa ) of the produced solvent 3 for liquefying the coal 1 constant and hydrogenolysis is conducted by using a catalyst for hydrogenating the solvent 3 to produce the solvent 3 for liquefying the coal 1 at a constant fa . The resultant solvent 3 for liquefying the coal 1 is circulated for use in slurrying of the coal 1.