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
    • 3. 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.
    • 4. 发明专利
    • MEASUREMENT OF RESIDENCE TIME OF COAL SLURRY IN LIQUEFACTION TOWER AND LIQUEFACTION OF COAL THEREBY
    • JPH10298559A
    • 1998-11-10
    • JP10924097
    • 1997-04-25
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • IKEDA KOICHIIMADA KUNIHIROIGUCHI KENJINOGAMI YOSHINOBUTAKEDA TETSUYA
    • C10G1/06C10G1/08
    • PROBLEM TO BE SOLVED: To provide a method for easily measuring the residence time of coal slurry in a liquefying reaction tower under such a severe condition as high temperatures and pressures without the need of using any hard-to-estimate value, by determining the residence time grounded on a pressure difference within the tower and flow rate of the slurry at the outlet of the tower. SOLUTION: This method for measuring the residence time of coal slurry in a reaction tower for coal liquefaction, which is closely involved in the liquefying characteristics, is directed to such a coal liquefaction process that a coal, liquefying solvent and catalyst are blended for the coal slurry and a liquefying gas is fed into the resultant slurry for hydrocracking in the tower for the coal liquefaction under high temperatures and pressures, and the measurement is conducted by determining a pressure difference within the tower and flow rate of the slurry at the outlet of the tower. The pressure difference measurement is carried out e.g. by using a unit 3 composed of a couple of pressure sensing nozzles 4, 4 inserted into two vertically different positions in the tower 1 and a pressure difference sensing device 5 connected with the couple of nozzles 4, 4 to measure the pressure difference between the couple of nozzles 4, 4 a vertical length H apart from each other. The flow rate of the coal slurry is pref. estimated by sampling the slurry from inside the tower 1 to determine the amount and composition of the sample.
    • 5. 发明专利
    • METHOD OF LIQUEFYING COAL
    • JPH08302357A
    • 1996-11-19
    • JP11603895
    • 1995-05-15
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • KAWABATA MUTSUMARONAMIKI YASUKIENDO KOHEIHANADA YOSHIAKISAKAWAKI KOJINOGAMI YOSHINOBUIGUCHI KENJI
    • C10G1/06
    • PURPOSE: To provide a method of liquefying coal to produce products improved in qualities by subjecting a slurry containing coal, a solvent and a catalyst to a liquefaction reaction to obtain specified mixtures A, B and C, hydroforming mixture C, distilling the hydroformate, recovering a light oil and a middle oil, and recirculating a heavy oil. CONSTITUTION: A solvent 1, a catalyst 2, and coal 3 are mixed with each other in a slurrying tank 4 and the formed slurry is sent together with a reducing gas 5 such as hydrogen to a liquefier 6 to effect a liquefaction reaction under high-temperature and high-pressure conditions. The product is separated into a light oil 12, a middle oil 13, and a heavy oil 14 in gas/liquid separators 7-11, and the obtained liquid is separated into a heavy oil 16 and residues 17 in a vacuum distillation tower. A mixture of the light oil 12, the middle oil 13, and the heavy oil 16 are fed together with a reducing gas into a solvent hydrogenation towers 18 and 19 and reformed to obtain a mixture of a reformed light oil 12' with a reformed middle oil 13' and a reformed heavy oil 16'. The mixed modified oil is separated in atmospheric distillation towers 20, 21 and 22 to recover product light oils 23 and 24 and a product middle oil 25, and the reformed heavy oil 26 is hydrogenated to obtain a hydrogenation product recirculated as a solvent for coal slurrying.
    • 8. 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.