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    • 2. 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
    • LIQUEFACTION OF COAL
    • JPH09296180A
    • 1997-11-18
    • JP10831896
    • 1996-04-30
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • IKEDA KOICHIIMADA KUNIHIROMOCHIZUKI MICHIHARUIGUCHI KENJIMITA SHIGERUMIHASHI TOSHITSUGU
    • C10G1/06C10G1/08
    • PROBLEM TO BE SOLVED: To efficiently, economically and advantageously liquefy coal by mixing the coal with a solvent and a catalyst for liquefying the coal, providing a slurry, evaluating properties of contents of each reactional column comprising multistage liquefying reactional columns, regulating operating conditions for each reactional column and carrying out the hydrogenolysis. SOLUTION: For example, a sample collecting device equipped with a receiver 1, a nozzle 2 for collection, a collecting valve 4, a degassing valve 5, a sample recovering valve 6, an inert gas introduction valve 7, etc., is installed in each liquefying reactional column, etc., to collect contents of each liquefying reactional column therefrom. Properties of the contents such as coal conversion rate and a liquefied oil yield are evaluated to perform the regulation (e.g. the regulation of the reactional time, concretely regulation of the number of the liquefying reactional columns used) of operating conditions according to progress conditions of the liquefying reaction for each liquefying reactional column when mixing the coal with a solvent and a catalyst for liquefying the coal, carrying out the hydrogenolysis of the resultant coal slurry with hydrogen gas under high temperature and pressure conditions using a reactional column 3 comprising the continuous multistage liquefying reactional columns and liquefying the coal.
    • 5. 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.
    • 7. 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.
    • 8. 发明专利
    • LIQUEFCTION OF COAL
    • JPH09296182A
    • 1997-11-18
    • JP11252796
    • 1996-05-07
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • ITONAGA MASUMIIMADA KUNIHIROIGUCHI KENJI
    • C10G1/06
    • PROBLEM TO BE SOLVED: To stably liquefy coal in a constant reactional state by keeping the volume ratio of the vapor phase and a liquid and a solid phases in a reactional column constant, carrying out the hydrogenolysis of a coal slurry, providing a liquefied oil, distilling the liquefied oil, hydrogenating the resultant medium oil and heavy oil, affording a solvent and circulating the resultant solvent for use. SOLUTION: A solvent for liquefying coal is mixed with the coal and a catalyst for liquefying the coal to provide a coal slurry, which is then pressurized and heated in the presence of hydrogen. The volume ratio (Rv ) of the vapor phase and the liquid and solid phases in a mixed phase stream flowing in the container is measured with a CT sensor part 2 and a CT image reconstructing part 6 installed in the reactional column 1 and one or more of the opening of a hydrogen gas flow regulating valve 8, the opening of a coal slurry flow regulating valve 10 and the pressure of the introduced hydrogen are operated and controlled so as to keep the Rv constant. Thereby, hydrogenlysis is carried out to afford a liquefied oil, which is then distilled. Apart or all of the resultant medium oil is mixed with all of the heavy oil, heated and pressurized in the presence of a catalyst for hydrogenating the solvent and hydrogenated to provide a solvent for liquefying the coal. The resultant solvent is then circulated for use in slurrying.
    • 9. 发明专利
    • LIQUIDIZATION OF COAL
    • JPH09272875A
    • 1997-10-21
    • JP8402996
    • 1996-04-05
    • NIPPON STEEL CORPMITSUI SEKITAN EKIKA KK
    • MOCHIZUKI MICHIHARUIMADA KUNIHIROKAWABATA MUTSUMAROIGUCHI KENJISAKAWAKI KOJITAKEDA TETSUYA
    • C10G1/06
    • PROBLEM TO BE SOLVED: To provide a method for liquidizing coal by liquidizing the coal in the presence of hydrogen gas at a high temperature and at a high pressure, capable of profitably liquidizing the various kinds of coal in a high liquidization yield by controlling the conditions of the liquidization reaction so that the average retention time of the reaction product is controlled within a proper range. SOLUTION: This method for liquidizing coal comprises injecting a tracer having an attenuation action on neutron rays into (A) a coal slurry comprising (A1 ) coal, (A2 ) a solvent for the liquidization and (A3 ) a catalyst for the liquidization at the inlet of (Z) a liquidization reaction tower 17, measuring the concentrations of the tracer with time tracer concentration-measuring devices 22 provided with neutron ray-irradiating members and neutron ray-detecting members 21, 23, 24 disposed at the exits of the towers Z 17, 18, 19, determining the average retention times of the tracer in the towers Z 17, 18, 19, controlling the amounts of the hydrogen gas blown from the lower parts of the towers Z 17, 18, 19 into the towers, simultaneously heating and pressing the coal slurry A to hydrocrack the coal A1 into a liquidated oil, distilling the obtained liquidized oil into a product oil and a heavy oil, producing the solvent A2 from the heavy oil, and subsequently recycling the solvent A2 to the raw material of the coal A.